NOVELTY - A one organic fertilizer solid material fermentation tower, comprising cover top is set with the tower body, the tower body inner set with fermentation pool, a fermenting pool bottom is a multi-turning plate combination is formed by a bottom plate, a fermentation pool set with the walking machine, the lower part of the tower body set with a tapered hopper, the lower hopper set with a discharge wherein the lower part material wherein set with a discharging conveyor belt, a fermenting pool side wall set with a feeding conveying pipe, a feeding conveying pipe lower end set with mixing pool. This utility new type is a one organic fertilizer solid material fermentation tower, a tower body and a feeding conveying pipe, the fermentation pool and a discharging conveying belt organic combine to make the material from the add material to enter the next process of the fermentation process is simple and effective to save the time and labour cost.
NOVELTY - One organic fertilizer production with a fermenting pool, comprising preparing a cement fermentation pool, the bottom of the ferment pool set with multi-intervals of arrangement of vent pipe, the upper air pipe set with each multi-branch pipe, a vent pipe through one of integrated pipe is set on the air outlet of the fan and a fermentation pool external connection. This utility new type is a one organic fertilizer production with fermentation pool, a fermenting pool bottom part uniform arrangement multi-air pipe, use the fan through air pipe and a fermentation pool inner conveying large amount of air, in the fermentation process is for the top and the bottom of a material of good air contact, effective increase the fermentation efficiency and shortens fermentation time, and ensure the quality of fermentation.
NOVELTY - One a walking type turner, comprising walking machine frame below the machine frame set with the hopper, the hopper behind the chain turn set with polishing mechanism, the chain turn throwing mechanism is inclined set with machine frame up b, a chain turning mechanism set with a driving wheel, the driving wheel through driving connection with a drive motor is set on a machine frame, inner the feeding hopper set with a multi-, a poking wheel set on a driving device of a machine frame. This utility new type is one a walking type turner through matching work of drawing wheel and chain turning mechanism, a efficient to carry out the work of composite fertilizer for a field, with flexible and of flexibility.
NOVELTY - This utility new type claims a one water nutrition biological type large granule fertilizer, comprising with a multi-composite fertilizer granule, outside fertilizer granule is covered in a trace layer, and the element layer is covered in rear of a multi-composite fertilizer granule through between adhesive and is a whole, the outside is covered with water-retention layer, outside is covered with microorganism agent layer. This utility new type through trace layer in a multi-composite fertilizer granule outside a covering after bonding and is a whole, and then in turn coated , microorganism microbial inoculum layer, this fertilizer not only can increase fertilizer and water utilization rate, improving ecological environment, but also causes a crop balance nutrition, increasing crop yield, improving product quality, increase soil fertility, improving and repairing soil.
NOVELTY - One centrifugal granulator, comprising a foundation bed, the foundation bed set with a supporting frame, the supporting frame is set with a driving motor, a shaft of a driving motor setting one granulating cylinder, said foundation bed set with a fixed platform, the fixed platform set with a conveying belt, the conveying belt set with a lower hopper, a supporting frame is set with a dust-proof, dust-proof setting b. granulating cylinder. Combination of this utility new type is a one centrifugal granulator, use granulating cylinder and feeding device, a saving labour and time, excluding a restrain flying dust in a granulation process, avoids the pollution to production environment, sprinkling device for supply and process material in the water, the telescopic pole is used for regulating inclination angle of granulating cylinder, to adapt to different a and a, uniformly cloth point a to a fertilizer granule size is uniform, and the quality is good.
NOVELTY - The utility model relates to a high-efficiency energy-saving anaerobic fermentation tank, comprising tank body, bottom of the tank body is set with feeding pipe, feeding pipe extends into the tank body through a plurality of distributing pipes, tank body is set with overflow groove in upper part, an overflow groove and a discharging tube connected, jar body in lower from bottom to top in turn set with a level three phase separator and second level three phase separator, and through a collecting tube pneuma and pneuma pipe connected, pneuma and center pipe cylinder connected, cylinder bottom centre is higher than the discharge pipe, the bottom center through center pipe and reflux cloth-like l connected, reflowing and cloth-like l the lower jar body part. Anaerobic fermentation jar through the center cylinder and set with through centre pipe and reflux cloth-like l connected, a biogas taken pneuma of digestion liquid re-flow to jar body, fully use resource, a return liquid through the center pipe and cloth-like l in a reflow process of low flow form water flow impact force, for a material jar bottom has the function of water power stir, without need to use other power device a stir, saves the energy consumption, a fully using of material at the same time is increased.
NOVELTY - Preparing ecological bed reprocessing bio-organic fertilizer using Pleurotus eryngii waste material and cow dung comprises e.g. collecting Pleurotus eryngii mushroom and placing in frame, crushing, paving, transporting waste material and cow dung mixture into a fermenting pool of organic fertilizer plant, adding beneficial bacteria, culturing, carrying out fermentation, piling bio-organic fertilizer concentrate and carrying out secondary composting fermentation, turning stack, transferring into a stirrer and crushing into granule, and preparing nutritional element.    USE - The method is useful for preparing ecological bed reprocessing bio-organic fertilizer using Pleurotus eryngii waste material and cow dung (claimed).    ADVANTAGE - The method produces nutrient-rich organic fertilizer with high quality.    DETAILED DESCRIPTION - Preparing ecological bed reprocessing bio-organic fertilizer using Pleurotus eryngii waste material and cow dung comprises (i) collecting Pleurotus eryngii mushroom and placing in frame, (ii) taking off bag, crushing, (iii) paving, where the average thickness of 1-2 cm, (iv) transporting waste material and cow dung mixture into a fermenting pool of organic fertilizer plant, then adding beneficial bacteria and culturing and carrying out fermentation, (v) piling bio-organic fertilizer concentrate and carrying out secondary composting fermentation, (vi) turning stack in second fermentation process, (vii) then transferring into a stirrer and crushing into granule of rape seed size, (viii) preparing nutritional element, and (ix) packing using quantitative packaging machinery.
NOVELTY - Grape fertilizer comprises 5-10 pts. wt. ammonium persulfate, 3-9 pts. wt. diammonium hydrogen phosphate, 1-5 pts. wt. borax, 5-9 pts. wt. microbial fertilizer, 4-9 pts. wt. balsam pear, 6-14 pts. wt. monopotassium dihydrogen phosphate, 4-6 pts. wt. animal bone powder, 1-5 pts. wt. formic acid, 7-15 pts. wt. corn straw, 4-7 pts. wt. copper sulfate, 2-6 pts. wt. potato straw, 7-10 pts. wt. bentonite, 3-5 pts. wt. peel powder, 6-8 pts. wt. potassium dihydrogen phosphate and 9-16 pts. wt. wheat bran.    USE - Used as grape fertilizer.    ADVANTAGE - The fertilizer has long acting effect (claimed), good absorbing speed, is provided with balanced nutrition, does not cause pollution, and increases soil fertility.
NOVELTY - The biomass reaction apparatus (10) has a circulation line (14) for circulating and supplying the biomass slurry (SL), saccharification solution, and fermentation solution with respect to the reaction tank (12). A dissolved oxygen amount increase and decrease mechanism (16) is provided in the circulation line. The mechanism includes a film-degassing module (42) interposed by the branch line (46) branched from the circulation line, and a gas supply structure (44) which selectively supplies oxygen or nitrogen to the circulation line.    USE - Biomass reaction apparatus.    ADVANTAGE - Rapidly increases or decreases amount of dissolved oxygen when performing fermentation, saccharification or simultaneous fermentation and saccharification by providing the film-degassing module in the branch line, and gas supply structure which selectively supplies oxygen or nitrogen to the circulation line.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the reaction apparatus.    Biomass reaction apparatus (10)    Reaction tank (12)    Circulation line (14)    Dissolved oxygen amount increase and decrease mechanism (16)    Film-degassing module (42)    Gas supply structure (44)    Branch line (46)    Biomass slurry (SL)
NOVELTY - The after-treatment system (100) has an oxidation catalyst (130) disposed in an exhaust path (120) between an engine block (110) and a turbocharger (140). The oxidation catalyst is configured to store methane during the temperature of the first portion of an operating engine cycle and to oxidize the stored methane during the higher temperature of the second portion of the operating engine cycle.    USE - After-treatment system for use in vehicle. Uses include but are not limited to compression-ignition natural gas engine vehicle, natural gas dual fuel engine vehicle, spark ignition natural gas engine vehicle, and spark ignition natural gas stoichiometric engine vehicle (all claimed), as well as light duty trucks, medium duty trucks, heavy duty trucks, cars, motor bikes, motorcycles, boats, buses, vans, minivans, trucks, sports utility vehicles, natural gas vehicles, hybrid fuel vehicles, and multiple fuel vehicles.    ADVANTAGE - The oxidation catalyst adsorbs methane emissions at low temperatures and releases oxidized methane at high temperatures, resulting in lower methane hydrocarbon emissions. By placing the oxidation catalyst upstream of the turbocharger, the catalyst can use the same higher exhaust temperature for methane oxidation since the high temperature enhances methane reduction. The reduction in throttling loss improves fuel consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method of reducing methane emissions in a vehicle.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a natural gas engine after-treatment system.    After-treatment system (100)    Engine block (110)    Exhaust path (120)    Oxidation catalyst (130)    Turbocharger (140)
NOVELTY - The organic waste water processing system (101) has initial stage sedimentation basin (1) for separating an organic waste water into solid and liquid, and an anaerobic reactor (3) which processes the liquid unit of the initial stage sedimentation basin by an anaerobic microbe. The aerobic reactor processes the liquid unit of anaerobic reactor by anaerobic microbe, and a boiler (6) has first heating line (10a) which sends heat energy from the boiler to sludge-digestion tank (5) and second heating line (10b) which supplies portion of heat energy to the anaerobic reactor.    USE - Organic waste water processing system.    ADVANTAGE - Improves the organic matter removal rate of anaerobic reactor since the anaerobic microorganisms in the anaerobic reactor are activated by heating anaerobic reactor with surplus heat which is portion of heating gas of sludge-digestion tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic waste water processing system. (Drawing includes non-English language text).    Initial stage sedimentation basin (1)    Anaerobic reactor (3)    Sludge-digestion tank (5)    Boiler (6)    First heating line (10a)    Second heating line (10b)    Organic waste water processing system (101)
NOVELTY - The electrochemical apparatus (10) has gas supply lines (17) that supply the supply gas which generates water-vapor-electrolysis reaction or fuel cell reaction by the electrochemical cell (15) to each of the hydrogen electrode (13) and the oxygen electrode (14). The first heat exchange part (18) transmits the heat energy which arises in the electrochemical cell by water-vapor-electrolysis reaction and fuel cell reaction to the gas supply line where supply gas flows, and is provided in the inside of reaction container (11).    USE - Electrochemical apparatus.    ADVANTAGE - Exploits effectively the heat energy generated inside the apparatus by simple structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an operating method of electrochemical apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram which shows the electrochemical apparatus.    Electrochemical apparatus (10)    Reaction container (11)    Hydrogen electrode (13)    Oxygen electrode (14)    Electrochemical cell (15)    Gas supply lines (17)    First heat exchange part (18)
NOVELTY - The cell has a sealing element (16) which is arranged in one end side to seal flow paths (14A). A gas supply/collection element is arranged in other end side, so that the supplied hydrogen gas or produced reducible fuel gas is collected in flow paths. A compact element (141) is inserted in a porous support (14) at the flow paths, so that the flow paths are parted to two regions in a length direction and perpendicular width direction. The reducible fuel gas or the hydrogen gas is flowed through two regions of flow paths which are demarcated by the compact element.    USE - Electrochemical cell e.g. solid oxide fuel cell.    ADVANTAGE - The operating efficiency of the reducible fuel gas is improved, so that the generating efficiency of the fuel cell is improved. The generation efficiency of the hydrogen is improved. The electrolysis efficiency of the electrolysis cell is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of the porous support of the electrochemical cell. (Drawing includes non-English language text)    Porous support (14)    Flow paths (14A)    Sealing element (16)    Gas manifold (17)    Compact element (141)
NOVELTY - Device for producing organic substance comprises (a) syngas generation furnace, (b) organic-substance-synthesizing unit, (c) moisture-content-increasing unit, and (d) moisture-content-reducing unit.    USE - The device is useful for producing organic substance (claimed).    DETAILED DESCRIPTION - Device for producing organic substance comprises (a) syngas generation furnace, (b) organic-substance-synthesizing unit, (c) moisture-content-increasing unit, and (d) moisture-content-reducing unit, where the syngas generation furnace generates carbon dioxide-containing syngas by partially oxidizing a carbon source, organic-substance-synthesizing unit generates an organic substance from the syngas, moisture-content-increasing unit is arranged between the syngas generation furnace and organic-substance-synthesizing unit and increases moisture content of the syngas, and moisture-content-reducing unit is arranged between the moisture-content-increasing unit and organic-substance-synthesizing unit and reduces moisture content of syngas. An INDEPENDENT CLAIM is included for method of producing organic substance, which involves (a) producing syngas by partially oxidizing a carbon source in the syngas generation furnace, (b) generating organic substance from the syngas, and (c) reducing and/or increasing the moisture content of the syngas to obtain product.
NOVELTY - The system (100) has computing devices determining a concentration of respective gas using comparison of three signals which are converted to electrical signals. The computing devices are isolated from ambient air in which hazardous gases potentially exist in significant concentration or quantity. Gas sensor heads (101) are arranged in locations in which hazardous gases potentially exist in ambient air. Laser driver modules (102) and photodetectors are communicatively coupled to the gas sensor heads by a connection which includes a fiber optic cable (113).    USE - Fiber optic gas sensing system for sensing gases e.g. methane, carbon monoxide and carbon dioxide (all claimed), in coal mines.    ADVANTAGE - The system is provided in which electrical components and the signals can be provided remote from combustible gases, thus eliminating a risk of explosions from sparks or electrical discharges. The sensor head is provided with improved expandability and robustness, while defining a gas chamber that is vibration/impact insensitive and dust/water vapor proof in nature. The system ensures that computer controlled voltage bias provides reduced system complexity, reduced maintenance improved signal-to-noise ratio (SNR), improved accuracy, reliability, simplicity, precision and convenience.    DETAILED DESCRIPTION - The three signals are direct signals (108) and optical signals (109, 109', 109'', 110). An INDEPENDENT CLAIM is also included for a method for detecting and determining concentration of gases.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a gas sensing system for detecting gases.    Gas sensing system (100)    Gas sensor heads (101)    Laser driver modules (102)    Direct signals (108)    Optical signals (109, 109', 109'', 110)    Fiber optic cable (113)
NOVELTY - This utility model claims a plasma exhaust gas treatment device, comprising orderly connected of a plasma exhaust gas treatment furnace, metal fiber sintered felt filter and low temperature plasma waste gas treatment unit. This utility new type using the high temperature of a plasma, a collective characteristics realize the high efficiency process of waste gas treatment, using the compactness of metal fiber sintered felt filtering core, steady performance, long service life of a solid mixed gas of a pneuma; using the active group of low temperature plasma final purification. The effluent after a of this utility new type processing device is the collection of dust and solid by main is divided into carbon dioxide, gaseous water one of mixed gas, after processing a waste pneuma final product does not has a second time pollute problem, this utility new type claims of a plasma and the metal fiber sintered felt filtering combine technology, a process gas supply is ideal.
NOVELTY - The device has a cylindrical pool body (1) whose center part is fixed with a conical reaction tube (2) that is fixed with a cylindrical peripheral clapboard (3). The conical reaction tube is fixed with a reaction room (4). The cylindrical peripheral clapboard is fixed with the cylindrical pool body. The conical reaction tube is fixed with a multi-layer reaction cylinder mesh part (7). Another reaction room (5) is fixed with a multi-layer baffle plate (16). An upper inner wall of the cylindrical pool body is formed with a water groove (15).    USE - Aerobic granule sludge integrated sewage treating device.    ADVANTAGE - The device is inexpensive and convenient to assemble and operate, and occupies less space, reduces treating cost and increases water quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an aerobic granule sludge integrated sewage treating method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an aerobic granule sludge integrated sewage treating device.    Cylindrical pool body (1)    Conical reaction tube (2)    Cylindrical peripheral clapboard (3)    Reaction rooms (4,5)    Multi-layer reaction cylinder mesh part (7)    Water groove (15)    Multi-layer baffle plate (16)
NOVELTY - Organic fertilizer preparation involves mixing 300 pts. wt. palm tree essence solution (5-10%), 40 pts. wt. bamboo extract solution (5-10%) and 60 pts. wt. bamboo stem cell. Distilled water is added to the obtained material, and then stirred uniformly at 35-40 degrees C for 7-8 hours. The obtained mixture is mixed with 190 pts. wt. tomato essence solution and 10 pts. wt. stem cells. Distilled water is added to the obtained material, and then stirred uniformly. The obtained mixture is fermented at 35-40 degrees C for 7-9 hours.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer that is safe.    DETAILED DESCRIPTION - Organic fertilizer preparation involves mixing 300 pts. wt. palm tree essence solution (5-10%), 40 pts. wt. bamboo extract solution (5-10%) and 60 pts. wt. bamboo stem cell. Distilled water is added to the obtained material, and then stirred uniformly at 35-40 degrees C for 7-8 hours. The obtained mixture is mixed with 190 pts. wt. tomato essence solution and 10 pts. wt. stem cells. Distilled water is added to the obtained material, and then stirred uniformly. The obtained mixture is fermented at 35-40 degrees C for 7-9 hours. Duckweed extract (180 pts. wt.) and duckweed dry cell (10 pts. wt.) are added in the obtained mixture. Distilled water is added to the obtained material, and then stirred uniformly. The obtained mixture is fermented at 35-40 degrees C for 7-9 hours. Parasitic plant essence (100 pts. wt.) and parasitic plant stem cells (10 pts. wt.) are added in the obtained mixture. Distilled water is added to the obtained material, and then stirred uniformly. The obtained mixture is fermented at 35-40 degrees C for 6-8 hours. Milk (100 pts. wt.) is added in the obtained mixture. Distilled water is added to the obtained material, and then stirred uniformly. The obtained mixture is fermented at 30-35 degrees C for 7 days to obtain organic fertilizer.
NOVELTY - Preparing R-1-(3,4-dimethylphenyl) ethanol, comprises sequentially adding p-chlorophenol, dicyclohexylcarbodiimide and 4-dimethylaminopyridine in a dichloromethane and then stirring at normal temperature, filtering and concentrating to obtain pure p-chlorophenol ester, adding p-chlorophenol ester in toluene, adding 1-(3,4-dimethylphenyl) ethyl alcohol in a shaker and filtering using column chromatography to obtain R-1-(3,4-dimethylphenyl) ethanol ester, adding alcohol and lithium hydroxide to 10 times the volume amount of obtained product, heating, then converting, drying and concentrating.    USE - The method is useful for preparing R-1-(3,4-dimethylphenyl) ethanol (claimed).    ADVANTAGE - The method is capable of preparing R-1-(3,4-dimethylphenyl) ethanol using easily available raw materials with high yield and selectivity under mild condition in an environmentally-friendly manner.    DETAILED DESCRIPTION - Preparing R-1-(3,4-dimethylphenyl) ethanol or its ester, comprises sequentially adding chlorophenol, dicyclohexylcarbodiimide and 4-dimethylaminopyridine in a dichloromethane in a mass ratio of 1:1-1.2:1-1.2:0.01-0.05 and then stirring at normal temperature, filtering and concentrating to obtain pure p-chlorophenol ester, adding p-chlorophenol ester in toluene in a mole ratio of 1:1-1.5, adding 5-20 mass% of 1-(3,4-dimethylphenyl) ethyl alcohol in a shaker at 35-70 degrees C and filtering using column chromatography to obtain R-1-(3,4-dimethylphenyl) ethanol ester with a purity of more than 99%, adding alcohol and lithium hydroxide to 10 times the volume of obtained product in a mass ratio of 1:1 and heating, then converting, drying and concentrating.
NOVELTY - Preparing R-1-(3-chlorophenyl) ethanol, comprises sequentially adding chlorophenol, dicyclohexylcarbodiimide and 4-dimethylaminopyridine in a dichloromethane and then stirring at normal temperature, filtering and concentrating to obtain pure p-chlorophenol ester, adding p-chlorophenol ester in toluene, adding 1-(3,4-chlorophenyl) ethyl alcohol in a shaker and filtering using column chromatography to obtain R-1-(3,4-chlorophenyl) ethanol ester, adding alcohol and lithium hydroxide to 10 times the volume amount of obtained product heating and then converting, drying and concentrating.    USE - The method is useful for preparing R-1-(3-chlorophenyl) ethanol (claimed).    ADVANTAGE - The method is capable of preparing the R-1-(3-chlorophenyl) ethanol using easily obtainable raw materials, with high yield and selectivity, under mild condition in an environmentally-friendly manner.    DETAILED DESCRIPTION - Preparing R-1-(3-chlorophenyl) ethanol or its ester, comprises sequentially adding chlorophenol, dicyclohexylcarbodiimide and 4-dimethylaminopyridine in a dichloromethane in a mass ratio of 1:1-1.2:1-1.2:0.01-0.05 and then stirring at normal temperature, filtering and concentrating to obtain pure p-chlorophenol ester, adding p-chlorophenol ester in toluene in a mole ratio of 1:1-1.5, adding 5-20 mass% of acidic resin and lipase in a shaker at 35-70 degrees C and filtering using column chromatography to obtain R-1-(3,4-chlorophenyl) ethanol ester with purity of more than 99%, adding alcohol and lithium hydroxide to 10 times the volume amount of obtained product in a mass ratio of 1:1 and heating, and then converting, drying and concentrating.
NOVELTY - Preparing N-(5-(4-bromophenyl)-6-chloro-4-pyrimidinyl)-N'-propyl sulfonamide (I) comprises adding N-propyl sulfonamide and 5-(4-bromophenyl)-4,6-dichloropyrimidine to an organic solvent, then adding alkoxy metal compound (A) and stirring the mixture to react.    USE - (I) is useful as intermediate for preparing temazepam.    ADVANTAGE - The one-pot method is capable of preparing (I) with high yield and purity, reduced solvent dosage and cost, and without using N-propyl sulfonamide potassium salt, hence eco-friendly.    DETAILED DESCRIPTION - Preparing N-(5-(4-bromophenyl)-6-chloro-4-pyrimidinyl)-N'-propyl sulfonamide (I) comprises adding N-propyl sulfonamide and 5-(4-bromophenyl)-4,6-dichloropyrimidine to an organic solvent, then adding alkoxy metal compound of formula (ROM) (A) and stirring the mixture to react.    R = 1-4C = 1-4C alkoxy, preferably tert-butyl, ethyl and/or propyl; and    M = first main group element of periodic table, preferably K or Na.
NOVELTY - Preparing a dicoumarin compound comprises reacting a 4-hydroxycoumarin compound with an aromatic aldehyde compound such as pyridine-4-carbaldehyde, 1,3-benzodioxole-5-carbaldehyde, furan-2-carbaldehyde, (E)-3-phenylprop-2-enal or an aldehyde compound (I) in the presence of an aqueous catalytic system of choline type ionic liquid and a solvent, and heating the mixture to 25-70 degrees C under normal pressure condition.    USE - The process is useful for preparing a dicoumarin compound (claimed).    ADVANTAGE - The process is capable of simply and economically preparing the dicoumarin compound with high yield using inexpensive, non-toxic and biocompatible reagents and catalyst having high catalytic activity and good heat stability and without using organic solvent, thus reducing environmental pollution.    DETAILED DESCRIPTION - Preparing a dicoumarin compound comprises reacting a 4-hydroxycoumarin compound with an aromatic aldehyde compound comprising a benzaldehyde compound of formula (I), pyridine-4-carbaldehyde of formula (II), (E)-3-phenylprop-2-enal of formula (III), 1,3-benzodioxole-5-carbaldehyde of formula (IV) or furan-2-carbaldehyde of formula (V) in the presence of an aqueous catalytic system of choline type ionic liquid and a solvent, and heating the mixture to 25-70 degrees C under normal pressure condition. The choline type ionic liquid is 2-hydroxyethyl(trimethyl)ammonium of formula (i), 2-hydroxyethyl(dimethyl)ammonium of formula (ii), hydroxyl ion (OH-), acetate ion (CH3COO-), lactate ion (CH3CH(OH)COO-) or bisulfate ion (HSO4-).    X = phenyl (substituted with F, Cl, Br, OH, NO2, CH3, CF3, OCH3 or CHO) or H.
NOVELTY - Producing fermented compost, comprises (i) drying coffee waste until moisture content of 40-50%, (ii) adding 5-6 pts. wt. microorganisms and 5-6 pts. wt. amino acid into 100 pts. wt. dried coffee waste, and (iii) fermenting the dried coffee.    USE - The fermented compost is useful for inhibiting tetranychus urticae, mulberry thrips, greenhouse white fly, caterpillar, fall armyworm, maggot, lace bug, moth fly, coccid, maggot or Paratrechina longicornis (claimed).    ADVANTAGE - The compost has 75% insecticidal activity compare to regular compost (all claimed), and is environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for fermented compost produced by the above method.
NOVELTY - Producing compost for horticulture using coffee waste, comprises (a) drying coffee waste such that the coffee waste has moisture content of 40-50%, (b) adding 5-6 pts. wt. microorganisms and 5-6 pts. wt. amino acids to 100 pts. wt. dried coffee waste, and (c) fermenting.    USE - The method is useful for producing compost for horticulture using coffee waste to reduce generation of gas including at least one of ammonia, hydrogen sulfide, methyl sulfide, mercaptan, trimethylamine, acetaldehyde, propionaldehyde, butyraldehyde, valeraldehyde, isobutanol, ethyl acetate, methyl isobutyl ketone, toluene, styrene, xylene, propionic acid, valeric acid, butyric acid and alcohol (all claimed).    ADVANTAGE - The coffee waste compost reduces generation of odor, and recycles coffee waste and so is environmentally friendly. Test details are described but no results given.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for compost for horticulture using coffee waste, produced using the above method.
NOVELTY - This utility model relates to marsh gas collection system. The marsh gas collecting system comprises refuse landfill, wherein the landfill place of gas collecting bottle, pipe device and intelligent control device, the gas collecting bottle through the pipeline device and the intelligent control device connected with. The intelligent control device includes in turn connected with the power detection device, intelligent controller and control part, the detecting device and the controller are setting on the pipeline device. This new utility model provided by the marsh gas collecting system has high security, suitable urgency process, can remote control and it saves the resource.
NOVELTY - Harvested straw is cut, immersed in boiling water and acetic acid is added, water-washed and dried. Dilute sulfuric acid and straw are reflux-extracted and filtered. Calcium hydroxide and dilute sulfuric acid are added to filtrate, and magneton is added, heated and filtered, to obtain filtrate. The filtrate is heated and concentrated, to obtain lignocellulose solution. Wood cellulase is added to lignocellulose solution, concentrated and stirred, to obtain sugar liquid. The obtained precipitate is filtered, washed and dried, to obtain material used as gauze packing for domestic desiccant.    USE - Recycling of straw (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly recycling of straw, within short period of time.    DETAILED DESCRIPTION - Harvested straw is cut to length of 3-6 cm, immersed in boiling water at 90-95 degrees C, and acetic acid is added and soaked for 15 minutes. The soaked straw is water-washed for 3-5 times and dried in sun for 2-3 hours. 1 mol.L-1 Dilute sulfuric acid and straw are provided to continuous reflux extraction apparatus, reflux-extracted at 80-90 degrees C for 3-10 hours and filtered. The amount of sulfuric acid covers the straw. Calcium hydroxide and dilute sulfuric acid are added to filtrate, and magneton is added, heated at 90-95 degrees C with stirring such that precipitate is not formed and filtered, to obtain filtrate. The filtrate is heated in condensing pipe and concentrated, to obtain lignocellulose solution. Wood cellulase is added to lignocellulose solution, concentrated and magneton is added and stirred at 35-45 degrees C, to obtain sugar liquid. The filtrate residue is immersed in aqueous ammonia for 30 minutes, water-washed for 3-5 times, dried in sun, ground in mill and mixed with dry corn, to obtain mixture used as poultry feed. The precipitate is filtered, water-washed and dried, to obtain material used as gauze packing for domestic desiccant.
NOVELTY - Shampoo comprises 12-18 pts. wt. Angelica, 3-7 pts. wt. collagen amino acid, 5-12 pts. wt. citric acid, 7-11 pts. wt. oriental arborvitae, 6-9 pts. wt. cortex dictamni, 10-15 pts. wt. radix sophorae flavescentis, 9-15 pts. wt. saponins, 4-8 pts. wt. coconut oil acid monoethanolamide, 1-7 pts. wt. sodium lauryl sulfate, 8-16 pts. wt. tea seed, 8-12 pts. wt. Polygonum multiflorum, 0.25-1.25 pts. wt. essence, 2-7 pts. wt. mulberry bark, and 55-79 pts. wt. water.    USE - Shampoo.    ADVANTAGE - The shampoo has scientific and reasonable formulation, has simple process without pollution, is easy to rinse, provides hair with luster, pliancy and elasticity, and has anti-dandruff and antipruritic effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of shampoo by extracting Angelica, oriental arborvitae, cortex dictamni, radix sophorae flavescentis, saponin, tea seed, P. multiflorum, and mulberry bark with 3 times amount water to obtain liquid mixture A; filtering liquid mixture; concentrating filtrate to \6 of original volume; adding collagen amino acids, citric acid, coconut oil acid monoethanolamide, and sodium lauryl sulfate; uniformly stirring; filtering to obtain filtrate; adding filtrate with essence; and stirring well to obtain shampoo.
NOVELTY - Bacterial composition comprises 10-20 pts. wt. Bacillus subtilis, 10-25 pts. wt. Bacillus coagulans, 10-20 pts. wt. Bacillus megaterium, 15-25 pts. wt. Trichoderma viride, and 10-30 pts. wt. Trichoderma reesei.    USE - The bacterial composition is useful for preparing an organic fertilizer (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) producing the bacterial composition comprising inoculating Bacillus subtilis, Bacillus coagulans, Bacillus megaterium, Trichoderma viride and Trichoderma reesei strains in a high density culture medium with shaker flask, where the strains are inoculated at a volumetric ratio of 15-30%, inoculating the cultured strains into a fermentation tank, and drying the strain culture; and (2) preparing an organic fertilizer comprising (a) mixing cattle or sheep excrement with rice hull and adding 1-2 kg/ton of bacterial composition with uniformly mixing to obtain mixed raw material with a moisture content of 50-65 wt.%, (b) placing the mixed raw material in a strip-shaped fertilizer stack, maintaining the temperature at 55-65 degrees C, carrying out fermentation process, where the mixture is turned once for every 12 days of fermentation, and maintaining the moisture content to 50-65 wt.% during fermentation, and (c) after the fermentation temperature is dropped to room temperature, obtaining the organic fertilizer with a moisture content of 20-30 wt.%.
NOVELTY - The hydrolysis photoelectrochemistry cell comprises an electrolyte (30) that is connected with a photoelectrode (20). The photoelectrode is connected with a nanostructure semiconductor layer (21) that is formed on the substrate (10). A cathode (40) is connected to the photoelectrode that is equipped within the external circuit (50). A free pattern layer is formed on the substrate. A nano-particle layer is formed within the photoelectrode. The electrolyte is connected with the side portion of the cathode.    USE - Hydrolysis photoelectrochemistry cell for use as energy source.    ADVANTAGE - The cathode is connected to the photoelectrode that is equipped within the external circuit, where a free pattern layer is formed on the substrate, and thus enhances the hydrogen production efficiency of the hydrolysis photoelectrochemistry cell, enhances the reproducibility and reliability of the hydrolysis photoelectrochemistry cell, reduces the manufacture unit cost of the nanostructure, and hence facilitates the regulation of population density of the nanostructure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing method for a hydrolysis photoelectrochemistry cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a hydrolysis photoelectrochemistry cell.    Substrate (10)    Photoelectrode (20)    Nanostructure semiconductor layer (21)    Electrolyte (30)    Cathode (40)    External circuit (50)
NOVELTY - Bio-fertilizer comprises 137.5-165 pts. wt. diammonium phosphate, 62.5-75 pts. wt. ammonium chloride, 350 pts. wt. organic fertilizer, 50-100 pts. wt. humic acid residue, and 1 pt. wt. microbial composition. The organic fertilizer is prepared by fermenting mixture of chicken manure, zeolite powder and calcium chloride.    USE - The bio-fertilizer is useful for fish, preferably silver carp (claimed).    ADVANTAGE - The fertilizer contains 12% nutrients and 85% organic matter (dry weight), accelerates growth rate of fish, and prevents disease of fish.
NOVELTY - This utility new type provide the one a hydrogen oxygen gas happen device, comprising a shell, a multi-pole plate group and lower shell, said electrode group including one upper top plate, a middle plate and one multi-lower plate, each said plate group independently of a form is one large rooms, in the electrode group of each two adjacent of a plate form one small electrolytic room, the upper plate, middle plate and lower plate are set with a cylindrical of the pneuma channel and the water channel. Corrosion protecting Therefore, this utility new type can flexibly control size and efficiency of electrolysis electromotive force, and hydrogen produce efficiency, and plate of high property, insulation property of insulation pad, electrolytic water and a flow rate of hydrogen oxygen gas is fast, it can produce b each suitable for a different power to a vehicle, and provide more rapid, better is hydrogen oxygen gas.
NOVELTY - Purification of feed water (1) containing contaminants involves passing feed water containing contaminants through an anion exchange resin (2) to capture contaminants, periodically regenerating the resin by passing regenerant fertilizer solution (5) including one or more inorganic salts through the resin to release contaminants from the resin into the regenerant fertilizer solution, rinsing the resin of residual regenerant solution by passing rinse solution through the resin, and isolating the regenerant and rinse solution from the resin to provide an enhanced fertilizer solution.    USE - Purification of feed water used for preparing enhanced fertilizer solution (claimed) used as fertilizer for crops e.g. fruits, vegetables, grains, turf grasses, and other horticultural and agricultural products.    ADVANTAGE - The method enables economical, efficient, and environmentally-friendly purification of feed water.    DETAILED DESCRIPTION - Purification of feed water containing contaminants involves passing preset volume of the feed water containing contaminants through an anion exchange resin to capture contaminants on the resin, periodically regenerating the resin by passing preset volume of regenerant fertilizer solution including one or more inorganic salts through the resin to release contaminants from the resin into the regenerant fertilizer solution, rinsing the resin of residual regenerant solution by passing preset volume of rinse solution through the resin, and isolating the regenerant and rinse solution from the resin to provide an enhanced fertilizer solution. An INDEPENDENT CLAIM is included for preparation of enhanced fertilizer solution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of water treatment system.    Feed water (1)    Anion exchange resin (2)    Treated stream (3)    Service resin (4)    Regenerator fertilizer solution (5)
NOVELTY - This utility new type provide a fermentation jar used for manufacturing technology of humic acid, belongs to the fermentation technology field, comprising a tank body and a stir, the jar body set with a sludge has injection tube, alkali liquid injection pipe, a sludge discharging pipe and used for discharging after fermenting the supernatant obtained is derive material tube, a stir device comprise motor, rotation axis by driving a motor and stir target set with the rotation axis a is b, the stir target comprising transverse pole and the vertical rod along the rod length direction interval is set, a cross pole and the vertical rod through a detachable bolt connection. The fermentation jar has set with stir device and raise temperature system, the fermentation speed is fast, a short, for use of domestic sludge is high, effective solves the problem that the acid used for manufacturing process of fermenting jar fermentation speed is slow, and a ferment is not capable of fully problem.
NOVELTY - Preparing castelanone comprises crushing Castela tweedii, ultrasonically extracting with ethanol solution, concentrating the extract to dryness to obtain ethanol extract, extracting crude extract with ethyl acetate, filtering, vacuum concentrating filtrate to obtain a liquid concentrate, volatilizing solvent to dryness, eluting in a silica gel column by dichloromethane-methanol gradient elution, tracking and monitoring by thin layer chromatography (TLC), collecting castelanone eluent, processing high speed counter-current chromatography, separating, purifying, and freeze-drying.    USE - The castelanone is useful in intestinal absorption accelerator containing medium chain fatty acid salt, bile salts, chenodeoxycholic acid salt and chitosan or its derivative (claimed) and preventing tumor.    ADVANTAGE - The method: is simple and environmentally friendly; produces product, which has high purity and yield and increases biological utilization degree.    DETAILED DESCRIPTION - Preparing castelanone comprises (a) crushing Castela tweedii, ultrasonically extracting with ethanol solution, concentrating the extract to dryness to obtain Castela tweedii ethanol extract, (b) extracting crude extract with ethyl acetate, filtering, vacuum concentrating filtrate to obtain a liquid concentrate, (c) volatilizing solvent to dryness, eluting the liquid concentrate in a silica gel column, by dichloromethane-methanol gradient elution, tracking and monitoring by thin layer chromatography (TLC), and collecting castelanone eluent, and (d) removing liquid concentrate by high speed counter-current chromatography method, separating, purifying, and freeze-drying.
NOVELTY - Extracting Sanguisorba officinalis, involves cutting S.officinalis, placing the cut raw material into a high speed tissue triturator and passing through 60 meshes sieve, adding ethyl alcohol aqueous solution and cellulase, carrying out enzymolysis, extracting the enzymolyzed mixture, filtering the extract, concentrating the filtrate, then subjecting to high pressure silica gel column chromatography, eluting the product, concentrating, cooling and crystallizing to obtain coarse product and then recrystallizing to obtain the product.    USE - The method is useful for extracting S.officinalis (claimed).    ADVANTAGE - The method is simple, rapid and environmentally-friendly, and consumes less energy.    DETAILED DESCRIPTION - Method of extracting pomolic acid, involves cutting S.officinalis, placing the cut raw material into a high speed tissue triturator and processing at 18000 rotations/minute for 5 minutes, then passing through 60 meshes sieve, adding ethyl alcohol aqueous solution and 0.5% cellulase enzyme, carrying out enzymolysis for 70-120 minutes under ultrasonic power of 500 W at 45 degrees C, extracting the enzymolyzed mixture, filtering the extract, concentrating the filtrate, then subjecting to high pressure silica gel column chromatography, eluting the product, concentrating, cooling and crystallizing to obtain coarse product and then recrystallizing to obtain the product.
NOVELTY - Processing heavy metal polluted soil involves spraying insecticide, enriching soil with earthworms and decompositing soil with microbe.    USE - Method for processing heavy metal polluted soil (claimed).    ADVANTAGE - The method enables to process heavy metal polluted soil in simple manner.
NOVELTY - Medicinal fertilizer comprises 1-4 pts. wt. pomegranate leaves, 5-9 pts. wt. locust leaves, 15-25 pts. wt. peach leaves and 3-5 pts. wt. wheat bran, and prepared by cleaning pomegranate, locust and peach leaves with aqueous sodium chloride solution. The cleaned leaves are dried and then stirred with wheat bran to obtain mixture that is boiled with water. The boiled mixture is covered with plastic thin film for fermentation. The fermented product is mixed with edible alcohol (3-4 ml), glucose (0.4g), yeast paste, calcium carbonate (1.5g), agar (1.5g) and water (100g) to obtain another mixture.    USE - Medicinal fertilizer.    ADVANTAGE - The medicinal fertilizer is green, and helps in waste recycling.    DETAILED DESCRIPTION - Medicinal fertilizer comprises 1-4 pts. wt. pomegranate leaves, 5-9 pts. wt. locust leaves, 15-25 pts. wt. peach leaves and 3-5 pts. wt. wheat bran, and prepared by cleaning pomegranate, locust and peach leaves with aqueous sodium chloride solution. The cleaned leaves are dried and then stirred with wheat bran to obtain mixture that is boiled with water. The boiled mixture is covered with plastic thin film for fermentation. The fermented product is mixed with edible alcohol (3-4 ml), glucose (0.4g), yeast paste, calcium carbonate (1.5g), agar (1.5g) and water (100g) to obtain another mixture that is kept at 30 degrees C for 2 days to obtain product, which is stored at 4 degrees C.
NOVELTY - Medicinal fertilizer comprises 3-8 pts. wt. pepper leaves, 8-13 pts. wt. pomegranate leaves, 5-15 pts. wt. willow leaves, 5-15 pts. wt. peach leaves and 1-5 pts. wt. bran, and prepared by cleaning pepper, willow, pomegranate and peach leaves with aqueous sodium chloride solution. The cleaned leaves are dried and then stirred with bran to obtain mixture that is boiled with water. The boiled mixture is covered with plastic thin film for fermentation. The fermented product is mixed with edible alcohol (3-4 ml), glucose (0.4g), yeast paste, calcium carbonate (1.5g), agar (1.5g) and water (100g).    USE - Medicinal fertilizer.    ADVANTAGE - The medicinal fertilizer is green and eco-friendly, and ensures low carbon and soil restoration.    DETAILED DESCRIPTION - Medicinal fertilizer comprises 3-8 pts. wt. pepper leaves, 8-13 pts. wt. pomegranate leaves, 5-15 pts. wt. willow leaves, 5-15 pts. wt. peach leaves and 1-5 pts. wt. bran, and prepared by cleaning pepper, willow, pomegranate and peach leaves with aqueous sodium chloride solution. The cleaned leaves are dried and then stirred with bran to obtain mixture that is boiled with water. The boiled mixture is covered with plastic thin film for fermentation. The fermented product is mixed with edible alcohol (3-4 ml), glucose (0.4g), yeast paste, calcium carbonate (1.5g), agar (1.5g) and water (100g) to obtain another mixture that is kept at 30 degrees C for 2 days to obtain product, which is stored at 4 degrees C.
NOVELTY - Medicinal fertilizer comprises 2-3 pts. wt. pepper leaves, 1.5-3 pts. wt. willow leaves, 10-25 pts. wt. poplar leaves, 7-15 pts. wt. phoenix tree leaves, 2.5-6 pts. wt. Cedrela sinensis leaves and 5-10 pts. wt. rice hull, and prepared by cleaning pepper, willow, poplar, phoenix and Cedrela sinensis leaves with aqueous sodium chloride solution. The cleaned leaves are chaffed and then stirred with vinegar to obtain mixture that is boiled with water. The boiled mixture is mixed wit rice hull and then covered with plastic thin film for fermentation.    USE - Medicinal fertilizer.    ADVANTAGE - The medicinal fertilizer is eco-friendly, and helps in waste recycling and supplies nutrients of rice hull.    DETAILED DESCRIPTION - Medicinal fertilizer comprises 2-3 pts. wt. pepper leaves, 1.5-3 pts. wt. willow leaves, 10-25 pts. wt. poplar leaves, 7-15 pts. wt. phoenix tree leaves, 2.5-6 pts. wt. Cedrela sinensis leaves and 5-10 pts. wt. rice hull, and prepared by cleaning pepper, willow, poplar, phoenix and Cedrela sinensis leaves with aqueous sodium chloride solution. The cleaned leaves are chaffed and then stirred with vinegar to obtain mixture that is boiled with water. The boiled mixture is mixed wit rice hull and then covered with plastic thin film for fermentation. The fermented product is mixed with edible alcohol (3-4 ml), glucose (0.4g), yeast paste, calcium carbonate (1.5g), agar (1.5g) and water (100g) to obtain another mixture that is kept at 30 degrees C for 2 days to obtain product, which is stored at 4 degrees C.
NOVELTY - Medicinal fertilizer comprises 5-10 pts. wt. willow leaves, 7-15 pts. wt. pear leaves, 10-25 pts. wt. tung tree leaves and 10-30 pts. wt. corn cob, and prepared by cleaning willow, pear and tung tree leaves with aqueous sodium chloride solution. The cleaned leaves are dried and then stirred with corn cob and vinegar to obtain mixture that is boiled with water. The boiled mixture is covered with plastic thin film for fermentation. The fermented product is mixed with edible alcohol (3-4 ml), glucose (0.4g), yeast paste, calcium carbonate (1.5g), agar (1.5g) and water (100g).    USE - Medicinal fertilizer used for conditioning soil (claimed).    ADVANTAGE - The medicinal fertilizer is eco-friendly, and supplies nutrients of corn cob.    DETAILED DESCRIPTION - Medicinal fertilizer comprises 5-10 pts. wt. willow leaves, 7-15 pts. wt. pear leaves, 10-25 pts. wt. tung tree leaves and 10-30 pts. wt. corn cob, and prepared by cleaning willow, pear and tung tree leaves with aqueous sodium chloride solution. The cleaned leaves are dried and then stirred with corn cob and vinegar to obtain mixture that is boiled with water. The boiled mixture is covered with plastic thin film for fermentation. The fermented product is mixed with edible alcohol (3-4 ml), glucose (0.4g), yeast paste, calcium carbonate (1.5g), agar (1.5g) and water (100g) to obtain another mixture that is kept at 30 degrees C for 2 days to obtain product, which is stored at 4 degrees C.
NOVELTY - Medicinal fertilizer comprises 2-10 pts. wt. peach leaves, 4-10 pts. wt. apple leaves, 10-20 pts. wt. birch leaves and 10-30 pts. wt. soybean straw, and is prepared by cleaning peach, apple and birch leaves with aqueous sodium chloride solution. The cleaned leaves are dried and stirred with soybean straw and vinegar to obtain mixture that is boiled with water. The boiled mixture is covered with plastic thin film for fermentation. The fermented product is mixed with edible alcohol (3-4 ml), glucose (0.4g), yeast paste, calcium carbonate (1.5g), agar (1.5g) and water (100g).    USE - Medicinal fertilizer.    ADVANTAGE - The medicinal fertilizer is green and eco-friendly, and helps in waste recycling and supplies nutrients of soybean straw.    DETAILED DESCRIPTION - Medicinal fertilizer comprises 2-10 pts. wt. peach leaves, 4-10 pts. wt. apple leaves, 10-20 pts. wt. birch leaves and 10-30 pts. wt. soybean straw, and is prepared by cleaning peach, apple and birch leaves with aqueous sodium chloride solution. The cleaned leaves are dried and stirred with soybean straw and vinegar to obtain mixture that is boiled with water. The boiled mixture is covered with plastic thin film for fermentation. The fermented product is mixed with edible alcohol (3-4 ml), glucose (0.4g), yeast paste, calcium carbonate (1.5g), agar (1.5g) and water (100g) to obtain another mixture that is kept at 30 degrees C for 2 days to obtain product, which is stored at 4 degrees C.
NOVELTY - Preparation of ibandronate sodium monohydrate involves adding 3-(N-methyl-N-pentylamino)propionic acid hydrochloride phosphite and phosphorus trichloride to toluene solvent, obtaining ibandronate, hydrolyzing, forming sodium hydroxide into salt, purifying, then adding water, and concentrating.    USE - Preparation of ibandronate sodium monohydrate (claimed).    ADVANTAGE - The method enables environmentally-friendly preparation of nontoxic and stable ibandronate sodium monohydrate with high yield and without solvation.
NOVELTY - The device has a fermentation jar (1) which is set with a marsh gas collector and a raw material feeding pipe (4). The side wall of the fermentation jar is set with a discharging pipe (6). The fermentation jar is comprised with fermentation biogas slurry and biogas fermentation raw material. The fermentation jar is set with a stir device comprising a liquid circulation pump (5) and a circulation pipeline. The feeding pipe is set with a spraying unit. A spraying pipe and a liquid jar are set in 10-60 degrees. An adjustable nozzle (3) and jar side wall are set in 10-60 degrees.    USE - Biogas pneuma hydraulic circulation stir uniform mixing device.    ADVANTAGE - The reaction speed of the mixing device can be enhanced. Energy consumption of the mixing device can be reduced. Fermentation liquid crust can be avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas pneuma hydraulic circulation stir uniform mixing device.    Fermentation jar (1)    Nozzle (3)    Feeding pipe (4)    Liquid circulation pump (5)    Discharging pipe (6)
NOVELTY - Biological organic fertilizer is obtained by preparing biological leavening agent by mixing e.g. calcium phosphate, fermented soybean meal, rice bran and effective microbial inoculum, performing anaerobic fermentation, then mixing milk cow excrement, straw, earthworm, biological leavening agent and cellulase, fermenting, the adding sodium alginate and activated sludge, performing fermentation, crushing the fermented material, granulating and drying the granules to obtain the product.    USE - The biological organic fertilizer is useful for promoting growth of crops and increasing stress resistance of crops.    ADVANTAGE - The fertilizer is prepared by simple process in large quantities and environmentally-friendly. The fertilizer is rich in probiotics, effectively adjusts microbial content in soil and decomposes organic substances in soil, improves soil fertility, increases crop yield and quality of the crops, and has long-lasting effect.    DETAILED DESCRIPTION - Biological organic fertilizer is obtained by preparing biological leavening agent by mixing 5 pts. wt. calcium phosphate, 6 pts. wt. fermented soybean meal, 15 pts. wt. rice bran, 15 pts. wt. corn powder, 5 pts. wt. colza cake, 10 pts. wt. bran and 2 pts. wt. effective microbial inoculum, maintaining water content of 35-40% and performing anaerobic fermentation at 25-30 degrees C for 7-10 days, then mixing 60-70 pts. wt. milk cow excrement, 20-30 pts. wt. straw, 10-20 pts. wt. earthworm, 2-3 pts. wt. biological leavening agent and 1-2 pts. wt. cellulase, maintaining the water content of 35-40%, naturally fermenting the mixture for 15-20 days, adding 10-20% sodium alginate and 5-10% activated sludge, mixing uniformly, performing secondary fermentation at 28-35 degrees C for 5-7 days, crushing the fermented material to 20-30 meshes sieve, granulating the mixture and drying the granules until the water content is 12-15% to obtain the product.
NOVELTY - Grape fertilizer comprises 100-150 pts. wt. pig manure, 60-70 pts. wt. human excreta, 40-50 pts. wt. chicken manure, 50-60 pts. wt. duck manure, 40-50 pts. wt. goose dung, 15-25 pts. wt. plant ash, 15-20 pts. wt. urea, 8-12 pts. wt. boric acid, 5-10 pts. wt. potassium sulfate, 2-5 pts. wt. zinc sulfate, and 2-4 pts. wt. calcium superphosphate.    USE - Used as grape fertilizer.    ADVANTAGE - The fertilizer is rich in nutrition component, which is good for growing grape, increasing yield and quality of grape, uses widely available raw material source, and reduces the production cost.
NOVELTY - Method for preparing microbial complex fermented protein feed, involves adding microbial complex fermentation agent in straw-based solid medium, and fermenting the mixture to obtain fermented protein feed at 28-35 degrees C and pH 5-7, where the microbial complex fermentation agent comprises Trichoderma, Aspergillus niger, Geotrichum, Candida, Bacillus, Pediococcus acidilactici, urea, potassium dihydrogen phosphate, magnesium chloride, organic chelating agent, and humic acid.    USE - The method is useful for preparing microbial complex fermented protein feed (claimed).    DETAILED DESCRIPTION - Method for preparing microbial complex fermented protein feed, involves adding microbial complex fermentation agent in straw-based solid medium, and fermenting the mixture to obtain fermented protein feed at 28-35 degrees C and pH 5-7, where the microbial complex fermentation agent comprises 1.5-7.5x 106 colony-forming unit (cfu)/g Trichoderma, 1.5-7.5x 106 cfu/g Aspergillus niger, 1-4x 106 cfu/g Geotrichum, 1-4x 106 cfu/g Candida, 0.45-3x 106 cfu/g Bacillus, 0.15-1.5x 106 cfu/g Pediococcus acidilactici, 1-2% urea, 0.1-0.5% potassium dihydrogen phosphate, 0.01-0.1% magnesium chloride, 0.5-1.5% organic chelating agent, and 0.1-0.5% humic acid.
NOVELTY - Synthesis of catalyst involves providing a metal complex (I), reacting metal complex with oxygen-containing ligand, replacing specific groups of oxygen-containing ligand, and obtaining catalyst.    USE - Synthesis of catalyst used as organometallic catalyst used in manufacture of polymers and pharmaceuticals.    ADVANTAGE - The method enables efficient synthesis of catalyst with high yield and reduced generation of waste material, without performing a separate purification process, by fast and economical process.    DETAILED DESCRIPTION - Synthesis of catalyst involves providing a metal complex of formula (I), reacting metal complex with oxygen-containing ligand, replacing group (R4) and group (R5) of oxygen-containing ligand, and obtaining catalyst.    M=metal chosen from molybdenum or tungsten;    R1=alkyl, heteroalkyl, aryl, or heteroaryl (all optionally substituted);    R2,R3=H, alkyl, heteroalkyl, aryl, or heteroaryl (all optionally substituted);    R4,R5=heteroalkyl or heteroaryl containing nitrogen (both optionally substituted);and    R4+R5=optionally substituted bidentate ligand with respect to M.
NOVELTY - Composition comprises 2.5-4 wt.% Enteromorpha polysaccharide, 0.5-0.7 wt.% polyhexamethylene guanidine, 2-4 wt.% Enteromorpha hydrolase, 2-4 wt.% sodium alginate, 2-4 wt.% banana mesothelin and remainder purified water.    USE - The composition is useful for treating athlete's foot (claimed), improving metabolism, regulating qi, and promoting blood circulation and function of nervous system.    ADVANTAGE - The composition has improved stability and favorable odor, and prevents skin damage, and is nontoxic, nonirritating, and prepared by environmentally-friendly method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the composition which involves dissolving Enteromorpha polysaccharide and polyhexamethylene guanidine in purified water, adding banana mesothelin, sodium alginate and Enteromorpha hydrolase, mixing uniformly, cooling mixture and packaging product.
NOVELTY - Heavy metal pollution of soil repairing process involves performing pesticide spray, earthworm enrichment and microorganism decomposition.    USE - Method for repairing heavy metal pollution of soil by comprehensively using biochemical resource (claimed).    ADVANTAGE - The method enables to repair heavy metal pollution of soil in a simple manner, and ensures improved soil fertilizer effect and reduced pests of soil.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for preparing a pesticide spray, which involves sterilizing plastic thin film of organic fertilizer by using ultraviolet rays, and then adding microbial inoculum to the sterilized product; soaking pyrethrum and rotenone in warm water at 10-20 degrees C for 30 minutes, and then heating them at 30-50 degrees C for 5-10 hours, particularly 7.5 hours; taking supernatant of the obtained material; adding Bacillus thuringiensis powder to the obtained supernatant liquid, and then spraying them on the sterilized product to obtain the finished product;    (2) a method for enriching earthworm, which involves pouring soil with good breeding earthworms after pesticide spray, and then watering the soil twice in every morning at 11:00-14:00; collecting earthworms enriched soil after 4 days watering; and    (3) a method for microorganism decomposition, which involves putting microorganism in the earthworms enriched soil after 4 days of earthworm enrichment to produce the desired effects.
NOVELTY - Preparing fertilizer involves mixing phosphoric acid and urea in mol ratio of 1.1-1.2:1 at 83-96 degrees C, and then stirred at speed of 170-205 revolutions per minute for 3 hours to obtain slurry. Ammonia gas is introduced in the slurry at speed of 410-485 revolutions per minute at 70-80 degrees C for 26-28 minutes to obtain ammonium phosphate slurry having pH value 10.1-11.6. Ammonium phosphate slurry is cooled and crystallized and then nitrogen-phosphorus element is mixed in mol ratio of 1.8-1.9:1, and filtered to obtain ammonium phosphate product and filter liquid.    USE - Method for preparing fertilizer used for mulberry tree (claimed).    ADVANTAGE - The method is cost-effective and eco-friendly, enables to prepare fertilizer that improves mulberry yield and quality. Fertilizer reduces soil compaction rate.    DETAILED DESCRIPTION - Preparing fertilizer involves mixing phosphoric acid and urea in mol ratio of 1.1-1.2:1 at 83-96 degrees C, and then stirred at speed of 170-205 revolutions per minute for 3 hours to obtain slurry. Ammonia gas is introduced in the slurry at speed of 410-485 revolutions per minute at 70-80 degrees C for 26-28 minutes to obtain ammonium phosphate slurry having pH value 10.1-11.6. Ammonium phosphate slurry is cooled and crystallized and then nitrogen-phosphorus element is mixed in mol ratio of 1.8-1.9:1, and filtered to obtain ammonium phosphate product and filter liquid. Trace element compound and potassium are added in filter liquid in mol ratio of 1:1.3-1.6:1.8-1.9:1 to obtain a product. Product is dried in a drier at 60-72 degrees C for 1.1-1.4 hours with rate of 12 degrees C/minute to obtain fertilizer.
NOVELTY - Preparing fertilizer involves mixing phosphoric acid and carbamide in mol ratio of 1.4-1.8:1 at 100-120 degrees C for 4-5 hours with heating rate of 15 degrees C/minute, and then stirred to obtain intermediate slurry. Alkaline potassium salt (1.4-1.5 mol) is mixed in the intermediate slurry to obtain nitrogen-phosphorus-potassium slurry. Nitrogen-phosphorus-potassium slurry is cooled and crystallized, and then filtered to obtain filter cake and filter liquid. Filter liquid comprises nitrogen (3.2-7.5%) phosphorus pentoxide (1-2%), potassium hydroxide (3-5%).    USE - Method for preparing fertilizer used for shepherd's purse (claimed).    ADVANTAGE - The method is cost-effective and eco-friendly, enables to prepare fertilizer that reduces soil compaction rate.    DETAILED DESCRIPTION - Preparing fertilizer involves mixing phosphoric acid and carbamide in mol ratio of 1.4-1.8:1 at 100-120 degrees C for 4-5 hours with heating rate of 15 degrees C/minute, and then stirred to obtain intermediate slurry. Alkaline potassium salt (1.4-1.5 mol) is mixed in the intermediate slurry to obtain nitrogen-phosphorus-potassium slurry. Nitrogen-phosphorus-potassium slurry is cooled and crystallized, and then filtered to obtain filter cake and filter liquid. Filter liquid comprises nitrogen (3.2-7.5%) phosphorus pentoxide (1-2%), potassium hydroxide (3-5%). Trace element compound and Bacillus species are mixed with filter liquid to obtain a product, and then heated at 45-55 degrees C for 5 hours in a drier with speed of 3 degrees C/minute to obtain fertilizer.
NOVELTY - Preparing fertilizer involves mixing phosphoric acid and carbamide in mol ratio of 1.4-2.0:1 at 80-100 degrees C for 2-3 hours to obtain intermediate slurry. Alkaline calcium salt (1.4-1.5 mol) is mixed in the intermediate slurry to obtain calcium-phosphorus-potassium slurry having pH value 3-3.5. Calcium-phosphorus-potassium slurry is cooled and crystallized, and then filtered to obtaino calcium dihydrogen phosphate and filter liquid. Filter liquid comprises calcium ions (0.9-1.1mol), phosphorus pentoxide (0.9-1.1mol), potassium hydroxide (0.01-0.03mol).    USE - Method for preparing fertilizer used for cauliflower (claimed).    ADVANTAGE - The method is eco-friendly and reduces wastage of calcium phosphorus element resource, and increases purity of calcium biphosphate product.    DETAILED DESCRIPTION - Preparing fertilizer involves mixing phosphoric acid and carbamide in mol ratio of 1.4-2.0:1 at 80-100 degrees C for 2-3 hours to obtain intermediate slurry. Alkaline calcium salt (1.4-1.5 mol) is mixed in the intermediate slurry to obtain calcium-phosphorus-potassium slurry having pH value 3-3.5. Calcium-phosphorus-potassium slurry is cooled and crystallized, and then filtered to obtain filter cake and filter liquid. Filter liquid comprises calcium ions (0.9-1.1mol), phosphorus pentoxide (0.9-1.1mol), potassium hydroxide (0.01-0.03mol). Phosphorus element and nitrogen-phosphorus element are added in the filter liquid to obtain a product, and then heated at 40-50 degrees C for 2 hours in a drier to obtain fertilizer.
NOVELTY - Producing fertilizer involves preparing threonine fermentation broth using culture medium in jar to obtain a mixture that is filtered and bleached. The bleached material is crystallized to obtain crystals and mother liquor. The mother liquor is hydrolysed with bacterial protein to obtain stock solution that is utilized to obtain fertilizer.    USE - Method for producing fertilizer (claimed).    ADVANTAGE - The method enables to produce effective fertilizer in economic manner.
NOVELTY - Microorganism organic fertilizer preparation involves crushing mushroom residue and agricultural residue or food processing factory residues, and then soaking them in water. The fiber of the obtained material is decomposed, and then the obtained material is inoculated with fiber bacteria, proteolytic bacteria and bacterial strains with potassium efficient complex. The obtained material is mixed with 2-8% enzyme producing composite microorganism, and then the obtained mixture is fermented. The obtained material is mixed with base material, additives and dipotassium hydrogen phosphate.    USE - Method for preparing microorganism organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare microorganism organic fertilizer, which ensures improved yield.    DETAILED DESCRIPTION - Microorganism organic fertilizer preparation involves crushing mushroom residue and agricultural residue or food processing factory residues, and then soaking them in water. The fiber of the obtained material is decomposed, and then the obtained material is inoculated with fiber bacteria, proteolytic bacteria and bacterial strains with potassium efficient complex. The obtained material is mixed with 2-8% enzyme producing composite microorganism, and then the obtained mixture is fermented. The obtained material is mixed with base material, additives and dipotassium hydrogen phosphate, and then the obtained mixture is performed for solid fermentation. The obtained material is mixed with grass carbon to obtain powder or granules.
NOVELTY - Organic liquid fertilizer comprises 150-250 pts. wt. water, 5-20 pts. wt. soybean flour, 5-20 pts. wt. rice bran, 5-20 pts. wt. fish meal, 5-20 pts. wt. shrimp, 5-20 pts. wt. brown sugar, 1-5 pts. wt. refined sodium alginate, 0.5-1.5 pts. wt. egg, 1-5 pts. wt. amino acid powder and 5-15 pts. wt. composite microbial inoculum.    USE - Organic liquid fertilizer used for cultivating wax apple (claimed).    ADVANTAGE - The organic liquid fertilizer is prepared in a cost-effective manner, increases yield of wax apple, and improve quality of wax apple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic liquid fertilizer, which involves:    (A) mixing components uniformly to obtain a mixture; and    (B) fermenting the mixture in a sealed container for 20 days to obtain final product.
NOVELTY - Nutrient fertilizer comprises 3-4.5 pts. wt. dry chicken manure, 0.2-1 pts. wt. bean cake, 0.2-2 pts. wt. wood ash, 1-1.2 pts. wt. waste mushroom, 0.5-0.7 pts. wt. trichlorfon, 0.5-1.5 pts. wt. fruit juice, 1-1.5 pts. wt. cane sugar, 0.5-1 pts. wt. carbendazim.    USE - Nutrient fertilizer used for apple (claimed).    ADVANTAGE - The nutrient fertilizer is prepared in a simple manner, and increases yield of apple. Apple fruit has high sugar content, delicious taste and nutritious.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing nutrient fertilizer, which involves:    (A) mixing and crushing dry chicken manure and bean cake, and then adding wood ash to obtain a mixture;    (B) mixing remaining components with water and stirring uniformly; and    (C) fermenting the mixture at 30 degrees C for 10-15 days by using a sealed reaction kettle to obtain final product.
NOVELTY - Preparing disinfectant involves placing calcined calcium in a sealed double-layer stainless steel container, particularly a rotary vacuum dryer or mixer. Sealed double-layer stainless steel container comprises 0.1-0.3 molar mass of carbon dioxide at top layer, cold water or hot water is filled in middle layer and calcined calcium at inner layer. Oyster shell calcium is added in the sealed double-layer stainless steel container and heated at 35-90 degrees C, where higher concentration of carbon dioxide is released through a decompression valve.    USE - Method for preparing disinfectant used for preserving food (claimed) and cleaning bottle.    ADVANTAGE - The method is easy to control, enables to prepare disinfectant in a simple, eco-friendly and cost-effective manner. Disinfectant removes pesticide residues.
NOVELTY - Environmental remediation system comprises underground drainage pipe (19), woody plant growing micro-environment device connected with ground micro-ecological restoration device. The woody plant growing micro-device comprises inner shell (4) and outer shell (5). The inner shell layer is set with geotextile filter screen (10). The ecological restoration device comprises ecological restoration ground cloth (2), planting hole, activated carbon cloth layer, montmorillonite mineral powder layer and non-woven soil cloth layer. The planting hole is set with nutrition soil.    USE - Environmental remediation system used for cleaning soil surface layer.    ADVANTAGE - The environmental remediation system does not pollute air, and has high survival rate and strong practicability.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of environmental remediation system.    Ecological restoration ground cloth (2)    Inner shell (4)    Outer shell (5)    Geotextile filter screen (10)    Underground drainage pipe (19)
NOVELTY - Organic fertilizer is prepared using fermented vegetable waste product and 2x 109-3x 109 colony forming units (CFU)/ ml complex microorganism chosen from Bacillus mucilaginosus, B.subtilis, B.licheniformis, B.megaterium, Pseudomonas aeruginosa, Lactobacillus plantarum, and Azotobacter chroococcum in ratio of 1:7-8:4-6:3-5:1-3:3-5:1-2.    USE - As organic fertilizer containing fermented vegetable waste product.    ADVANTAGE - The organic fertilizer is environmentally-friendly and ensures to promote plant growth, and reduce pests and diseases of plants, and use of inorganic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the organic fertilizer, which involves (a) inoculating P.aeruginosa, B.subtilis, B.licheniformis, and B.megaterium in volume ratio of 1:3-5:2-4:1-3 into a fermentation medium, and performing shake culture of resulting fermentation culture to obtain mixed bacterial culture, (b) inoculating respectively B.mucilaginosus, and A.chroococcum and L.plantarum into a fermentation medium, and performing shake culture of resulting fermentation culture to obtain mixed bacterial culture, (c) mixing the resulting mixed bacterial culture obtained in the step (a) and (b) in ratio of 1:3-5:1-3:18-22 to obtain complex microbial mixture, (d) mixing the obtained complex microbial mixture with adsorbent and stirring the resulting mixture uniformly, (e) crushing vegetable waste to a particle size of 3-5 mm, controlling moisture content of the crushed vegetable waste to 60-70%, adding 0.1-0.5 %mass microbial mixture obtained in the step (d) to the resulting crushed vegetable waste, and mixing the obtained mixture with 0.2-2 %mass calcium carbonate powder to obtain product.
NOVELTY - Fertilizer is prepared using 80-100 parts mass pig manure, 40-60 parts mass Daphne giraldii leaf, 2-4 parts mass ammonium sulfate, 3-5 parts mass potassium sulfate, 0.5-0.7 part mass borax, 1-3 parts mass zinc sulfate, 100-120 parts mass silkworm excrement, 90-110 parts mass mushroom residue, 50-70 parts mass sea tangle residue, 3-5 parts mass amino acid, 1-3 parts mass humic acid and 80-100 parts mass water.    USE - As fertilizer for grapes.    ADVANTAGE - The fertilizer is environmentally-friendly and ensures to improve soil fertility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the fertilizer, which involves (a) weighing the above-mentioned raw materials, (b) crushing weighed raw materials, (c) fermenting the crushed raw materials in a fermentation tank, and (d) heating the fermentation product at 80 degrees C and 1 MPa and granulating the mixture to obtain product.
NOVELTY - Fertilizer comprises 13-15 pts. wt. nitrogenous fertilizer, 16-18 pts. wt. phosphate fertilizer, 20-22 pts. wt. potash fertilizer, 40-60 pts. wt. plant ash, 10-12 pts. wt. bean cake, 8-10 pts. wt. cotton seed, 80-100 pts. wt. dairy manure, 0.3-0.5 pts. wt. effective microorganism liquid, 3-5 pts. wt. protein mud, 20-30 pts. wt. furfural slag, 0.1-0.3 pts. wt. Borax (RTM: Sodium tetraborate) and 30-40 pts. wt. inebrians.    USE - Fertilizer used for orange (claimed).    ADVANTAGE - The fertilizer is safe and environment-friendly, and reduces plant diseases and controls insect pests without toxic component.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) crushing raw materials in a crusher;    (B) fermenting the crushed material in a jar;    (C) pre-heating the obtained mixture in a screw mixer to 80-90 degrees C;    (D) maintaining the head pressure of the mold to 1.1-1.3 magapascal; and    (E) granulating the obtained material to obtain the desired product.
NOVELTY - Fertilizer comprises 100-120 parts mass dried cattle manure, 70-90 parts mass peat, 30-50 parts mass weathered coal, 20-30 parts mass cassava residue, 40-60 parts mass silkworm excrement, 20-40 parts mass protein powder, 10-12 parts mass soybean meal, 20-30 parts mass furfural residue, 8-10 parts mass nitrogen fertilizer, 3-5 parts mass phosphate fertilizer, 7-9 parts mass potash fertilizer and 50-60 parts mass water.    USE - The fertilizer is useful for promoting growth of cucumber.    ADVANTAGE - The cucumber fertilizer is natural, nutritious and prepared by simple method, and improves soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer which involves mixing 110 parts mass dried cattle manure, 80 parts mass peat, 40 parts mass weathered coal, 25 parts mass cassava residue, 50 parts mass silkworm excrement, 30 parts mass protein powder, 11 parts mass soybean meal, 25 parts mass furfural residue, 9 parts mass nitrogen fertilizer, 4 parts mass phosphate fertilizer, 8 parts mass potash fertilizer and 55 parts mass water uniformly, homogenizing mixture, fermenting mixture at 80 degrees C and 1 MPa pressure under closed condition and granulating fermented mixture to obtain the product.
NOVELTY - Use of sodium metasilicate and sodium orthosilicate as catalyst is claimed for producing biodiesel from source of triglyceride and methanol or ethanol.    USE - Used for producing biodiesel from source of triglyceride and methanol (claimed).
NOVELTY - Separation and purification of biodiesel involves using pressurized carbon dioxide, where pressure range is 2-50 megapascal.    USE - Method for separation and purification of biodiesel (claimed).    ADVANTAGE - The method enables to separate and purify biodiesel in cost-effective manner.
NOVELTY - The method involves preparing inoculum. Growth and induction of enzymatic complex are estimated such that a recovery product is obtained. Cellulolytic enzymes are utilized in enzymatic hydrolysis of a lignocellulosic biomass. Agricultural residues and rice husk comma residues of wood comma bagasse are obtained.    USE - Method for producing enzymes with Filamentary Penicillium Fungus Echinulatum for use in enzymatic reaction hydrolysis of lignocellulosic biomass.    ADVANTAGE - The method enables improving capacity of lignocellulosic biomass in an effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a method for producing enzymes with Filamentary Penicillium Fungus Echinulatum. '(Drawing includes non-English language text)'
NOVELTY - Antioxidant additive formulation comprises mixtures of antioxidant, metal chelating agent, 2-methoxy-4-propylphenol and eugenol derivatives.    USE - Antioxidant additive formulation for use in biodiesel (claimed).
NOVELTY - Polyurethane resin comprises biodiesel as green solvent or diluent, which comprises polyol, preferably vegetable oil, chain extender, preferably difunctional hydroxy or amino with short chain (2-5 carbons) or large (6-12 carbons), and tri or tetrafunctional crosslinking agent.    USE - Polyurethane resin used in coatings and for preparing elastomer (claimed).    ADVANTAGE - The polyurethane resin is non toxic.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing polyurethane resin, which involves:    (A) mixing ethyl acetate, biodiesel, the castor oil, propylene glycol, butyl hydroxytoluene and trimethylolpropane to obtain mixture; and    (B) adding toluene diisocyanate into mixture and then heating mixture at 70 degrees C to obtain the product.
NOVELTY - Biokerosene production involves processing raw material containing glycerides with lower alcohol containing 1-5 carbons atom in presence of homogeneous or heterogeneous catalyst at certain atmospheric pressure. Transesterification of obtained material is carried out at more than 150 degrees C temperature and certain atmospheric pressure. Transesterified product is purified in presence of high vacuum at 0.001-5 mmHg pressure to obtain residue having heavy ester (more than 16 carbon atoms).    USE - Method for producing biokerosene by integrated process (claimed).    ADVANTAGE - The method enables to produce biokerosene with high purity and yield.    DETAILED DESCRIPTION - Biokerosene production involves processing raw material containing glycerides with lower alcohol containing 1-5 carbons atom in presence of homogeneous or heterogeneous catalyst at certain atmospheric pressure. Transesterification of obtained material is carried out at more than 150 degrees C temperature and certain atmospheric pressure. Transesterified product is purified in presence of high vacuum at 0.001-5 mmHg pressure to obtain residue having heavy ester (more than 16 carbon atoms). Decarbonylation if residue is carried out in a fixed or fluidized bed reactor in presence of a catalyst i.e. zeolite at 150-800 degrees C to obtain a mixture of hydrocarbons and oxygenated compounds. Hydrocarbons and oxygenated compounds are separated from mixture of hydrocarbons and oxygenated compounds. The oxygenated compounds are decarboxylated or hydrogenated, and then purified at certain atmospheric pressure to obtain the finished product i.e. biokerosene.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the biokerosene production method. (Drawing includes non-English language text).
NOVELTY - Hydroxymethylfurfural production involves hydrolyzing alkoxide, adding n-propanol, ethanol and zirconium oxide to hydrolyzed product, and then adding aqueous ammonia to the mixture for maintaining pH to 10-1.5, where the mixture is stirred, and then polymerized at room temperature to obtain gel. Gel is dried in a muffle furnace in presence of exhaust gases to obtain xerogel. Xerogel is washed with alcohol, and then calcined at low temperatures for long time. 3-Chloropropyltriethoxysilane is added to calcined material, and then heated in oil bath at 90-120 degrees C.    USE - Method for producing hydroxymethylfurfural used as a catalyst for dehydration of sugars and production of biofuel (all claimed).    ADVANTAGE - The method enables producing hydroxymethylfurfural that is efficient for production of biofuel.    DETAILED DESCRIPTION - Hydroxymethylfurfural production involves hydrolyzing alkoxide, adding n-propanol, ethanol and zirconium oxide to hydrolyzed product, and then adding aqueous ammonia to the mixture for maintaining pH to 10-1.5, where the mixture is stirred, and then polymerized at room temperature to obtain gel. Gel is dried in a muffle furnace in presence of exhaust gases to obtain xerogel. Xerogel is washed with alcohol, and then calcined at low temperatures for long time. 3-Chloropropyltriethoxysilane is added to calcined material, and then heated in oil bath at 90-120 degrees C. The hot material is stirred, and then imidazolium salt is added to the stirred material. The material is stirred in ultrasonic bath for 2-8 hours, and then processed with dichloromethane at 50 degrees C. Zirconium oxide is added to the processed material, and then processed with toluene. The mixture is stirred in presence of nitrogen at 90-120 degrees C for 10-12 hours to obtain the desired product.
NOVELTY - Organic silicon fertilizer preparation from industrial citrus residue involves separating waste, and then fermenting citrus residue. The obtained material, rice husk and silicon are mixed to obtain the finished product.    USE - Method for preparing organic silicon fertilizer from industrial citrus residue (claimed).
NOVELTY - Producing 9-alpha-hydroxyandrostenedione involves inserting ksh gene obtained from genetically engineered Mycobacterium smegmatis me2 155 strain into the shuttle vector pMV261 to obtain recombinant expression vector. The plasmid of recombinant expression vector is incorporated into another strain for producing 9-alpha-hydroxyandrostenedione.    USE - Method for producing 9-alpha-hydroxyandrostenedione from genetically engineered Mycobacterium smegmatis me2 155 strain (claimed).    ADVANTAGE - The method enables to produce 9-alpha-hydroxyandrostenedione that has high conversion rate in a simple and environment-friendly manner.
NOVELTY - Imidazo(1,2-a)pyridin-3-yl-methanol (II) is reacted with hydrohalic acid (III), and then obtained compound is reacted with Grignard reagent in presence of carbon dioxide, to obtain 2-(imidazo(1,2-a)pyridin-3-yl)acetic acid (I).    USE - Preparation of 2-(imidazo(1,2-a)pyridin-3-yl)acetic acid used as intermediate for preparing minodronic acid for preparing medicine for treating osteoporosis.    ADVANTAGE - The method efficiently and economically provides 2-(imidazo(1,2-a)pyridin-3-yl)acetic acid with high yield and purity without causing pollution to the environment.    DETAILED DESCRIPTION - Imidazo(1,2-a)pyridin-3-yl-methanol of formula (II) is reacted with hydrohalic acid of formula (III), and then obtained compound is reacted with Grignard reagent in presence of carbon dioxide, to obtain 2-(imidazo(1,2-a)pyridin-3-yl)acetic acid of formula (I).    X=chloro, fluoro or iodo.
NOVELTY - The system has an oxidation reaction jar (1) that is set in inner portion of a stir blade (2). The oxidation reaction jar is set with a main liquid (4) and a nitric acid (3). A side wall upper portion of the oxidation reaction jar is set with a supernatant outlet (5). The supernatant outlet pipeline is connected to a separate physical unit through a liquid inlet. The separate physical unit is provided for separating a precipitate and separating a sulfone, methyl sulfonic acid sodium and sodium nitrate.    USE - System for processing waste salt in dimethyl sulfoxide.    ADVANTAGE - The active ingredient is recycled easily. The simple structure, reduced energy consumption and increased extraction efficiency of the system are increased and environmental friendly .    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the front end portion, crusher and oxidation reaction jar.    Oxidation reaction jar (1)    Stir blade (2)    Nitric acid (3)    Main liquid (4)    Supernatant outlet (5)
NOVELTY - Device comprises a vertical body (1) and horizontal body (2), which form H-shaped structure at lower ends of the device. A weight control cell (8) controls weight of inserted materials, which is fixed at upper ends of a body (3). The body comprises folded steel sheet and reinforced carbon, where two inputs are provided at top of the body. The body is closed tightly at bottom of an outlet (5), and tightly closed internally and horizontally at ends of threads. Exchangeable drive is reduced by gear of bike, and positioned at top and bottom of the body.    USE - Device used in mixer for stabilizing organic material (claimed).    DETAILED DESCRIPTION - Device comprises a vertical body and horizontal body, which form H-shaped structure at lower ends of the device. A weight control cell controls weight of inserted materials, which is fixed at upper ends of a body. The body comprises folded steel sheet and reinforced carbon, where two inputs are provided at top of the body. The body is closed tightly at bottom of an outlet, and tightly closed internally and horizontally at ends of threads. Exchangeable drive is reduced by gear of bike, and positioned at top and bottom of the body. Endless thread is controlled by an electrical panel containing contactors, relays, timers and emergency key.    DESCRIPTION OF DRAWING(S) - The drawing shows a frontal view of a device.    Vertical body (1)    Horizontal body (2)    Body (3)    Outlet (5)    Weight control cell (8)
NOVELTY - The generator has an internal combustion engine that is exploded by electrolysis process to break hydrogen and oxygen in the generator, where the hydrogen and oxygen are directly added to mixture of air and fuel through an air duct in an internal combustion.    USE - Hydrogen and oxygen generator for use as a greenhouse gas emission reducer to reduce pollution in a motor vehicle.    ADVANTAGE - The generator provides emission reduction of waste pollutant gas such as carbon monoxide and carbon dioxide and increases water production.
NOVELTY - Producing organic molecule involves pretreating biomass and then mixing with ionic liquid in a mixer to obtain mixture. The mixture is hydrolyzed and then separated to obtain sugar syrup and residue. The sugar syrup is fermented to obtain the product.    USE - Method for producing organic molecules (claimed).    ADVANTAGE - The method does not use catalyst to produce organic molecules.
NOVELTY - System comprises supply unit (2) installed in an opening in base of heated cylinder (3), where material is transported by a thread (4) for drying and removing excess natural moisture from organic waste through drains (7). The liquid is passed from filtering unit (6). The output is collected and ground using grinding unit (5).    USE - System used for recycling organic waste (claimed) from household, meals companies, street market, supply market and other market.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of system.    Supply unit (2)    Cylinder (3)    Thread (4)    Grinding unit (5)    Filtering unit (6)    Drains (7)
NOVELTY - Producing phenolic compound involves utilizing an enzyme system with feruloyl esterase property for treatment of bagasse from sugarcane to obtain second-generation ethanol.    USE - Method for producing phenolic compound, particularly ferulic acid and coumaric acid (claimed) used as a precursor for producing vanillin.    ADVANTAGE - The method enables to produce phenolic compound that acts as a precursor for producing vanillin, and thus prevents the wastage of nonrenewable resource, because the preparation of vanillin requires utilization of nonrenewable resource.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an enzyme system, which comprises a recombinant nucleotide sequence that encodes for enzyme.
NOVELTY - Bio-kerosene fuel production involves preparing feedstock containing material rich in glycerides, 1-5C lower alcohol, and a homogeneous or heterogeneous catalyst at atmospheric pressure. The resulting material is heated at 150 degrees C to promote transesterification reaction at atmospheric pressure. The obtained product is purified in high vacuum to get bio-kerosene, where the residue includes heavy ester containing more than 16 carbon atoms.    USE - Method for producing bio-kerosene fuel from fossil origin.    ADVANTAGE - The method produces bio-kerosene fuel with a high degree of purity and characteristics similar to fossil fuel. The obtained fuel is an alternative to jet fuel that reduces emissions of pollutants with low toxicity.    DETAILED DESCRIPTION - Bio-kerosene fuel production involves preparing feedstock containing material rich in glycerides, 1-5C lower alcohol, and a homogeneous or heterogeneous catalyst at atmospheric pressure. The resulting material is heated at 150 degrees C to promote transesterification reaction at atmospheric pressure. The obtained product is purified in high vacuum to get bio-kerosene, where the residue includes heavy ester containing more than 16 carbon atoms. The residue undergoes decarbonylation in fixed-bed or fluidized reactor in presence of zeolites as catalyst at 150-600 degrees C to obtain a mixture of hydrocarbons and oxygenates. The obtained mixture is separated, where the obtained hydrocarbons fraction is compatible with fossil kerosene composition. The oxygenates fraction is subjected to hydrogenation reaction, where the resulting product is purified by distillation at atmospheric pressure to give hydrocarbons called as bio-kerosene and lower hydrocarbons.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the method for producing bio-kerosene. (Drawing includes non-English language text).
NOVELTY - Reusing effluent involves processing lignocellulosic biomass to produce ethanol by hydrolysis, during first generation and second generation steps. The lignocellulosic biomass is pre-treated by an integrated energy-efficient arrangement to generate by-product in presence of steam. Lignocellulosic biomass is treated in a RF vessel to generate by-product. The steam arises from the column and hydrolyses by-product obtained from lignocellulosic biomass. The generated steam also provides energy for preheating hydrolysis reactor.    USE - Method for reusing effluent used for ethanol production by integrated energy-efficient arrangement (claimed).    ADVANTAGE - The method enables to reuse effluent generated from agro-based industries. The agro-based industries utilizes lignocellulosic biomass such as bagasse, sugar cane straw, corn, cereal, wheat, sorghum or sugar beet to obtain ethanol in a highly efficient manner. The lignocellulosic biomass is utilized to produce bioelectricity.    DETAILED DESCRIPTION - Reusing effluent involves processing lignocellulosic biomass to produce ethanol by hydrolysis, during first generation and second generation steps. The lignocellulosic biomass is pre-treated by an integrated energy-efficient arrangement to generate by-product in presence of steam. Lignocellulosic biomass is treated in a RF vessel to generate by-product. The steam arises from the column and hydrolyses by-product obtained from lignocellulosic biomass. The generated steam also provides energy for preheating hydrolysis reactor. The steam is utilized as hot water source, which is supplied to the hydrolysis reactor for the separation and recovery of effluent. The condensate obtained from the vapor is recovered by indirect exchange process to RF vessel to continue the recycling process of effluent.
NOVELTY - The method involves utilizing a separation system of chemical components (3) for separating fractions to obtain a product. A coal retrieval system (4) and a gas separation unit (5) are utilized for separating liquid biomass such as lignin, esters, coke biomass, nitrogen fertilizer chip and carboxylic acids. Devolatilization process of the biomass is performed in total or partial absence of oxygen by using a single reactor to obtain a range of biomass products from the obtained product.    USE - Method for separating a fraction of devolatilization biomass product.    ADVANTAGE - The method enables separating a fraction of devolatilization of the biomass product in efficient and versatile manner. The method enables reducing production cost of the biomass product and avoiding losses of the biomass product.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for separating a fraction of devolatilization biomass product. '(Drawing includes non-English language text)'    Biomass alimentation system (1)    Devolatilization reactor (2)    Chemical components (3)    Coal retrieval system (4)    Gas separation unit (5)
NOVELTY - The system comprises a controlled compression system (1) for extracting methane from hydrogen sulfide, and carbon dioxide from biogas through a passage. The compression system delivers hydrogen sulfide to an adsorption tower with a catalyst system iron oxide-based alloys (2), which removes element of biogas. A water cooling tower (3) is provided for stabilizing temperature at 12 degrees C, and forwards water and gas into the tower absorption of carbon dioxide for performing pressurized washing.    USE - System for treating and separating components of biogas.    ADVANTAGE - The system performs the entire process with high simplicity combined and high efficiency, and gives excellent quality products with characteristic established by regulatory agencies with reduced biogas loss (less than 5%).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for extracting hydrogen sulfide from biogas, which involves removing element biogas through a combination of suitable pressure by using catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the method for extracting hydrogen sulfide from biogas. (Drawing includes non-English language text).    Compression system (1)    Alloys (2)    Water cooling tower (3)    Carbon dioxide absorption tower (4)    Separation tower (5)
NOVELTY - Biolubricant production involves adding 5-12% (w/w) polyhydric alcohol, 1-11% (w/w) water, 77-94% methyl biodiesel, and 1-4% (w/w) enzymatic catalyst in a reactor. The reaction mixture is heated at 40-55 degrees C and at 0.01-1 Bar pressure. The reaction is processed through high performance liquid chromatography (HPLC) to get desired conversion. The obtained mixture is filtered and centrifuged, and then stored at -10 degrees C for further analysis.    USE - Method for producing biolubricant from castor or Jatropha biodiesel (claimed).    ADVANTAGE - The method produces biolubricant in a simple and cost-effective manner by using castor and Jatropha as a great potential raw material.
NOVELTY - A purple alfalfa seed germination promoting method involves soaking purple alfalfa seeds in Bacillus subtilis GB03 liquid, and taking out the purple alfalfa seeds.    USE - Method for promoting germination of purple alfalfa seeds.    ADVANTAGE - The method enables promoting germination of purple alfalfa seeds in a simple manner with nonpathogenic property, strong stress resistance, important economic value and non-toxic and harmless B.subtilis liquid for humans and animals, applying widely in seeding pasture grass, increasing yield of grass per unit area, and avoiding environmental pollution.
NOVELTY - Method for preparing biofertilizer using soy sauce residue, involves (a) drying soy sauce residue, adding water to the dried soy sauce residue, and adding carbon and nitrogen to mixture, (b) adding Bacillus subtilis, B.natto and Aspergillus niger to the feed mixture, and performing the aerobic fermentation of mixture, and stacking mixture, (c) controlling moisture content of mixture, adding humic acid to the mixture, turning mixture, and fermenting mixture, and (d) adding probiotics to the semi-finished products, and stirring mixture.    USE - The method is useful for preparing biofertilizer using soy sauce residue (claimed).    ADVANTAGE - The method is environmentally-friendly.    DETAILED DESCRIPTION - Method for preparing biofertilizer using soy sauce residue, involves (a) drying soy sauce residue, adding water to the dried soy sauce residue, and adding carbon and nitrogen in a ratio of 15-25:1 to the mixture, (b) adding 50 million/g Bacillus subtilis, B.natto and Aspergillus niger in a ratio of 50:5:1 to the feed mixture, and performing the aerobic fermentation of the mixture at 50 degrees C, and stacking mixture at 50-70 degrees C for 10 days, (c) controlling moisture content of the mixture to 38-42%, adding 20 wt.% humic acid to the mixture, turning mixture, and fermenting mixture for at least 10 days, and (d) adding probiotics and fertilizer to the semi-finished products, and stirring mixture for 3 days.
NOVELTY - Preparing organic fertilizer using domestic garbage involves selecting domestic garbage after magnetic separation to obtain mixture of multi-perishable organic substance. Bacillus subtilis and Aspergillus niger are added in the obtained mixture of organic substance, where the number ratio of obtained mixture of organic substance, Bacillus subtilis and Aspergillus niger is 20-50:1:1-5, and the water content of the material is 50-65%. The obtained mixture is fermented at 60 degrees C for twice. The obtained material is dried.    USE - Method for preparing organic fertilizer using domestic garbage (claimed).    ADVANTAGE - The method increases conversion rate of domestic garbage and waste, ensures improved household garbage value, and reduces pollution.    DETAILED DESCRIPTION - Preparing organic fertilizer using domestic garbage involves selecting domestic garbage after magnetic separation to obtain mixture of multi-perishable organic substance. Bacillus subtilis and Aspergillus niger are added in the obtained mixture of organic substance, where the number ratio of obtained mixture of organic substance, Bacillus subtilis and Aspergillus niger is 20-50:1:1-5, and the water content of the material is 50-65%. The obtained mixture is fermented at 60 degrees C for twice. The obtained material is dried, where the water content of the material is 15%. The dried material is crushed, and then sieved. The obtained material is carbonized at 300-600 degrees C, and then nitrogenous fertilizer and phosphate fertilizer are added to the obtained material, where the total nutrient is not less than 5%. The obtained material is ground, and then dried at 300-600 degrees C. Organic degradation substance (10-50%) is added, and then mixed uniformly to obtain the desired product.
NOVELTY - A hydrogenated nopyl aldehyde cyclic acetal compound comprises monocyclic ring and fused ring in which monocyclic ring is obtained by performing condensation reaction of hydrogenated nopyl aldehyde and diol and fused ring is hydrogenated nopyl ethyl ether precursor.    USE - Hydrogenated nopyl aldehyde cyclic acetal compound for preventing anthrax baceteria in loquat and Camellia oleifera, blight fungus in pepper, Magnaporthe grisea in rice, and Sclerotia in lettuce.    ADVANTAGE - Hydrogenated nopyl aldehyde cyclic acetal compound is environment-friendly and has good bacterial inhibition.    DETAILED DESCRIPTION - A hydrogenated nopyl aldehyde cyclic acetal compound of formula (I) comprises monocyclic ring and fused ring in which monocyclic ring is obtained by performing condensation reaction of hydrogenated nopyl aldehyde and diol and fused ring is hydrogenated nopyl ethyl ether precursor An INDEPENDENT CLAIM is included for synthesis of hydrogenated nopyl aldehyde cyclic acetal compound which involves placing hydrogenated nopyl aldehyde:diol with molar ratio of 1:2 into conical flask, adding oxalic acid as catalyst, replacing water-carrying water separator and condenser, heating while stirring, reacting until water separator is not cloudy, extracting with benzene, washing extract with saturated brine for 2 times, drying with anhydrous sodium sulfate, distilling under reduced pressure, drying, collecting fractions, purifying by gas chromatography, and subjecting to structural analysis.
NOVELTY - Preparing progesterone, comprises e.g. (i) adding 4-androstenedione and triethyl orthoformate into a lower alcohol solvent, carrying out acid catalyzed reaction to obtain 3-ethoxy-10,13-dimethyl-7,8,9,10,11,12,13,14,15,16-decahydro-1H-cyclopenta(a)phenanthren-17(2H)-one (I), (ii) adding (I) and nitroethane into an organic solvent, reacting under ethylene diamine catalysis to obtain 3-ethoxy-10,13-dimethyl-17-(1-nitroethylidene) 2,7,8,9,10,11,12,13,14,15,16,17-dodecahydro-1H-cyclopenta(a)phenanthrene (II), and (iii) reducing (II) with zinc dust, carrying out acid hydrolysis, and refining.    USE - The method is useful for preparing progesterone (claimed).    ADVANTAGE - The method: has high product yield and purity, and high solvent recovery rate; and is economical and environment-friendly.    DETAILED DESCRIPTION - Preparing progesterone, comprises (i) adding 4-androstenedione and triethyl orthoformate into a lower alcohol solvent, carrying out acid catalyzed reaction to obtain 3-ethoxy-10,13-dimethyl-7,8,9,10,11,12,13,14,15,16-decahydro-1H-cyclopenta(a)phenanthren-17(2H)-one (I), (ii) adding (I) and nitroethane into an organic solvent, reacting under ethylene diamine catalysis to obtain 3-ethoxy-10,13-dimethyl-17-(1-nitroethylidene) 2,7,8,9,10,11,12,13,14,15,16,17-dodecahydro-1H-cyclopenta(a)phenanthrene (II), and (iii) adding (II) into lower alcohol solvent, reducing with zinc dust, carrying out acid hydrolysis to obtain progesterone crude product, and refining the crude product using activated carbon to obtain refined progesterone having high performance liquid chromatography (HPLC) content of more than 99.5%, melting point of 128-131 degrees C and yield of 83-87%.
NOVELTY - The method involves feeding manure to a digester (10, 20) to generate digestate (3), and passing a part of the digestate through a channel i.e. elongated channel, of a first heating zone (30) while heating the digestate by a heat exchanger (35) with the part of the thermal energy. The obtained product is heated in a second heating zone (40) with the energy to provide treated digestate. A first tube is provided with first volume to provide second volume between the first tube and a second tube, and liquid is heated with the portion of the thermal energy for heating the digestate.    USE - Method for treatment of manure i.e. liquid manure.    ADVANTAGE - The first tube is provided with the first volume to provide the second volume between the first tube and the second tube, and liquid is heated with the portion of the thermal energy for heating the digestate, thus allowing the manure to be treated in an efficient manner with low losses of energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for treatment of manure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a treatment arrangement.    Treatment apparatus (1)    Digestate (3)    Digesters (10, 20)    Heating zones (30, 40)    Heat exchanger (35)
NOVELTY - This utility model claims one new set of wastewater treatment and microorganism electrolytic system promoting methane recovery in the integrated. System comprises external power supply, electric power and connect the cathode and anode respectively in left right two on one electrode chamber, the electrode chamber with two cation exchange membrane separated bottom is equipped with magnetic force stirrer for stirring, another cathode provided with methane collecting port. The experiment are added with waste water and sludge at two poles of Yin and Yang, the microorganism is anode chamber by decomposing the organic object in waste water obtaining energy, at the same time for reaction process of the electronic product and hydrogen ion transfer to cathode chamber, microorganism and cathode chamber by decomposing organic matter producing methane, at the same time because of flow of electric current with make the degradation efficiency and yield of waste water and methane with of big pole is increase.
NOVELTY - This utility new type provide the one a pyrogenation gastification furnace for life garbage comprehensive processing system, said system comprising pre-heat accumulating type rotary bed pyrolyzing furnace, oil pneuma separating purification device, fixed bed gasification device, pneuma storage device and a gas recovery device, the domestic garbage raw material after drying, molding and sorting, crushing, after pre-processing, pyrolysis furnace in a high temperature oil-gas and pyrolytic carbon, pyrolytic carbon gasification after a gasification gas for as heat accumulating type radiant tube burner is gas fuel. This technology operation cost is low, the economic benefit is good, the gasification of low heat value of combustible gas generation in the heat accumulating type radiant tube combustion, solves the problem that the inner gasification pyrolysis garbage carbon poor economic benefit and pyrogenation gastification furnace for life garbage recycling of industrial popularization.
NOVELTY - Waste water processing involves processing poultry manure to obtain ammonia waste water with 100-300 mg/L nitrogen, and then blowing carbon dioxide through the obtained material to adjust 7-7.2 pH. The obtained material is treated with ammonia sulfate solution, and then the obtained material is added with micro-algae liquid. The obtained material is inoculated with 0.2-0.4 g/L Chlorella, and then the obtained material is mixed with carbon dioxide gas. The obtained material is fermented for 5asterisk8 days to obtain the finished product.    USE - Method for processing waste water to obtain water soluble fertilizer from poultry excrement (claimed).    ADVANTAGE - The method enables to process waste water in cost-effective and eco-friendly manner, ensures reduced floor area for the processing.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for waste water processing, where device comprises reactor main body, an air inlet unit, which is connecting upper part of the reactor main body, top outlet of the reactor main body is connected with pipe, a sealed container and an inner container.
NOVELTY - Asymmetric aromatic azo compounds preparation involves adding aromatic hydrazine in a two-phase system of dichloromethane containing a solid base catalyst, in which haloaryl is added dropwise at 20-40 degrees C, and then subjecting for ultrasonic treatment for 0.5-2.0 hours. The solid is filtered after completing reaction, where a liquid phase catalytic oxidation reaction is performed for 4-6 hours for removing aqueous phase to obtain crude product. The obtained crude product is recrystallized from dichloromethane to give the finished asymmetric aromatic azo compound.    USE - Method for preparing asymmetric aromatic azo compounds (claimed).    ADVANTAGE - The method prepares asymmetric aromatic azo compounds in a simple, safe, and eco-friendly manner by avoiding diazotization dangerous operation. The reaction is accomplished under mild condition with good selectivity, controllability, convenient recovery and use of un-reacted organic raw material, and reduced processing intensity on industrial scale.
NOVELTY - The device has a condensate water venting apparatus installed in a lower end portion of a heat exchanger. The heat exchanger collects waste heat of exhaust gas. Nitrogen oxide and sulfur oxide of the exhaust gas are dissolved in condensed water. A selective catalytic reduction apparatus and a flue gas desulfurization (FGD) equipment are installed in an oxidation period shear. An oxidizing agent injection system i.e. ozone injection system, is installed in a front-end of an oxidation catalyst unit. The heat exchanger oxidizes nitrogen oxide, sulfur oxide and volatile organic compound.    USE - Exhaust gas treatment device for an exhaust gas heat retrieval system, a seawater desalination system and a carbon dioxide and condensed water use system (all claimed) in a greenhouse.    ADVANTAGE - The heat exchanger effectively oxidizes sulfur oxide, carbon monoxide and volatile organic compound of the exhaust gas generated in the condensed water after desulfurizing sulfur oxide and carbon monoxide so as to simply pure the exhaust gas and collect waste heat during purifying process of the exhaust gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a carbon dioxide and condensed water use system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an exhaust gas treatment device.
NOVELTY - Preparing graphene oxide thin film involves performing ultrasonic dispersion of graphene oxide with to obtain graphene oxide dispersion, adding graphene oxide dispersion to hyperbranched dendrimers or polymer, and then stirring to obtain a mixed solution. The mixed solution is filtered to obtain the desired product.    USE - Method for preparing graphene oxide thin film used for preparing drug i.e. ciprofloxacin, norfloxacin and tetracycline (claimed).    ADVANTAGE - The method enables preparing graphene oxide thin film in an eco-friendly manner.
NOVELTY - One based on anaerobic digestion technology of a supply system, garbage storing tank of it through conveying belt and solid-liquid separating machine is connected with the solid-liquid separating machine separate the solid through a solid path and hydrolysis pool connection from the solid liquid separating machine separate the liquid through a liquid path and anaerobic fermentation jar connect, anaerobic marsh gas of a fermenting jar through pipeline and a gas cabinet, gas cabinet through pipeline marsh gas generator and a marsh gas generator by a power and a power circuit connection, a marsh gas generator by a high temperature smoke through pipeline pneuma and residual heat until a combustion engine, waste heat through direct combustion engine is a supply cold and heat load requirement, hot water heat exchanger through pipeline and municipal water taking pipe connection, after entering into municipal water hot water heat exchanger is a heat exchange a user living hot water. This utility new type is beneficial effect is: the exhaust gas a garbage is useful a cold thermoelectric resource, solves the problem that the waste gas is not rational to cause treatment of environment pollution and guarantees the supply of fuel supply system.
NOVELTY - A urea solution one hydrolysis production of ammonia system, including hydrolysis, hydrolyzing a thermometer T1, a pressure transmitter P hydrolysis, hydrolyzing the liquid level meter, the urea solution adjusting valve (A1), a hydrophobic heat exchanger, a steam adjusting valve (A2), hydrolyzing pneuma outlet adjusting valve (A3), a steam heat exchanger, hydrolyzing pneuma outlet thermometer T2. pneuma exit flow F, steam drain valve and a control a hydrolysis, the hydrolysis is set with a 7 interface, a connection a. hydrolyzing a control module through the cable a hydrolysis and a temperature gauge T1, a pressure transmitter P hydrolysis, hydrolyzing the liquid level meter, the urea solution adjusting valve (A1), a steam adjusting valve (A2), hydrolyzing pneuma outlet adjusting valve (A3), hydrolyzing pneuma outlet temperature gauge T2 and hydrolysis pneuma exit flow F a, the utility model is new type is simple and reliable, flexible and convenient control. Using steam as the heat source of the hydrolysis system, which greatly reduces the operation cost. It is without side product produce, so without second pollution.
NOVELTY - Preparation of chitin organic fertilizer comprises taking 10-30 wt.% shellfish, 10-20 wt.% edible fungi slag and 50-80 wt.% food plant residue based on dry basis, anaerobically fermenting, aerobically fermenting and aging.    USE - Method for preparing chitin organic fertilizer (claimed).    ADVANTAGE - The method has simple operation, low cost and no pollution.
NOVELTY - This utility new type relates to a solid waste gasification process one thermoelectric integrated system, said system comprises a pyrolysis furnace (1), a radiation tube burner (2), a dust removing device (3), one filter (4), a high temperature crude gas storage tank (5), a heat exchanger (6), a filter (7), a recovery device one (8), a gas purification tank (9), an electric generator (10) and boiler (11). This utility new type solid waste gasification process thermoelectric integrated system, zero pollution and can use the waste process.
NOVELTY - This utility new type claims a one with combustion pneuma or electric heat energy splitting of the biomass gas furnace, upper and lower two section, the upper section top cover set with feeding port and a material distributor, wherein reflux gas distributor set with the following raw material distributor, a hearth inner set with one heat exchanger, heat exchanger tube inner self-propelled temperature splitting pneuma, heat exchanger upper end enclosure set with a splitting pneuma exit tube, tube is raw material, end sealing head lower heat exchanger top part set with high temperature splitting pneuma inlet pipe , end lower tube plate heat exchanger, by support ring support plate, wherein the support ring plate by a support block is welded on the upper tube support, a heat exchanger upper end enclosure splitting pneuma exit pipe is the exit tube can freely move a filler culvert, set with a expansion joint on the gas inlet tube, end enclosure following heat exchanger set with grate, hearth and connected. This utility new type of splitting a pneuma tar-free, high.
NOVELTY - This utility new type relates to biomass energy preparing field, especially a one external burner of biomass gasification furnace. Gasification furnace comprising pyrolyzing gasification device and high temperature dust remover, pyrolysis and gasification device comprise cylinder of shell, lower section of shell is a combustion room set with a volute, spiral cut corresponding to mounting with the burner. External burner by a gasification furnace inner supply biomass pyrolyzing gasification needed heat of the inner through a load of a burner of a gasification furnace accurately pyrolysis and gasification temperature, and through the air coefficient of a burner is between 0.7 and 1, the gasification furnace inner excess air amount, a nitrogen content in the combustible gas is reduced, increase the combustion gas of a heat value, increase gas yield, a stable production technology condition, increase heat utilization efficiency, reduce the slag carbon-containing amount, low cost for preparing high heat value combustible biomass.
NOVELTY - This new type utility claims one wood crushing system and a biomass comprising a wooden meal fuel production device, wood crushing system of the vibration sieve and sawdust comprising crusher, vibration sieve comprising sieve and the lower part of the screen , through the conveying belt directly with the discharge hole of sawdust a crusher, a screen rear screen of a big wood raw material through a feeding conveying belt input sawdust. A sieving sieve rear qualified grain diameter of wood raw material directly into a dryer, only the screen a retain a big wood into sawdust granule crusher so as to reduce dust crushing machine of feeding quantity, increase big wood raw material of crushing quality, increase production efficiency and saves energy consumption.
NOVELTY - The solid waste, gas and/or fuel combustion pneumatic device has a gas purification device (28) that sends clean gas into a gas cabinet (24) to supply clean gas to a power generating unit (25) connected to an urban gas pipe network device. The gas cabinet returns gas to an incinerator (20) to burn gas with a particulate heat carrier supplementing high temperature. The power generating unit comprises an internal combustion engine or a gas turbine generator set which is coupled to a complete device.    USE - Solid waste, gas and/or fuel combustion pneumatic device used for power generation.    ADVANTAGE - Ensures high heat transfer efficiency between raw garbage and heat carrier without generating dioxin.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a combustion pneumatic device.    Fuel inlet (19)    Incinerator (20)    Gas cabinet (24)    Power generating unit (25)    Gas purification device (28)
NOVELTY - A hydraulic-type biomass fuel granulator comprises body, press wheel, bearing seat, guard board, guard plate, template bracket, hydraulic device, main motor, gauge guard, bearing pressure cover, bearing gland, bearing plate, supporting plate, bracing plate, base plate, support shaft, built-in template, guideway, cross roller, cross-roller guideway, support plate, base, base support, cylinder rod, hydraulic cylinder, cylinder plate, hydraulic cylinder cover, electromagnetic reversing valve, and hydraulic pump.    USE - Hydraulic-type biomass fuel granulator.    ADVANTAGE - The granulator is reliable, energy-saving and light-weight, has simple structure, small floor area, high operation efficiency, low failure rate and high stability, reduces equipment operation and maintenance costs, and ensures long service life of bearing.
NOVELTY - The machine has a biomass gasification furnace that is orderly connected to an air outlet of cyclone dust collector (31) through a gas pipeline. A burning layer of furnace unit is provided with an oxygen inlet and an outlet. The bottom portion of the combustion layer is provided with an activity fire grate. One end of connecting rod is passed through the furnace wall of the furnace unit connected with outer portion of driving connecting pole mechanism.    USE - Lower-sucking type biomass gasification machine with slag eliminating function.    ADVANTAGE - The structure of the gasification machine is simplified. The design of the gasification machine is reasonable. The concavo-convex structure of special bearing, an annular groove and an annular bump are mutually matched, so as to achieve the valid protection of the bearing. The use lifetime of bearing is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the lower-sucking type biomass gasification machine.    Cyclone dust collector (31)    Water box (32)    Cooling device (33)    Oil liquid separator (34)    Coal air blower (35)
NOVELTY - The biomass gasification furnace has furnace shell (8) set with mortar (15) with one side set with furnace feet (14) while its center is set with a concave air distribution plate (10). Other side of mortar is set with gasification air inlet pipe (13). The gasification air inlet pipe is connected with the total air inlet pipe (12) connected with the furnace shell being coated with heat preservation material (9).    USE - Biomass gasification furnace.    ADVANTAGE - Reduces gas content, and natural gasification of material in furnace. Provides good environment-friendly effect of rear collecting sewage of crushing the biomass material mixing and drying.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure of the biomass gasification furnace.    Furnace shell (8)    Heat preservation material (9)    Concave air distribution plate (10)    Total air inlet pipe (12)    Gasification air inlet pipe (13)    Furnace feet (14)    Mortar (15)
NOVELTY - Biological fuel manufacturing system comprises crusher, root, stem, leaves or their mixture of plant crushed aggregates form, and steam explosion device; feeding port, water steam with check valve entrance and discharging port, particle for a high pressure steam treatment in the water steam forming raw material discharging opening entering into spiral pipeline, solid-liquid separate machine, vibration sieving machine, solid raw material shatter, lubricant pressure molding device, cooling device, waste heat use system, spiral pipeline, dryer and pressure molding device.    USE - Biological fuel manufacturing system.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic diagram of the biological fuel manufacturing system (Drawing includes non-English language text).
NOVELTY - This utility new type claims a heat exchange function of one UASB reactor, reaction room is a hollow cylindrical structure of two end opening, reaction room upper part set with sealing, the sealing head top part set with a dust collecting room pneuma, pneuma room top part set with a marsh gas room, gas room through seal plate with the gas storage room, storage room connected with pneuma pump, set with a tube pneuma, pneuma pipe connected the air inlet at the lower part of the gas storage room heat exchange tube, the heat exchange tube mounting to the reaction room, storage room set with a biogas outlet pipe pneuma, pneuma room through returning pipe connected reaction room, reaction room upper part set with one level three phase separator in the reaction room lower part set with a second level three phase separator, reaction room bottom of the settling chamber, the bottom of settling room is set with spiral feeder, the bottom return pipe set with a water distributor, a water distributor connected feeding tube, reaction room on the mounting bracket a, reaction room lower part set with fermentation liquid outlet, the device can increase heat exchange of air inlet amount direction according to a regulating heat exchange pipe of gas production.
NOVELTY - This utility new type provide the one a scale pig farm excrement sewage zero discharging system, comprising a sub-system pollution, energy recovery by using sub-system and a recovery by sub-system, said three between a sub-system connecting with each other. This utility new type provide a scale pig farm excrement sewage zero discharging system, which not only reduces the using water amount, reduces the nitrogen quantity, saves land area matching, and obtain a good economic benefit.
NOVELTY - A bio-material is dissolved in ethyl alcohol, to obtain mixture (A). The biomaterial is mixed with mineral oil, to obtain mixture (B). The mixture (A) is immersed in impregnation material and dried, and then mixture (B) is immersed in the impregnation material, cooled and dried, to obtain ignition briquette.    USE - Manufacture of ignition briquette (claimed).
NOVELTY - The device has first supply tube (62) and first drain pipe (64), which are set in upper portion and lower portion of hollow pyrolysis tank (14) and reforming furnace (4). A cleaning device (70) is arranged for removing the tar piled in surface of inside wall of reforming furnace and connected to first supply tube and the first drain pipe, and dilute sulfuric acid tank. The oxygen is supplied to reforming furnace that is arranged to produce synthetic gas comprising carbon monoxide and hydrogen to reduction reaction of steam and carbon.    USE - Device for removing tar for biomass waste reformer.    ADVANTAGE - The cleaning device is arranged for removing the tar piled in surface of inside wall of reforming furnace and connected to first supply tube and the first drain pipe so that the miniaturization of the facility is achieved. The detarring efficiency about the tar layer is improved by supplying dilute sulfuric acid into the pyrolysis tank. The separation of upper and lower portion reforming furnaces is prevented by fixing screw and the locking element is connected in screw holes of masses. The reforming furnace is separately is maintained at high temperature and the safety in the high pressure state is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for removing tar for biomass waste reformer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for removing tar for biomass waste reformer. (Drawing includes non-English language text)    Reforming furnace (4)    Pyrolysis tank (14)    Supply tube (62)    Drain pipe (64)    Cleaning device (70)
NOVELTY - The advanced sewage treatment system has an advanced treatment device, in which an anoxic chamber (100,300,500) and an anaerobic tank (200,400) are positioned. A division conveying line is formed, in which the return sludge (20) from a division inlet line is returned. The processing water from the anoxic chamber is flowed in the aeration tank. The nitric acid impediment is prevented within the anaerobic tank. The wastewater high disposal process decreasing the total amount of the nitrate nitrogen prevents the dissolved oxygen impediment of the anoxic chamber.    USE - Advanced sewage treatment system for use with divided inflow of influent and endogeneous denitrified return sludge.    ADVANTAGE - The advanced sewage treatment system has an advanced treatment device, in which an anoxic chamber and an anaerobic tank are positioned, where the division conveying line is formed, in which the return sludge from a division inlet line is returned, and thus ensures simple and efficient treatment of the sewage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an advanced sewage treatment system. (Drawing includes non-English language text).    Inflow water (10)    Division inflow (11,12)    Return sludge (20)    Anoxic chamber (100,300,500)    Anaerobic tank (200,400)
NOVELTY - Method for processing organic waste involves carrying out biological denitrification of excrement (W) and biological treatment residue (P) using biological treatment installation (2), separating solid and liquid of biological treatment residue into supernatant liquid (S1) and concentrate (C) by primary solid-liquid separation, performing organic acid fermentation process by fermenting the concentrate using an organic acid fermenter (6), generating a souring sludge (A), and introducing souring sludge and supernatant liquid (S1) into biological treatment installation.    USE - Method for processing organic waste e.g. excrement, for forming treated water.    ADVANTAGE - The method enables efficient processing of organic waste with improved utilization of organic carbon source in denitrifying reaction of biological treatment residue, and reduced usage amount of chemicals as organic carbon source, by economical process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic waste processing facility (1).    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of organic waste processing facility. (Drawing includes non-English language text)    Organic waste processing facility (1)    Biological treatment installation (2)    Organic acid fermenter (6)    Souring sludge (A)    Concentrate (C)    Biological treatment residue (P)    Supernatant liquid (S1)    Excrement (W)
NOVELTY - The system (1) has an abnormality detection part (35) for detecting abnormality of a system power supply (PS). A fuel cell (13) generates electric power, which is supplied out of a system main body. A modifier (11) modifies raw material (D) to fuel gas (E), which is supplied to the fuel cell. A control part (40a) controls per unit time of the generated electric power of the fuel cell and amount of generation flow of the fuel gas in the modifier when abnormality of the system power supply is detected. An amount measurement part measures flow volume of the raw material.    USE - Household fuel cell system.    ADVANTAGE - The abnormality detection part detects abnormality of the system power supply, so that flow volume of fuel gas can be estimated when abnormality of the system power supply eliminates so as to avoid generation of malfunctions such as a voltage drop of the fuel cell and lack of fuel gas and improve performance of electric power generation in a state.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for operating a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a typical systematic diagram of a fuel cell system.'(Drawing includes non-English language text)'    Raw material (D)    Fuel gas (E)    System power supply (PS)    Fuel cell system (1)    Modifier (11)    Fuel cell (13)    Abnormality detection part (35)    Control part (40a)
NOVELTY - The method involves mixing a carbon molecular sieve (CMS) and a platinum (Pt) in a carbon black (CB). The platinum is dipped in the CB and CMS. The CMS is manufactured using zeolite with silicon (Si) and aluminum (Al). The 1-50 wt. % platinum is dipped in the CMS    USE - Method for manufacturing a fuel cell electrode catalyst.    ADVANTAGE - The method enables dipping metal catalyst material, thus improving battery capacity greater than 200 percentages, and increasing high efficiency of the fuel cell and reducing the used amount of the platinum.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation of a fuel cell electrode catalyst manufacturing method.
NOVELTY - The apparatus (10) has an electrochemical cell (15) arranged in an inner side of a reaction container (11), and forming a hydrogen electrode (13) and an oxygen electrode (14) in a solid oxide electrolyte (12). Gas supply lines (17a, 17b) supply gas generated by water vapor-electrolysis reaction or fuel cell reaction in the cell to the hydrogen and the oxygen electrodes. A heat exchange part (18) transmits heat energy arises in the electrochemical cell by the water vapor-electrolysis reaction and the fuel cell reaction to the supply lines when the supply gas flows from a gas outflow port (B).    USE - Electrochemical apparatus.    ADVANTAGE - The apparatus can implement high soundness, so as to effectively exploit the heat energy generated in the inner side of the apparatus by simple structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for operating an electrochemical apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an electrochemical apparatus.    Gas outflow port (B)    Electrochemical apparatus (10)    Reaction container (11)    Solid oxide electrolyte (12)    Hydrogen electrode (13)    Oxygen electrode (14)    Electrochemical cell (15)    Gas supply lines (17a, 17b)    Heat exchange part (18)
NOVELTY - The apparatus (100) has pair of isolation unit (401,402) which is arranged in state with which outer peripheral surface of edge portion of cell stacks (101) and internal peripheral surface of insertion unit (301,304) are contacted and filled to isolate inside and exterior of cell stack. A reducible gas supply path (308) induces reducible gas supplied from reducible gas inlet to inside of one end portion of cell stack. A reducible gas exhaust passage (309) induces reducible gas discharged from inside of other end portion of cell stack to reducible gas outlet (310).    USE - Reduction process apparatus for fuel electrode of cell stack.    ADVANTAGE - Since the apparatus has the structure which induces reducible gas to the inside of the cell stack corresponding to each reduction process unit by pair of isolation units, the cell stacks are reduction-processed simultaneously. Therefore, the work process at the time of reduction-processing cell stacks is shortened. Thus expense required in order to reduction-process is reduced shortening the period required by reduction process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for performing reduction process of fuel electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view illustrating the reduction process apparatus.    Reduction process apparatus (100)    Cell stack (101)    Insertion unit (301,304)    Reducible gas supply path (308)    Reducible gas exhaust passage (309)    Reducible gas outlet (310)    Isolation units (401,402)
NOVELTY - The reactor has a three-dimensional (3D) cathode (4) separated from an anode (1) by an electronically insulating layer (2). A cathode current feeder (3) is in electronic contact with the 3D cathode. The anode suppresses electro-oxidative loss of soluble reaction products. A micro-porous electronically insulating diaphragm is fixed or pressed onto a cathode layer. An electronically conductive porous layer is placed between the cathode layer and the cathode current feeder, where a carbon-di-oxide containing gas is fed into an electronically conductive porous layer.    USE - Single-cell continuous parallel plate membrane-less electrochemical reactor for facilitating electro-reduction of carbon dioxide to gaseous product e.g. carbon monoxide and methane. Can also be used for facilitating electro-reduction of carbon dioxide to format salt, formic acid, oxalic acid, ethene, formaldehyde and methanol.    ADVANTAGE - The reactor prevents the gaseous products from the anode and the cathode from mixing together by capillary pressure in the diaphragm while usual low solubility suppresses anode/cathode crossover in liquid phase. The insulating layer can have a porosity, pore size, thickness and surface energy selected to allow electrolyte liquid from a 2-phase feed stream to access the anode, to allow gas formed at the anode to escape, to suppress by-pass of fluids around the 3D cathode and to prevent electronic shorting between the anode and the cathode.    DETAILED DESCRIPTION - The insulating layer is made of a porous hydrophilic material.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a continuous reactor in which an electro-active surface of the anode is of a material that suppresses electro-oxidation of carbon dioxide products.    Anode (1)    Electronically insulating layer (2)    Cathode current feeder (3)    3D cathode (4)    Main fluid stream (11)
NOVELTY - This utility new type patent belongs to the solid waste treatment technology field, especially refers to a small solid biological one converter. It is a domestic garbage, each plant is not a biological part and animal food, human waste and so on each solid character waste of a bioreactor, a a solid waste and increase resource use rate. This biological converter aiming at a solid waste collecting treatment of low family, canteen, laboratory and other small area environment. The solid aerobic biological converter by support frame mould 1, the fermentation jar module 2, control module 3, cooling discharge module 4, power module 5. Through support frame module 1 a move of the whole reactor, saving labour, ferment jar. 2, discharge cooling module 4 and power module 5 the biological aerobic conversion of waste treatment, control module 3 a reactor of automatic and controllable, greatly saves manpower and material resources. Whole reactor design is elaborate, beautiful appearance, strong practicability, simple operation, energy saving and emission reduction.
NOVELTY - This utility new type claims a one aerobic fermenting device of liquid fertilizer system, comprising fermenting pool, fermenting pool one end set with discharge wherein, fermenting pool two side top part set with track, a track mounted transversely moving platform, a moving platform mounted walking wheel, a walking wheel and a walking drive motor connected, walking wheel and track matching the lower part, a transverse moving platform mounted cantilever, one end and moving platform is hinged cantilever and moving platform mounted between the first hydraulic pressure jar, the other end mounted throwing roller, throwing roller and turning driving motor connected, throwing roller outside peripheral wall set with a multi-pole stir, stir stick end part mounted throwing material plate, fermenting pool discharge wherein the top of one end set with cross beam, a lower cross beam mounting block material door, a material door and beam. It can finish for a layer of fertilizer pile, ensure the fertilizer fully contact the air to prevent the fertilizer stack temperature over-high, the operator a remote control, it does not need near distance operation, a high efficiency, a a continuous production and so on.
NOVELTY - Producing coffee waste compost, comprises (a) drying coffee waste such that the coffee waste has moisture content of 40-50%, (b) adding 5-6 pts. wt. microorganisms and 5-6 pts. wt. amino acids to 100 pts. wt. dried coffee waste, and (c) fermenting.    USE - The coffee waste compost is useful for fruits and vegetables (claimed).    ADVANTAGE - The coffee waste compost improves plant cell count, preferably greater than or equal to 10% (claimed), promotes plant growth, and recycles coffee waste and so is environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for coffee waste compost produced using the above method.
NOVELTY - The invention claims a device using combustion exhaust gas to promote aerobic fermentation reaction, comprising a fuel combustion device and an aerobic fermentation reactor, wherein the flue outlet of the fuel combustion device is connected with the conveying pipeline connected, the conveying pipeline is further connected to the air inlet of aerobic fermentation reactor or air inlet hole at the bottom of aerobic fermentation reactor. The conveying pipe of middle mounting channel has fan or blower and an electric three-way valve. This utility new type not only saves treatment system of the exhaust gas of the combustion device and cost, but also increase the aerobic fermentation efficiency of organic waste, shortens the fermenting time, environment-friendly processing the combustion waste gas, but also promotes the environment-friendly processing organic garbage waste, one item is energy-saving, new technology is environment-friendly.
NOVELTY - This utility new type claims a one for vehicle-mounted kitchen waste fermentation drying of circulation heating device, a set with the vehicle chassis and vehicle chassis of vehicle engine, the characteristic is a vehicle chassis set with fermentation drying groove, a clean water tank, circulation pump, heating water jacket, the first pipeline, the second pipeline, the first control valve and the second control valve, the fermentation drying groove set with heating jacket, after through a vehicle engine in vehicle driving process produce heat and heating water is set inner of water carry out heat exchange for a kitchen waste inner fermentation drying groove for drying process, which not only maintain the engine discharge and power property, and through heat exchange, it greatly reduces discharge pipeline temperature and prolongs the discharge pipeline use life of heat energy in a but also greatly saves the vehicle for drying process, it has simple structure, saves energy, is convenient to process.
NOVELTY - This utility new type claims a one liquid fermentation device, comprising comprising a feeding mechanism, the feeding mechanism is mounted the top end in the jar body and a feeding mechanism and a, middle position of said jar body inside set with stir shaft, bottom end of said stir shaft with a stir leaves, the stir shaft set with a propeller, the tank body is set with belt transmission device, a belt transmission device and a stirring wheel and a speed reducer belt pulley a; one side jar body is set with a speed reducer, the upper end of the speed reducer with a motor, the bottom end of the other side set with solid fertilizer material wherein, the solid fertilizer material wherein a lower two end of a set with a liquid fertilizer discharge wherein one the middle position of the tank body outside a set with temperature induction device and pH induction device. Using this utility new type solution, the structure is simple, the use is convenient, and it can uniform the stir biological fertilizer, and can be effective in a each a fungus.
NOVELTY - This utility new type refers to aerobic fermentation technology field, claims a one a fermentation device of ventilation system, comprising the fermentation groove and air blower, the bottom of ferment groove is provided with a lengthways groove, inner groove set with a vent pipe, an air outlet end air inlet end and air blower of aeration main duct is connected, two side groove is transversely opened with multiple aeration main duct connected and a ventilation groove, and the width of the ventilation groove is less than the diameter of aeration main duct, the cross section of the ventilation groove is an inverted convex shape, ventilation groove including a ventilation groove and b lower ventilation groove is set with a ventilation groove bottom part, a ventilation groove is larger than the cross section area of lower ventilation groove, the top of lower ventilation groove fixed with a clapboard, the clapboard is provided with a plurality of ventilating hole. This utility new type structure is simple, the operation is convenient, the uniform distribute oxygen release, which can promote effective organic waste of fermentation. This utility new type using plastic plate as clapboard, it can avoid expansion and contraction, the fermentation material blocking vent hole, the oxygen amount, increase the fermentation efficiency.
NOVELTY - This utility new type one using a plant straw and poultry and livestock manure a biological organic fertilizer of device, set with through groove straw, the straw into the straw groove according to the proportion, the straw conveying device entering into collecting container groove, one through the bottom outlet is set, and excrement from the excrement groove with slurry pump is sent, and urea water and additive from urine groove, groove with liquid additive pump is sent, a four mixture through pipe enter into mixing stacking groove is mixing, time when the water is not enough, through urea water spray pipe is set with water, a primary fermentation is to reduce the volume, and then rotating the subsequent stacking groove continuously. This utility new type is a beneficial effects: this organic fertilizer feeding device is simple structure, convenient operation, it can carry out good material is mixed, and a continuous production, the production of fertilizer quality steady efficient, the process does not ground and without waste pneuma, waste water, waste can be excellent maintenance of a production environment and sanitary.
NOVELTY - This utility new type claims a mesh-belt biological fertilizer feed, by the left machine frame, driving roller, a driven roller, a supporting roller, material distributing, spiral auger, adjust valve, a frame, a mesh belt, a right machine frame, a discharging device one, the whole machine is divided into seven layer network transmission, the first layer network transmission driven roller is mounted at the left upper machine frame, roller each mount 1 and right machine frame in a left machine frame, driving roller mounted at right upper machine frame, driving roller of the second layer network transmission mounted in the left upper machine frame, a driven roller mounted at right upper machine frame, third layer network transmission, network transmission fifth layer, seventh layer network transmission and the first layer network transmission identical, fourth network transmission layer, sixth layer network and the second transmission network transmission layer same, tank mounted at upper part of the first layer network transmission, distributing spiral auger mounted in inner material distributing tank, regulating valve in the right mounting a material tank, a discharging device mounted at right end of seventh layer network transmission, this machine has temperature control is accurate, continuous production, saves field.
NOVELTY - The method involves detecting the total usage time of an ion exchange unit (24). The shutdown time is detected from the last driving stoppage of a circulation pump (26). The circulation pump drive is started to the electric current application to the water electrolysis apparatus, when the determination is made that either the total usage time or the shutdown time exceeded the threshold value. The setup time is performed after the circulation pump drive started the electric current application to a water electrolysis apparatus (12).    USE - Method for starting water electrolysis system (claimed).    ADVANTAGE - The disconnected ion is circulated an ion exchange unit again, before the electrolysis is started. Since the ion is adsorbed in the ion exchange unit, the ion affected the water electrolysis process by the water electrolysis apparatus is suppressed reliably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for water electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water electrolysis system. (Drawing includes non-English language text)    Water electrolysis system (10)    Water electrolysis apparatus (12)    Ion exchange unit (24)    Circulation pump (26)    Temperature sensor (46)
NOVELTY - The method involves fixing a catalyst powder (21) by crimping on a base material (20) by rotating a catalyst powder side roller (31) installed so that the catalyst powder is connected. The base material on which the catalyst powder is deposited is moved by a movement unit (30). The circumferential speed of the catalyst powder side roller is larger than the moving speed of the movement unit.    USE - Method for manufacturing fuel cell catalyst layer.    ADVANTAGE - The loss of catalyst powder is effectively suppressed and the uniform catalyst layer is effectively formed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing apparatus of fuel cell catalyst layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the crimp fixing method of the catalyst layer.    Base material (20)    Catalyst powder (21)    Movement unit (30)    Catalyst powder side roller (31)    Base material side roller (32)
NOVELTY - System and method for odorless fermentative decomposition of biomass are claimed. The system comprises aseptic chamber, inlet and outlet. The method involves (a) preparing weakly acidic solution for fermentative decomposition using lactic acid bacteria derived from grains, where the weakly acidic solution suppresses offensive odor of various microorganisms during fermentative decomposition of biomass, (b) preparing microbial bed, and (c) performing odorless fermentative decomposition process using the weakly acidic solution and microbial bed.    USE - The system and method are useful for odorless fermentative decomposition of biomass (claimed).    ADVANTAGE - The system and method enable to perform odorless fermentative decomposition process cost-effectively, and in a simple manner within short period of time.    DETAILED DESCRIPTION - System and method for odorless fermentative decomposition of biomass are claimed. The system comprises aseptic chamber which is provided to perform fermentative decomposition process using lactic acid bacteria derived from grains, inlet and outlet. The method involves (a) preparing weakly acidic solution for fermentative decomposition using lactic acid bacteria derived from grains, where the pH of the solution is 4, and the weakly acidic solution suppresses offensive odor of various microorganisms during fermentative decomposition process, (b) preparing microbial bed, (c) performing odorless fermentative decomposition process using the weakly acidic solution prepared in the step (a) and microbial bed prepared in the step (b).
NOVELTY - Lip cosmetics comprise (a) oil gelatinizer having sugar skeleton, (b) astaxanthin, and (c) oil agent having viscosity of 5-500 Pa.second at 30 degrees C or 1-150 Pa.second at 30 degrees C.    USE - As lip cosmetics e.g. lip gloss and lipstick.    ADVANTAGE - The lip cosmetic has excellent stability and usability, provides improved plump feel of lips, excellent moisturizing effect, and flexible coating film, and enables to maintain liquid state or semi-solid state at room temperature.
NOVELTY - A composite gas separation membrane (10) has a gas separation layer (1) containing polyimide resin on upper side of a gas permeable supporting layer. The polyimide resin contains imide-containing structural units (I) and (V).    USE - Composite gas separation membrane is used in gas separation modules of gas separation apparatus used for separating gas containing carbon dioxide and methane (all claimed) used in thermal power stations, cement plants and iron mill blast furnace.    ADVANTAGE - The membrane has excellent gas permeability, gas separation performance and mechanical strength even in high pressure conditions, when used for separating gas containing impurities e.g. benzene, toluene and xylene, and high selectivity.    DETAILED DESCRIPTION - A composite gas separation membrane has a gas separation layer containing polyimide resin on upper side of a gas permeable supporting layer. The polyimide resin contains imide-containing structural units of formulae (I) and (V).    X=group chosen from groups of formulae (Ia)-(Ih);    X1=single bond or bivalent coupling group;    L=-CH=CH- or -CH2-;    R1,R2=H or substituent;    asterisk=bond-region with carbonyl group in formula (I);    Y1=group chosen from groups of formulae (IIa) and (IIb);    R3,R7=substituent;    A,B'=dissociative group;    p=0 or 1;    p1=0-2;    p2=2 or more;    Y3=group of formula (VI);and    p4=0-3.    An INDEPENDENT CLAIM is included for gas separation method, which involves selectively permeating carbon dioxide from the gas containing carbon dioxide and methane using composite gas separation membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the composite gas separation membrane.    Gas separation layer (1)    Porous layer (2)    Composite gas separation membrane (10)
NOVELTY - Composting device (10) comprises: a container (28) for receiving material to be composted, a water supply (19) for supplying water, a water outlet (17) for draining water, a pressing mechanism (12) for compressing the material in the receptacle, and a switching mechanism for selectively supplying water from the water supply to the pressing mechanism and draining water from the pressing mechanism to the water outlet such that the pressing mechanism is moved selectively between a first state in which the material is compressed in the container, and a second state for filling the container.    USE - Used as a composting device.    ADVANTAGE - The composting device enables decomposition by fermentation, and is easily operable even in private gardens.    DESCRIPTION OF DRAWING(S) - The figure shows a perspective sectional view of the composting device.    Composting device (10)    Pressing mechanism (12)    Water outlet (17)    Water supply (19)    Container (28)
NOVELTY - Preparing vortioxetine (I), comprises reacting 2,3-dimethyl-benzenethiol (IV), 1-bromo-2-iodo-benzene (III) and piperazine (II) with copper(I) iodide, phase transfer agent and alkali-containing aqueous solution.    USE - The method is useful for preparing vortioxetine (I), which is useful as an antidepressant drug (claimed).    ADVANTAGE - The method is capable of simply preparing vortioxetine in one-pot reaction without environmental pollution.    DETAILED DESCRIPTION - Preparing vortioxetine of formula (I), comprises reacting 2,3-dimethyl-benzenethiol of formula (IV), 1-bromo-2-iodo-benzene of formula (III) and piperazine of formula (II) with copper(I) iodide, phase transfer agent and alkali-containing aqueous solution.
NOVELTY - Leptolyngbya koreensis KIOST-1 strain deposited under low light conditions (4 mu mole photon/m2/s) and having an accession number of KCTC12347BP is new.    USE - The Leptolyngbya koreensis KIOST-1 strain is useful for producing: spirulina in outdoor cultivation (claimed); and biomass.    ADVANTAGE - The Leptolyngbya koreensis KIOST-1 strain allows nontoxic preparation of the spirulina and the biomass.
NOVELTY - This utility new type has stable property of microorganism multiplication type sewage processing system, comprising biological multiplication processing pool, the water groove, two times with water processing system, biological compost system, air blower and a primary settling tank, a water tank, a biological treatment pool multiplied a second time with a water treatment system and biological compost system, biological multiplication pool comprising a water inlet area, a clarification, the supernatant water groove, an air flow system, the aeration, sludge concentrate pool and a dissolved oxygen control system, a water inlet area connecting the water tank, a clarification system and air flow system, a clarification supernatant the water groove through a second time with water processing system, combine biological multiplication process a second time with water processing system carry out sewage treatment to ongoing water recycling device, the biological multiplication process and the produce section of a sludge biology compost process to obtain rich nutrition of organic fertilizer, so as to achieve the maximum limit of a resource and use.
NOVELTY - This utility new type claims a one burning sewage in use for generation of ozone device, comprising a generation, microorganism decomposing pool, a secondary sedimentation tank, a secondary water treatment system with a primary settling tank, a entrance, microorganism decomposing pool of microorganism decomposing pool is the water wherein a secondary sedimentation tank, generation system including gas pre-processing system and combustion pneuma generation set, pneuma generation set a gas pre-processing system, the gas pre-processing system is a microorganism decomposing pool is an air inlet an air outlet, two times with water comprising a sewage treatment pressure filter pump, filter jar, ultra-filtration system, in water recycling pool, a sewage filter booster pump, sewage filtering pressurizing pump connecting filter jar, filter jar a ultra-filtration system, ultra-filtration system in a water recycling pool, the organic substance of waste water process Anaerobic fermentation, after the limit of produce after containing a gas, used for marsh gas generation, Anaerobic fermentation of waste water treatment is a treatment to a water depth.
NOVELTY - Livestock and poultry dead and kitchen garbage comprehensively for preparing industrial lipid and organic fertilizer system, comprising high temperature sterilizing hydrolysis device, a crusher, a closeness, storage jar, primary magnetic sorting device, crushing device, a crushing separating device, the first stir mix device, using reclaimed fibre waste use device, solid-liquid separating device, the second stir mix device, a conveying device, the first steam preheating device, second steam preheating device, water storage tank, a three phase separator, oil water separator, Anaerobic fermentation jar, an aeration pool, pond, closeness horizontal double-layer tube aerobic fermentation jar, closeness horizontal aerobic fermentation jar, crushing and screening device, a chamber, an air supply device, discharge device, homogenizing storage chamber, organic fertilizer packaging device, a deodorizing industrial lipid. This utility new type is a large amount, fermenting period is short, treatment effect is good, the automatic degree high, a low cost, a process without peculiar smell, the kitchen garbage and dead livestock and poultry waste is valuable.
NOVELTY - The device comprises a tank for storing livestock manure, a tube for measuring amount of manure in the tank, a tank for fermenting the manure, a feeder for feeding air to the fermentation tank, heat guns for supplying heat to the air generated fed from the feeder, an outlet for discharging the fermented manure, and a viewing window for checking the fermentation process with the naked eye.    USE - The device is useful for fermenting organic fertilizer (claimed).    ADVANTAGE - The device is capable of rapidly fermenting the organic fertilizer with reduced generation of waste in an economical and energy efficient manner.
NOVELTY - This utility model claims a fermentation jar with a use of discharging hopper, aiming at a pipeline when a biological fermentation process in sampling a sewage collection hopper at the bottom end is in exist has material residue, is easy to produce phage, phage pollute the workshop environment. Reduce whole biological fermentation process in exist a possibility to pollute design. This utility new type through a traditional sewage collection hopper at the bottom for a sewage pipeline process innovation design, according to siphon principle in sewage pipeline at the two 180 degrees elbow and middle part of pipeline is connected the disinfecting liquid has part not absorbed lower liquid pipeline through pipeline in time, sterilizing liquid is a quantitative in a space in a two inner elbow, the pipeline in phage can not enter into workshop to ensure clean of the fermentation workshop through pipeline.
NOVELTY - This utility new type relates to a dry fermentation system, belongs to agricultural biomass using technology field. The system comprises fermentation warehouse, import the fermentation warehouse top one side, a discharge port located at one end warehouse bottom of fermentation, fermentation warehouse bottom installed with spiral transporting machine, upper part installed with feedstock import device, feedstock device comprising piston cylinder, piston cylinder-shaped vertical section and lower end and import connected, in horizontal section installed with reciprocating movement mechanism driving the piston. This new utility model not only realization of self-motion for discharging operation and continuous production, greatly reducing marsh gas engineering operation labour strength and improves the automatic operation function, and make fermentation warehouse bathing in hot water and heating, fermentation process using biogas reinforced spray operation, provided with biogas liquid break shell injection device in internal fermentation base body, realization of breaking and slurry injection enhanced mass transfer heat transfer function, so gas yield and gas quality are obtained is greatly improved.
NOVELTY - Increasing content of polar or weakly polar components comprises crushing traditional Chinese medicinal materials and then sieving, adding 40-100 vol.% of ethyl alcohol solution in the material liquid according to a ratio of 1:10-1:50, then adding 0.2-3% of an auxiliary extraction agent to extract at 40-80 degrees C for 0.5-5 hours, repeatedly extracting for 1-4 times and combining the extracting liquid, separating the extraction liquid through macro-porous resin and purifying, and finally obtaining extract containing polar or small polar active ingredient.    USE - The method is useful for increasing content of polar or weakly polar components comprising scutellarin, pseudo-ginseng, Oridonin and gastrodin (claimed).    ADVANTAGE - The method is capable of increasing content of polar or weakly polar components to 5-30% with less amount of auxiliary extracting agent and increased extraction rate, in a simple, cost-effective, eco-friendly and easy manner.
NOVELTY - An organic fertilizer is prepared by crushing plant residues into particle size of 20 mm; mixing with animal manure or inorganic fertilizer, and adjusting pH to 6-9; adding water such that the water content is 55-70 wt.%; adding 0.05-5 wt.% composite microorganism microbial inoculum; using conventional stack fermenting chamber for fermentation for 5 days; raising to 50 degrees C, and adding 0.05-5 wt.% second composite microorganism microbial inoculum; and fermenting for 1-2 days at 50-75 degrees C.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method produces fertilizer having improved decomposition, and increased compost speed.
NOVELTY - The equipment comprises a fermenter, a mixing system, a blower and an exhaust system, where a frame is fixedly installed in the fermenter. The mixing system comprises an auger drive shaft including forward and reverse drive motors. The shaft is disposed horizontally inside the fermenter. An auger blade structure is provided at the bottom of the fermenter. A water separating plate is set at the bottom of the fermenter. A water tank is connected with the fermenter. The water tank is set with a water outlet, where the air blower and the water tank are connected together through a gas pipeline.    USE - Agitation-type horizontal spiral straw compost generation equipment.    ADVANTAGE - The equipment is provides stable operations, requires less space, and reduces the operating cost.    DETAILED DESCRIPTION - The equipment comprises a fermenter, a mixing system, a blower and an exhaust system, where a frame is fixedly installed in the fermenter. The mixing system comprises an auger drive shaft including forward and reverse drive motors. The shaft is disposed horizontally inside the fermenter. An auger blade structure is provided at the bottom of the fermenter. A water separating plate is set at the bottom of the fermenter. A water tank is connected with the fermenter. The water tank is set with a water outlet, where the air blower and the water tank are connected together through a gas pipeline. The frame is set with a rolling wheel at the bottom. The plate is a straight or concave arc-shaped plate. The exhaust system includes an exhaust unit including a fan and a fan conduit. The upper part of the fermenter is provided with a set of air outlets, where each air outlet is connected to the exhaust system through a branch pipe.
NOVELTY - Use of mackerel fish waste for producing protein is claimed, where the application method comprises cleaning the mackerel fish and then removing bone, internal organs and head, peeling off the skin, hydrolyzing the obtained product to separate bones from fish and to obtain hydrolyzate and then centrifuging to remove supernatant, separating oil phase and water phase from the supernatant and then drying, and subjecting the obtained product to enzymolysis to obtain protein.    USE - The method is useful for producing protein from mackerel fish waste (claimed).    ADVANTAGE - The method is capable of easily producing the protein from mackerel fish in an economical manner.
NOVELTY - Fermenting edible mushroom waste organic fertilizer comprises crushing edible mushroom waste using a pulverizer, mixing crushed edible mushroom waste powder with a lime powder, adjusting the pH value to 6.5-8.8 without adding water to the powder, adding composite microbial inoculum to the powder and then uniformly mixing, sieving the edible mushroom waste powder through 40-80 mesh, fermenting the edible mushroom waste powder using a vertical fermentation equipment for 6-12 hours, and removing waste from the edible mushroom to obtain edible mushroom waste organic fertilizer.    USE - The method is useful for fermenting edible mushroom waste organic fertilizer (claimed).    ADVANTAGE - The method is capable of simply, economically and rapidly fermenting edible mushroom waste organic fertilizer with high production efficiency and quality.
NOVELTY - A cap tread rubber composition comprises biomass-derived rubber which is obtained by polymerizing aromatic vinyl and diene and has percent modern carbon (pMC) of greater than or equal to 1%, measured based on ASTMD6866-10.    USE - A cap tread rubber composition for pneumatic tire used for passenger cars (all claimed).    ADVANTAGE - The cap tread rubber composition-containing pneumatic tire has low fuel consumption and excellent wet grip performance and processability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) cap tread rubber for passenger car tires which is produced by using rubber composition; and    (2) pneumatic tire for passenger cars which contains cap tread produced using rubber composition.
NOVELTY - This new type utility claims one a rectal suppository administration device, belonging to the field of medical appliance, comprising a delivery cylinder push rod, further comprising disposable guide tube, a disposable guide tube front end is round table, rear end is cylindrical, the cylindrical part is a disposable guide tube of said outside are symmetrically fixed with two connecting a lug boss, round part in the disposable guide tube in the end is set with a cylindrical outlet hole, connecting with a one-way baffle plate in the inner end of the discharging hole is round part in the disposable guide tube outside is fixed set with a silicon rubber sleeve, a disposable guide tube and delivery cylinder screw thread connection, this utility new type has simple structure, convenient use, low cost, a single baffle plate preventing rectum waste entering into a delivery cylinder, which avoids pollution delivery cylinder, after use after a change disposable guide tube again use, sanitary and environment-friendly.
NOVELTY - Fertilizer comprises 3-5 pts. wt. bio-organic fertilizer, 15-20 pts. wt. water retention agent and 450-550 pts. wt. effective micro-organism expanded liquid comprising 0.5-2 pts. wt. effective micro-organism source liquid, 0.5-2 pts. wt. molasses and 2-4 pts. wt. deionized water.    USE - Fertilizer used for cultivating tobacco (claimed).    ADVANTAGE - The fertilizer restrains water evaporation from soil surface, and increases tobacco quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) preparing effective micro-organism expanded liquid by mixing source liquid, molasses and deionized water at 35-37 degrees C to obtain mixture;    (B) fermenting mixture anaerobically for 8-10 days to obtain effective micro-organism expanded liquid;    (C) mixing effective micro-organism expanded liquid, bio-organic fertilizer and water retention agent at 35-37 degrees C to obtain another mixture; and    (D) fermenting mixture for 7-8 days to obtain product.
NOVELTY - This utility new type provide a biological fertilizer fermenting one assistant device. Comprising fermenting pool, a fermenting pool comprising two side plate and a bottom plate, the biological fertilizer fermenting auxiliary device further comprising fermenting pool and phase matching of turning device and walking mechanism. The walking mechanism to drive turning device along the lateral movement of fermentation pool, the turning device including turning bracket by the walking mechanism drives and overturning is set with a turning up of bracket, the overturning from turn material bracket downward inclined set, lower end and bottom plate overturning phase contact. This utility new type provide a biological fertilizer fermenting auxiliary device, structure is simple, the cost is low, convenient arrangement, simple and fast operation, it is suitable for small scale of normal biological fertilizer.
NOVELTY - Organic fertilizer comprises organic waste, microbial fermentation agents and additive in percentage ratio of 70-75:29.99-24.99:0.01, and is prepared by mixing raw materials at not less than 55 degrees C for not less than 7 days to obtain organic fertilizer.    USE - Organic fertilizer used for stimulating crop growth and regulating metabolism.    ADVANTAGE - The organic fertilizer improves resilience of crops.
NOVELTY - Preparing bio-organic fertilizer involves adding dehydrating agent and heavy metal passivating agent in municipal domestic sludge, and then passivation process is carried out. Microorganisms inoculum is added in treated municipal domestic sludge and then aerobic fermentation is carried out to obtain a fermented product. The fermented product is mixed with inorganic fertilizer, dried it and then granulated and coated biocontrol agent.    USE - Method for preparing bio-organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare bio-organic fertilizer that improves soil structure and provides adequate nutrition to soil, and has enriched biological nutrient.
NOVELTY - Bio-organic fertilizer comprises fermentation material. Fermentation material comprises animal excrement (3000-3500kg), biological microbial inoculum (0.5 billion/gram), inorganic fertilizer (10-12.5 billion/g), ammonium sulfate (12-15kg) and zeolite powder (30-50kg).    USE - Bio-organic fertilizer.    ADVANTAGE - The bio-organic fertilizer is prepared in a cost-effective and eco-friendly manner, and production process is shorten effectively. The bio-organic fertilizer ensures effective viable count (less than or equal to 0.2 billion/g), organic matter ( greater than or equal to 45%), total nutrient ( greater than or equal to 5%), pH 5.5-7, moisture (less than or equal to 30%), fecal coliform count (less than or equal to 100 cells/g) and ascaris mortality rate ( greater than or equal to 90%).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-organic fertilizer, which involves:    (A) mixing zeolite powder, animal excrement, inorganic fertilizer and ammonium sulfate with biological microbial inoculum and performing fermentation at 60-65 degrees C for 15-20 days in presence of air; and    (B) measuring carbon nitrogen ratio (25-28%) of obtained fermentation product, and then performing fermentation of the fermented product in a clinker to obtain dark brown compost product with fecal odor to obtain final product.
NOVELTY - Preparing antibacterial agent involves diluting nanosilver by using water to obtain a mixture. Carbon particles are sprayed on the mixture at low pressure and then dried and packaged.    USE - Method for preparing antibacterial agent (claimed).    ADVANTAGE - The method is eco-friendly, enables to prepare antibacterial agent that has broad-spectrum antibacterial property and long-lasting effect. Antibacterial agent ensures non-toxic and non-irritating properties.
NOVELTY - Microorganism fertilizer comprises 20-40 pts. wt. domestic sludge, 17.5-27.5 pts. wt. straw powder, 5.5-9.5 pts. wt. humic acid, 0.1-0.2 pt. wt. fermentation fungus, 0.15-0.20 pts. wt. biological bacterium and 0.15-0.25 pts. wt. sodium polyacrylate.    USE - Microorganism fertilizer, in the form of liquid dosage, peat carrier powders, granular formulations, lyophilized dosage or mineral oil covers formulations (claimed).    ADVANTAGE - The fertilizer solves pollution and damaged soil structure problems. It ensures natural biological diversity and ecological system stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of microorganism fertilizer comprising mixing domestic sludge and fermentation strain; carrying out aerobic biological fermentation process; granulating; drying and cooling process, adding sodium polyacrylate and biological bacteria, and mixing.
NOVELTY - Biofertilizer comprises 20-40 pts. wt. domestic sludge, 17.5-27.5 pts. wt. straw powder, 5.5-9.5 pts. wt. humic acid, 0.1-0,2 pts. wt. fermentation yeast, 0.15-0.25 pts. wt. biological bacteria, and 0.1-0.2 pts. wt. nitrogen, phosphorus and potassium.    USE - Used as a biofertilizer.    ADVANTAGE - The biofertilizer solves the problem of sludge pollution, damaged soil structure, and low natural biological diversity and ecosystem stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the biofertilizer, comprising (i) mixing sewage sludge and fermentation yeast; (ii) carrying out aerobic fermentation of the mixture, then reacting with nitrogen, phosphorus and potassium nutrients; (iii) granulating the mixture; and (iv) drying the granulated particles, cooling, and mixing with biological bacteria.
NOVELTY - An organic fertilizer comprises 30-40 pts. wt. wormwood powder, 10-15 pts. wt. amino acid powder, 8-12 pts. wt. mineral substance, 40-55 pts. wt. high-protein substance and 0.05-0.2 pt. wt. enzyme preparation.    USE - Organic fertilizer.    ADVANTAGE - The fertilizer having pH of 6-8.5 contains more than 7 wt.% nitrogen, phosphorus and potassium nutrients, 40-45 wt.% organic matter and 20-25 wt.% water. It uses natural raw materials which have no pollution and do not affect water quality. It improves soil granular structure and air permeability, and increases water and fertility capacity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising mixing wormwood powder, amino acid powder, mineral substance, high-protein substance and water, stirring, aerobically fermenting at 55-75 degrees C for 5-7 days, drying, crushing, adding enzyme preparation, uniformly stirring and checking based on national standard.
NOVELTY - An excrement cleaning machine comprising front beam (16), rear beam (23), left and right side plate (17), reinforcing support (13), roller (1), rotating shaft, belt pulley, impeller, right swinging excrement impeller, bolt set, traction rope ring and shovel plate.    USE - Excrement cleaning machine used for poultry excrement fermentation pool (claimed).    ADVANTAGE - The machine saves labor force, and has high personal safety.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of excrement cleaning machine.    Roller (1)    Reinforcing support (13)    Front beam (16)    Left and right side plate (17)    Rear beam (23)
NOVELTY - The system comprises a composting compartment, a gas pipeline, a centrifugal fan and ammonia absorbing compartment including a gas distribution system, a gasket and an absorbing material. The composting compartment is provided in a left portion of a gas outlet. The gas pipeline is present in close contact with the composting compartment. A volume per hour of the air produced by the centrifugal fan is 10 times the volume of gas inside the composting compartment. The gas pipeline has number of branch pipe, and a thickness of 5-10 cm. The absorbing material has a height of more than 1.5 m.    USE - The system is useful for recovering volatile ammonia nitrogen fertilizer from livestock and poultry excrement (claimed).    ADVANTAGE - The system has simple structure, and recovers the fertilizer from livestock and poultry excrement in an efficient, economical and eco-friendly manner.    DETAILED DESCRIPTION - The system comprises a composting compartment, a gas pipeline, a centrifugal fan and an ammonia absorbing compartment including a gas distribution system, a gasket and an absorbing material. The composting compartment is provided in a left portion of a gas outlet. The gas pipeline is present in close contact with the composting compartment. A volume per hour of the air produced by the centrifugal fan is 10 times the volume of gas inside the composting compartment. The gas pipeline has number of branch pipe, and a thickness of 5-10 cm. The absorbing material has a height of more than 1.5 m, a pH value of 7-9, and moisture content of 50-60%.
NOVELTY - Restoration of heavy metal contaminated soil comprises insecticide spraying, performing earthworm enrichment and performing microbial decomposition.    USE - Method for restoring heavy metal contaminated soil used for improving soil fertility (claimed).    ADVANTAGE - The method has no secondary pollution and short processing cycle.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) Preparation of insecticide comprising taking 280-320 pts. wt. organic fertilizer, placing on sterile plastic film, flattening, performing UV germicidal irradiation for 3-5 days, cooling, adding 28-32 pts. wt. microbial agent and mixing to obtain component A; taking 0.03-0.09 pt. wt. matrine, placing in non-ferrous container, adding 1-5 times 10-20 degrees C warm water, soaking for 20-40 minutes, heating in low heat for 30-50 minutes, standing for 5-10 hours and collecting supernatant to obtain component B; and feeding 0.02-0.06 pt. wt. Bacillus thuringiensis powder into dispenser, adding component B, mixing and spraying to component A; and (2) Performing earthworm enrichment comprising spreading insecticide uniformly above soil, standing for 1-3 days, watering everyday at 11:00 am-2:00 pm for 3-5 days, adding decayed leaves or straw on soil surface and collecting earthworms.
NOVELTY - Preparing fertilizer comprises adding potassium solution in Penicillium strains and then providing in a fermentation tank, mixing the fermented mixture with inorganic potash, dry granulating the mixture, inoculating the mixture with industrial and agricultural organic wastes at ambient temperature and then adding potassium mineral solution, and leaching the solution at low temperature.    USE - The method is useful for preparing fertilizer (claimed).
NOVELTY - Preparing bioconverted organic fertilizer for tobacco involves mixing culture substrate containing black soldier fly eggs with 80-90 parts pig manure and 10-20 parts fertilizer cake comprising rapeseed meal or mixture of rapeseed meal, and peanut meal, and subjecting the mixture containing hatched larvae of the black soldier fly eggs to bioconversion, where the moisture content of the pig manure is 70-80%.    USE - The method is useful for preparing bioconverted organic fertilizer for tobacco (all claimed).    ADVANTAGE - The method is cost-effective.
NOVELTY - Multi-layered digestion bed aerobic composting method comprises: (i) mixing the pre-processed sludge compost with additive by stirring to obtain a sludge mixture; (ii) paving a layer of sludge mixture on a porous plate or a filter screen to obtain a single layered digestion bed; (iii) stacking more single layered digestion beds to form multi-layered digestion bed; and (iv) placing the multi-layered digestion bed in a shell or a cabinet, compositing the sludge mixture using aerobic microorganisms via fresh air or pure oxygen and discharging the generated exhaust gas.    USE - The method is useful as multi-layered digestion bed aerobic composting method.    ADVANTAGE - The method is economical, consumes small floor area and less energy, and achieves automatic sludge compost production line work.    DETAILED DESCRIPTION - Multi-layered digestion bed aerobic composting method comprises: (i) mixing the pre-processed sludge compost with additive by stirring to obtain a sludge mixture; (ii) taking a network frame including a porous plate or a filter screen with sideline along the porous plate or filter screen fixedly connected to the frame, then paving a layer of sludge mixture on the porous plate or filter screen to obtain a single layered digestion bed; (iii) stacking more single layered digestion beds to form a vertical multilayer frame structure i.e. multi-layered digestion bed; and (iv) placing the multi-layered digestion bed in a shell or a cabinet, which is set with a shell wall or cabinet wall and an accessible door for opening and closing, connecting the shell wall or cabinet wall with inlet and exhaust pipes, compositing the sludge mixture using aerobic microorganisms via fresh air or pure oxygen, discharging the generated exhaust gas via exhaust pipe of the shell or cabinet.
NOVELTY - Fertilizer comprises 2-7 pts. wt. Bacillus subtilis, 3-6 pts. wt. diatomite, 6-10 pts. wt. monocalcium phosphate, 1-5 pts. wt. glutamic acid, 3-8 pts. wt. peat, 2-5 pts. wt. animal manure, 3-9 pts. wt. ammonium molybdate, 5-9 pts. wt. zinc sulfate heptahydrate, 5-8 pts. wt. polyaspartic acid, 8-14 pts. wt. potato straw, 1-5 pts. wt. fly ash, 2-8 pts. wt. soybean meal, 3-6 pts. wt. ammonium chloride, 5-11 pts. wt. Artemisia rupestris, and 1-6 pts. wt. limestone.    USE - The fertilizer is useful for regulating acidity and basicity of soil (claimed), and increasing fertility of soil.    ADVANTAGE - The fertilizer promotes growth of crops, and regulates soil pH.
NOVELTY - Long-acting slow release fertilizer comprises 6-10 pts. wt. potassium fulvate, 5-9 pts. wt. urea phosphate, 4-8 pts. wt. polyvinyl alcohol, 6-11 pts. wt. potassium phosphate, 10-20 pts. wt. soybean meal, 3-7 pts. wt. expansive soil, 2-8 pts. wt. medical stone, 1-5 pts. wt. citric acid, 3-8 pts. wt. calcium superphosphate, 3-5 pts. wt. plant ash, 2-7 pts. wt. EDTA chelating zinc, 6-8 pts. wt. potassium sulfate, 8-14 pts. wt. vetch seeds, 1-2 pts. wt. Bacillus subtilis, 1-4 pts. wt. coating agent, and 2-4 pts. wt. release agent.    USE - Used as a long-acting slow release fertilizer.    ADVANTAGE - The fertilizer: supplies nutrients to crops for long-period; and utilizes microbial inoculum and organic fertilizer for improving soil fertility.
NOVELTY - Fertilizer composition comprises 7-15 pts. wt. corn straw, 4-8 pts. wt. conola straw charcoal, 1-5 pts. wt. zinc sulfate, 4-6 pts. wt. dilute hydrochloric acid, 3-7 pts. wt. Bacillus amyloliquefaciens, 3-5 pts. wt. potassium humate, 7-14 pts. wt. perlite, 5-7 pts. wt. calcium chloride, 2-4 pts. wt. humic acid, 6-10 pts. wt. ammonium hydrogen carbonate, 1-3 pts. wt. sodium silicate, 2-6 pts. wt. amino acid, 1-5 pts. wt. biogas residue, 3-6 pts. wt.peat and 8-16 pts. wt. soybean cake.    USE - Fertilizer composition.    ADVANTAGE - The fertilizer composition prevents soil and environment pollution, increase crop quality and improves soil structure.
NOVELTY - Melon fertilizer comprises 20-30 pts. wt. chicken manure, 2-4 pts. wt. effective microorganism (EM) fertilizer, 5-7 pts. wt. biological potash, 5-7 pts. wt. peat, 2-4 pts. wt. zinc sulfate, 6-8 pts. wt. nitrogen fertilizer, 10-12 pts. wt. potassium sulfate, 16-18 pts. wt. potassium fertilizer, 4-6 pts. wt. soil heat preservation agent, 2-4 pts. wt. carbendazim, 6-8 pts. wt. calcium superphosphate, 1-3 pts. wt. fermented strain and 10-12 pts. wt. phosphate fertilizer.    USE - The fertilizer is useful for preventing diseases in melon.    ADVANTAGE - The fertilizer increases yield of melon.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves uniformly mixing the above-mentioned raw materials, heating the mixture, preparing mixture into slurry, granulating slurry and spray-drying granule.
NOVELTY - Fertilizer for celery comprises 20-22 pts. wt. nitrogen, 18-20 pts. wt. phosphate, 15-17 pts. wt. potassium, 10-12 pts. wt. calcium, 0.6-0.8 pt. wt. starch, 30-40 pts. wt. corn straw, 0.5-0.7 pt. wt. Bacillus thuringiensis, 0.4-0.6 pt. wt. plant growth regulator, 0.3-0.5 pt. wt. B.subtilis, 3-5 pts. wt. fulvic acid, 0.7-0.9 pt. wt. Lactobacillus, 1-3 pts. wt. leavening agent, and 20-30 pts. wt. peat.    USE - The fertilizer is useful for celery (claimed).    ADVANTAGE - The fertilizer improves yield, quality and disease resistance ability of plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves uniformly mixing the above-mentioned raw materials, and heating and granulating obtained mixture.
NOVELTY - Gordon euryale seed fertilizer comprises 15-17 pts. wt. nitrogenous fertilizer, 15-17 pts. wt. phosphate fertilizer, 7-9 pts. wt. potash fertilizer, 100-120 pts. wt. dairy manure, 20-30 pts. wt. oil residue, 10-12 pts. wt. shell powder, 50-60 pts. wt. protein slurry, 20-30 pts. wt. plant ash, 8-10 pts. wt. gelatin, 3-5 pts. wt. diluent, 20-30 pts. wt. mushroom slag, and 10-12 pts. wt. silkworm excrement.    USE - Used as G. euryale seed fertilizer (claimed).    ADVANTAGE - The fertilizer: can be applied for one-time, thus saving time; meets the requirement of G. euryale nitrogen, phosphorus and potassium nutrient release; reduces fertilizer loss; and improves yield and quality of G. euryale.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the Gordon euryale seed fertilizer, comprising crushing the above components by a crusher and fermenting in a sealed jar, pre-heating a screw mixer to 70-80 degrees C, maintaining the temperature, adding the material into a reciprocating single-screw kneader, opening the screw mixer, maintaining mold head pressure to be 1.2-1.4 Mpa and spraying to form granular fertilizer.
NOVELTY - Fertilizer comprises 10-12 pts. wt. nitrogenous fertilizer, 8-10 pts. wt. phosphate fertilizer, 7-9 pts. wt. potash fertilizer, 80-100 pts. wt. chicken manure, 20-30 pts. wt. bean cake, 5-7 pts. wt. bitter bean, 10-12 pts. wt. peach, 20-30 pts. wt. soybean, 8-10 pts. wt. Chinese honeylocust tree leaves, 30-40 pts. wt. protein mud, 30-40 pts. wt. plant ash and 8-10 pts. wt. shell powder.    USE - Fertilizer.    ADVANTAGE - The fertilizer is safe and environment-friendly, and reduces plant diseases and controls insect pests without toxic component.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) crushing raw materials in a crusher;    (B) fermenting the crushed material in a jar;    (C) pre-heating the obtained mixture in a screw mixer to 80-100 degrees C;    (D) maintaining the head pressure of the mold to 2.0-2.2 magapascal; and    (E) granulating the obtained material to obtain the desired product.
NOVELTY - A pharmaceutical intermediate is obtained by dissolving raw material in a solvent at room temperature, adding an oxidant and iodine, stir-reacting for 3-8 hours at room temperature, detecting reaction completion by thin-layer chromatography, slowly adding water, separating out solid, filtering, and water-washing.    USE - Synthesis of pharmaceutical intermediate (claimed).    ADVANTAGE - The method enables simple and environmentally-friendly large-scale synthesis of pharmaceutical intermediate with high yield.
NOVELTY - A taxol-preparing plant extract is obtained by drying leaves, pulverizing dried raw materials, leaching with a mixed solvent of acetone and ethyl acetate, extracting concentrate under reduced pressure to obtain extract, chloroform-water extracting mixture and concentrating to obtain crude extract, subjecting crude extract to fixed-phase alumina column chromatography and reversed-phase 18C-silica gel column chromatography and recrystallizing with ethanol.    USE - Plant extract is used for preparing taxol.    ADVANTAGE - The plant extract having high content of taxol and purity is economically and environmentally-friendly prepared, by simple method.
NOVELTY - This utility new type claims a one pyrogenation gastification furnace for life garbage gasification furnace discharging device, the lower part comprising pyrolysis gasification furnace, a temperature induction switch conveyor belt, conveyor belt is set on discharge wherein a pyrolysis gasification furnace, temperature induction switch is set on inner pyrolysis gasification furnace, temperature induction switch connected in series in pyrolysis gasification furnace discharging motor and power supply, temperature induction switch connected in series in conveying motor and power supply. After using a technology plan, this utility new type one a pyrogenation gastification furnace for life garbage gasification furnace discharging device, without the need to participate and guarantee the safety of production, effectively increase the production efficiency and reduce the production cost.
NOVELTY - This new utility model claims of one of pyrogenation gastification furnace for life garbage gasification furnace, comprising gasification furnace main body, kick-out device, a controllable air tube, uniform cloth wind machine and automatic discharging device, the kicking place on top part gasification in the furnace body, the air suction pipe has multiple controllable one, vertically evenly distributed gasification in the furnace body inner wall, and fuel gas pipe connect, in the uniform cloth wind machine is set on gasification furnace body the bottom, of ash plate, the automatic discharging device is set on gasification furnace main body bottom. After using the technology scheme, this utility model new one of pyrogenation gastification furnace for life garbage gasification furnace can make household garbage for roadside market uniformly flat in pyrolysis gasification furnace in the pyrolytic gasification uniformity but use of carrying out full, can effective control of the temperature in every furnace, using pyrolysis gasification of stable process, cloth wind is uniform throughout the full pyrolysis gasification material supply; the safety is good, the production efficiency high.
NOVELTY - This new utility model claims of a kind of one can reduce environmental pollute the wooden meal preparing particle system, comprising raw material chamber, feeding machine and wooden meal preparing particle machine, feeding the two terminal respectively connect the storage bin and wooden meal and preparing particle machine, used for taking the material in material chamber and transporting wood to wood chips made particle storing and carrying out pelletizing machine, wherein, the wooden meal preparing particle system also comprises fan and dust removing device, the dust removing device and discharge port and the wooden meal preparing particle machine connected, the fan and the dust removing device connected, used for using the wooden meal preparing particle machine discharging the waste gas in the dust removing device and carrying out gas-solid separating process. The utility model new the wooden meal preparing particle system can wooden meal preparing particle machine for discharging the waste gas processing process, reducing of environment pollute, improving of work room air quality, and by de-dusting device to collect the wooden meal powder also can be back to the raw material chamber, for recycling use.
NOVELTY - This new type utility claims a combined household garbage one bar making machine combined add material device, comprising a, a stirrer, add additive device, quicklime add device, a humidifying device, transmission device and machine, the hopper is add material mixer, additive device add a stirrer inner material add additive, quicklime add. a stirrer inner add quicklime, the humidifying device is a stirrer inner material add water, the transmission device the stir is good material by stirrer to inner conveying machine. After using a technology plan, this utility new type one a combined domestic garbage in bar making machine combined add material device, arrangement structure is scientific and reasonable, it can effectively realize garbage rod continuous efficient of production, the made of garbage rod material quality is good.
NOVELTY - This utility model claims a high gas output environment-friendly marsh gas pool, wherein, fermentation pool by solar energy heat absorbing wall (1) and inner wall (2) compose the solar energy heat absorbing wall (1) and inner wall (2) is filled between water in the fermentation pool set with temperature sensor (4) and heating pipe (10), temperature sensor (4) and heating tube (10) and a controller (5) is connected and set with a feeding pool in two side fermentation pool is (6) and discharging pool (11), the upper end of the fermentation pool set with air outlet (7), a pool body right side of fermentation pool. acidification tank (8), acidification tank (8) through liquid (9) and the fermentation pool connected, pool body left side of fermentation pool water inlet pipe through a water pressure tank (3). Heat preservation effect obvious, the methane pool a year maintain a fermentation in a relative stable of temperature, using acidizing is acidizing pool to promote ferment pool ferment, water pressure tank and fermenting pool, regulating pool inner pressure, to increase quantity of gas.
NOVELTY - This utility new type claims a one and pig gas happen device, the lower part comprising Anaerobic respiration chamber and oxygen breathing chamber, Anaerobic respiration chamber through a door mounted in aerobic respiration chamber right front side, Anaerobic respiration chamber set with the liquid collecting chamber, the Anaerobic respiration chamber and between the liquid chamber set with a clapboard, the aerobic respiratory chamber a set with one feeding groove and one of a collecting liquid cabin and a gas-guide tube is above the Anaerobic respiration chamber set with a collecting bin, the top end of this collecting bin is set with discharge pipe, the discharge pipe set with a switch valve one, a liquid collecting chamber right side set with a discharging pipe, the discharging pipe set with a switch valve a, the upper oxygen breathing chamber is further set with a door for a turntable, one is a structure is reasonable, operation is convenient, which avoids environment pollution and pig peripheral use rate is high and pig gas happen device.
NOVELTY - The system comprises two fermentation tanks and adjusting vehicles, where each of the tanks is provided with a first track along the length of the tank. A first rail is movable on the tanks, where the first rail includes a scheduling car, a walking frame, a walking assembly, and a control assembly. The walking frame supports and moves the compost turners. A second rail is disposed perpendicular to the traveling direction of the walking frame. The control assembly is disposed in front and rear ends of the walking frame.    USE - The wrapping system is useful for bacterial residue fermentation conversion humus compost turners.    DETAILED DESCRIPTION - The system comprises two fermentation tanks and adjusting vehicles, where each of the tanks is provided with a first track along the length of the tank. A first rail is movable on the tanks, where the first rail includes a scheduling car, a walking frame, a walking assembly, and a control assembly. The walking frame supports and moves the compost turners. A second rail is disposed perpendicular to the traveling direction of the walking frame. The control assembly is disposed in front and rear ends of the walking frame for controlling the turners to be moved between the fermentation tanks and the walking frame. The walking assembly includes a walking wheel and a driving device mounted in an inner surface of the walking wheel. The control assembly includes a stroke switch arranged in a front end of the walking frame, and a stopper arranged in a rear end of the walking frame. A funnel is set in an inner surface of the walking frame. A lower part of the funnel is provided with an opening.
NOVELTY - Bio-fertilizer comprises 50-60 pts. wt. rice straw, 25-35 pts. wt. corn straw, 14-36 pts. wt. soybean straw, 10-18 pts. wt. potato, 21-35 pts. wt. chicken manure, 10-15 pts. wt. duck manure, 4-6 pts. wt. diammonium phosphate, 12-24 pts. wt. mustard straw, 12-24 pts. wt. flax straw, 10-13 pts. wt. marijuana stalk, 14-25 pts. wt. sunflower straw, 0.1-0.3 pt. wt. Bdellovibrio (powder), 0.1-0.2 pt. wt. bacteriophage (powder), 0.1-2 pt. wt. Oceanospirillales powder, 50-60 pts. wt. sewage sludge and 0.1-0.2 pt. wt. fermentation agent.    USE - As bio-fertilizer.    ADVANTAGE - The bio-fertilizer is cost-effective, and enables to increase quality of crops, and has balanced nutrition.
NOVELTY - Preparing Tricholoma lobayense cultivation log involves crushing dried banana stem, and leaves, mixing crushed banana stem, and leaves, bagasse, wheat bran, quicklime, and water, piling the mixture, carrying out anaerobic fermentation of the mixture, packing the culture substrate in a plastic bag of specification of 25x 52 cm, sterilizing the bag, selecting thick and white T.lobayense with good growth rate, planting the selected T.lobayense on the substrate under aseptic conditions, and cultivating T.lobayense.    USE - The method is useful for preparing T.lobayense cultivation log (claimed).    ADVANTAGE - The method is cost-effective, and suitable for large-scale production of T.lobayense, increases income of farmers, and does not cause pollution.    DETAILED DESCRIPTION - Preparing Tricholoma lobayense cultivation log involves (a) sun drying banana stem, and leaves to a moisture content of 10-13%, crushing dried materials, and sieving the crushed materials through a sieve of 20-30 mesh, (b) taking 76% crushed banana stem, and leaves, 13% bagasse, 8% wheat bran, 2% quicklime, and suitable amount of water, (c) mixing the above-mentioned materials, adding water to the mixture, and adjusting moisture content of the mixture to 55-60%, (d) piling the mixture to a height of 1 m, and width of 2 m, covering the pile tightly with a plastic film, and carrying out anaerobic fermentation of the mixture at 60 degrees C for 3-4 days until the mixture turns brown or dark brown to obtain culture substrate, (e) packing the culture substrate in a plastic bag of specification of 25x 52 cm, and sterilizing the bag, (f) selecting thick and white T.lobayense with good growth rate, (g) planting the selected T.lobayense on the substrate under aseptic conditions, and (h) cultivating T.lobayense.
NOVELTY - Wood tar extracting tank door viewing port, one is used for the plant in a plant extract insecticidal pesticide a pyroligneous liquor plant acid components of prior product, observation device of mother liquid wood tar extracting tank door, wherein a base, wherein two cover compose part, round hole seat inner diameter 0.1, wherein circular cover outside diameter 0.15, wherein base upper part outside edge and wherein cover inner wall with screw thread, and wherein b wherein base cover is screwed into one circular opening, upper side plane hole seat is provided with a concave groove of the seal material.
NOVELTY - This new utility model claims of one of continuous microwave heating biomass and organic garbage cracking device, microwave dryer (1) and outlet joint feeding hoisting machine (2) and import, a feeding hoisting machine (2) and outlet joint storage bin (3), carrying on hopper (3) and outlet joint feedstock spiral transporting machine (4) and import, and the spiral transporting machine (4) and outlet joint microwave cracking furnace body (5), and the microwave cracking furnace body (5) and outlet joint material spiral transporting machine (6), and the microwave cracking furnace body (5) is equipped with upper control temperature device, oxygen dividing pressure detecting device, a safety valve, an atmosphere pipeline system (7), a microwave feed enter system (8), a waste gas collecting and separating system (9), a cooling water system (10), control system (11) and atmosphere system (12). This utility new type is one of heating temperature low, response speed is fast, processing biomass and organic waste with high quality continuous microwave heating biomass and organic garbage cracking device.
NOVELTY - Marsh gas pool new type structure of the new utility model claims one kind of new type structure of marsh gas pool, comprising main pool and water in pressure, of gas storage room and ferment pool formed, top part is air storage chamber set with air guide pipe, one side main pool is provided with manure for mouth, the other side and water pressure in communicated, in hydraulic set with overflow port for mouth excrement fermentation pool is located on side wall of the fermentation pool and water pressure in between provided with manure outlet port, the outlet port at the other side wall manure ferment pool is over, carrying on excrement port is along and out of top end of excrement port located on the same one horizontal line of the bottom of fermentation pool excrement port at the side wall start to hydraulic direction downward incline, and extending to the overflow port in water flow pressure at the side wall, feces guiding flow the spherical ferment pool and pool bottom section provided with present inner concave half way, gas storage chamber whole present upper narrow lower wide is trapezoid, carrying on excrement port at along the gas storage room is set on side wall of bottom end of gas-guide tube is trapezoid and top, gas-guide tube provided with insurance valve, the target wherein one of supply pressure constant, suitable, not easy to crust and gas generating amount is large.
NOVELTY - Controlling weed involves irrigating rice in paddy field. Water is flooded in paddy field with high piers for two days. The water is stored for 3-5 days. Pretilachlor complexing agent is sprayed directly on the water layer of the rice fields to control growth of single and double leaves weeds in the paddy field.    USE - Method for controlling weed from rice (claimed).    ADVANTAGE - The method is simple, safe, environment-friendly and cost-effective, and has improved weeding effect and yield of rice.
NOVELTY - Method for treating catering waste, involves (a) collecting and processing solid waste by collecting solid waste including plastic bags, bottles, caps, broken bowl collected after removal and chopsticks, (b) processing solid materials including bones into fertilizer additive, and (c) collecting and processing food waste by fermentation and vermiculture method.    USE - The method is useful for treating catering waste into organic fertilizer (claimed).    ADVANTAGE - The method turns catering waste into valuable organic fertilizer and protects the environment.    DETAILED DESCRIPTION - Method for treating catering waste, involves (a) collecting and processing solid waste by collecting solid waste including plastic bags, bottles, caps, broken bowl collected after removal and chopsticks, (b) processing solid materials including bones into fertilizer additive, and (c) collecting and processing food waste by selecting aqueous leftover rice, pasta and meat residue, mixing, maintaining 85-95% moisture content of the mixture, subjecting to pump pressure filter machine, obtaining the filtrate and residue respectively, mixing the filtrate with biological sewage deodorant, liquid oxygen and microbial cells, fermenting the mixture, performing vermiculture using the fermented mixture, selecting and maintaining specific earthworms after breeding season for next batch cultivation, mixing the fermented mixture with chicken manure, processed solid materials and pig manure, and using the vermicompost as fertilizer.
NOVELTY - Culture base material comprises corn stalk, livestock or poultry manure, and gypsum in a dry weight ratio of 0.5-1.5:0.3-1:0.03-0.1.    USE - The culture base material is useful for Agaricus bisporus (claimed).    ADVANTAGE - The culture base material is prepared using easily available inexpensive raw materials, and has increased compost quality and increased production benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the above-cited culture base material, which involves mixing corn stalk, and livestock or poultry manure, pre-wetting the mixture until the moisture content is 79-80%, piling the mixture, stacking, spraying gypsum on the stacked materials, fermenting the mixture twice, and processing the fermented mixture.
NOVELTY - Method for preparing nutrition base for apricot spore mushroom, involves using 20-30% potato powder, 15-30% cottonseed hulls, 2-7% gypsum powder, 45-60% wheat and 5-15% auxiliary materials.    USE - The method is useful for preparing nutrition base for apricot spore mushroom (claimed).    DETAILED DESCRIPTION - Method for preparing nutrition base for apricot spore mushroom, involves using 20-30% potato powder, 15-30% cottonseed hulls, 2-7% gypsum powder, 45-60% wheat and 5-15% auxiliary materials. The method involves (a) crushing cottonseed hulls and wheat into particles of 1-2 cm, and mixing the crushed materials with potato powder and 80-90% water, (b) performing primary fermentation of the mixture for 10-15 days, (c) adding gypsum powder and auxiliary materials to the fermented mixture, and subjecting to secondary fermentation, (d) performing primary sterilization of the fermented mixture, (e) subjecting to secondary sterilization, and (f) packing the sterile mixture, where the fermentation is performed at 18-25 degrees C and humidity of 85-92%.
NOVELTY - Method for preparing nutrition base for apricot spore mushroom, involves using 25-30% potato powder, 20-30% cottonseed, 1-5% quicklime, 30-50% wheat, 5-10% sucrose and 10-15% auxiliary materials.    USE - The method is useful for preparing nutrition base for apricot spore mushroom (claimed).    DETAILED DESCRIPTION - Method for preparing nutrition base for apricot spore mushroom, involves using 25-30% potato powder, 20-30% cottonseed, 1-5% quicklime, 30-50% wheat, 5-10% sucrose and 10-15% auxiliary materials. The method involves (a) crushing cottonseed and wheat into particles of 1-2 cm, and mixing the crushed materials with potato powder and 80-90% water, (b) performing primary fermentation of the mixture for 10-15 days, (c) adding quicklime powder, sucrose and auxiliary materials to the fermented mixture, and subjecting to secondary fermentation, (d) performing primary sterilization of the fermented mixture, (e) subjecting to secondary sterilization, and (f) packing the sterile mixture, where the fermentation is performed at 18-25 degrees C and humidity of 85-92%.
NOVELTY - Method for preparing nutrition base for apricot spore mushroom, involves using 10-15% corn core, 20-30% cottonseed hull, 1-5% quicklime, 40-60% wheat, 10-15% glucose and 5-15% auxiliary materials.    USE - The method is useful for preparing nutrition base for apricot spore mushroom (claimed).    DETAILED DESCRIPTION - Method for preparing nutrition base for apricot spore mushroom, involves using 10-15% corn core, 20-30% cottonseed hull, 1-5% quicklime, 40-60% wheat, 10-15% glucose and 5-15% auxiliary materials. The method involves (a) crushing cottonseed and corn core into particles of 1-2 cm, and mixing the crushed materials with 80-90% water, (b) performing primary fermentation of the mixture for 10-15 days, (c) adding quicklime powder, wheat, glucose and auxiliary materials to the fermented mixture, and subjecting to secondary fermentation, (d) performing primary sterilization of the fermented mixture, (e) subjecting to secondary sterilization, and (f) packing the sterile mixture, where the fermentation is performed at 18-25 degrees C and humidity of 85-92%.
NOVELTY - Method for preparing nutrition base for golden needle mushroom, involves using 30-40% Linum usitatissimum, 10-20% sawdust, 5-8% quicklime, 15-25% soybean meal, 10-20% Sorghum and 5-15% corn core.    USE - The method is useful for preparing nutrition base for golden needle mushroom (claimed).    DETAILED DESCRIPTION - Method for preparing nutrition base for golden needle mushroom, involves using 30-40% Linum usitatissimum, 10-20% sawdust, 5-8% quicklime, 15-25% soybean meal, 10-20% Sorghum and 5-15% corn core. The method involves (a) crushing L.usitatissimum, sawdust and corn core uniformly, and mixing the crushed materials with 80-90% water, (b) performing primary fermentation of the mixture for 12-15 days, (c) adding quicklime to the fermented mixture, and performing primary sterilization of the fermented mixture, (d) adding soybean meal and Sorghum, and subjecting to secondary fermentation for 2-3 days, (e) performing secondary sterilization of the fermented mixture, and (f) packing the sterile mixture, where the fermentation is performed at 17-22 degrees C and humidity of 85-90%.
NOVELTY - Method for preparing nutrition base for golden needle mushroom, involves using 40-55% wheat straw, 10-20% sawdust, 5-8% gypsum powder, 10-20% soybean meal, 20-30% potato powder and 5-10% corn core.    USE - The method is useful for preparing nutrition base for golden needle mushroom (claimed).    DETAILED DESCRIPTION - Method for preparing nutrition base for golden needle mushroom, involves using 40-55% wheat straw, 10-20% sawdust, 5-8% gypsum powder, 10-20% soybean meal, 20-30% potato powder and 5-10% corn core. The method involves (a) crushing wheat straw, sawdust and corn core uniformly, and mixing the crushed materials with 80-90% water, (b) performing primary fermentation of the mixture for 12-15 days, (c) adding gypsum powder to the fermented mixture, and performing primary sterilization of the fermented mixture, (d) adding soybean meal and potato powder, and subjecting to secondary fermentation for 2-3 days, (e) performing secondary sterilization of the fermented mixture, and (f) packing the sterile mixture, where the fermentation is performed at 17-22 degrees C and humidity of 85-90%.
NOVELTY - Method for preparing nutrition base for Hypsizygus marmoreus and Tricholoma matsutake, involves using 35-50% wheat straw, 10-20% dairy manure, 5-15% soybean meal, 5-10% corn powder, 8-10% calcium carbonate and 10-20% auxiliary materials.    USE - The method is useful for preparing nutrition base for H.marmoreus and T.matsutake (claimed).    DETAILED DESCRIPTION - Method for preparing nutrition base for Hypsizygus marmoreus and Tricholoma matsutake, involves using 35-50% wheat straw, 10-20% dairy manure, 5-15% soybean meal, 5-10% corn powder, 8-10% calcium carbonate and 10-20% auxiliary materials. The method involves (a) crushing wheat straw into particles of 1-2 cm, and mixing the crushed materials with dairy manure, soybean meal, corn powder and 80-90% water, (b) performing primary fermentation of the mixture for 10-15 days, (c) adding calcium carbonate and auxiliary materials to the fermented mixture, and subjecting to secondary fermentation, (d) performing primary sterilization of the fermented mixture, (e) subjecting to secondary sterilization, and (f) packing the sterile mixture, where the fermentation is performed at 18-25 degrees C and humidity of 85-93%.
NOVELTY - Method for preparing nutrition base for Hypsizygus marmoreus and Tricholoma matsutake, involves using 30-40% wheat straw, 10-20% dairy manure, 5-15% peanut shell, 20-30% bran, 5-10% phosphate fertilizer and 5-10% auxiliary materials.    USE - The method is useful for preparing nutrition base for H.marmoreus and T.matsutake (claimed).    DETAILED DESCRIPTION - Method for preparing nutrition base for Hypsizygus marmoreus and Tricholoma matsutake, involves using 30-40% wheat straw, 10-20% dairy manure, 5-15% peanut shell, 20-30% bran, 5-10% phosphate fertilizer and 5-10% auxiliary materials. The method involves (a) crushing wheat straw into particles of 1-2 cm, and mixing the crushed materials with dairy manure, peanut shell, bran and 80-90% water, (b) performing primary fermentation of the mixture for 10-15 days, (c) adding phosphate fertilizer and auxiliary materials to the fermented mixture, and subjecting to secondary fermentation, (d) performing primary sterilization of the fermented mixture, (e) subjecting to secondary sterilization, and (f) packing the sterile mixture, where the fermentation is performed at 18-25 degrees C and humidity of 85-93%.
NOVELTY - Method for preparing nutrition base for Hypsizygus marmoreus and Tricholoma matsutake, involves using 40-50% wheat straw, 10-20% pig manure, 5-15% cottonseed hulls, 5-10% corn powder, 20-30% phosphate fertilizer and 8-10% auxiliary materials.    USE - The method is useful for preparing nutrition base for H.marmoreus and T.matsutake (claimed).    DETAILED DESCRIPTION - Method for preparing nutrition base for Hypsizygus marmoreus and Tricholoma matsutake, involves using 40-50% wheat straw, 10-20% pig manure, 5-15% cottonseed hulls, 5-10% corn powder, 20-30% phosphate fertilizer and 8-10% auxiliary materials. The method involves (a) crushing wheat straw into particles of 1-2 cm, and mixing the crushed materials with pig manure, cottonseed hulls, corn powder and 80-90% water, (b) performing primary fermentation of the mixture for 10-15 days, (c) adding phosphate fertilizer and auxiliary materials to the fermented mixture, and subjecting to secondary fermentation, (d) performing primary sterilization of the fermented mixture, (e) subjecting to secondary sterilization, and (f) packing the sterile mixture, where the fermentation is performed at 18-25 degrees C and humidity of 85-93%.
NOVELTY - Method for preparing nutrition base for Hypsizygus marmoreus and Tricholoma matsutake, involves using 40-50% wheat straw, 10-20% dairy manure, 5-15% cottonseed hulls, 10-20% corn powder, 8-10% calcium carbonate and 5-10% auxiliary materials.    USE - The method is useful for preparing nutrition base for H.marmoreus and T.matsutake (claimed).    DETAILED DESCRIPTION - Method for preparing nutrition base for Hypsizygus marmoreus and Tricholoma matsutake, involves using 40-50% wheat straw, 10-20% dairy manure, 5-15% cottonseed hulls, 10-20% corn powder, 8-10% calcium carbonate and 5-10% auxiliary materials. The method involves (a) crushing wheat straw into particles of 1-2 cm, and mixing the crushed materials with dairy manure, cottonseed hulls, corn powder and 80-90% water, (b) performing primary fermentation of the mixture for 10-15 days, (c) adding calcium carbonate and auxiliary materials to the fermented mixture, and subjecting to secondary fermentation, (d) performing primary sterilization of the fermented mixture, (e) subjecting to secondary sterilization, and (f) packing the sterile mixture, where the fermentation is performed at 18-25 degrees C and humidity of 85-93%.
NOVELTY - Method for preparing nutrition base for Hypsizygus marmoreus and Tricholoma matsutake, involves using 30-45% crop straw, 15-25% dairy manure, 10-20% peanut shell, 20-30% bran, 8-10% calcium carbonate and 5-10% auxiliary materials.    USE - The method is useful for preparing nutrition base for H.marmoreus and T.matsutake (claimed).    DETAILED DESCRIPTION - Method for preparing nutrition base for Hypsizygus marmoreus and Tricholoma matsutake, involves using 30-45% crop straw, 15-25% dairy manure, 10-20% peanut shell, 20-30% bran, 8-10% calcium carbonate and 5-10% auxiliary materials. The method involves (a) crushing crop straw into particles of 1-2 cm, and mixing the crushed materials with dairy manure, peanut shell, bran and 80-90% water, (b) performing primary fermentation of the mixture for 10-15 days, (c) adding calcium carbonate and auxiliary materials to the fermented mixture, and subjecting to secondary fermentation, (d) performing primary sterilization of the fermented mixture, (e) subjecting to secondary sterilization, and (f) packing the sterile mixture, where the fermentation is performed at 18-25 degrees C and humidity of 85-93%.
NOVELTY - Method for preparing nutrition base for Hypsizygus marmoreus and Tricholoma matsutake, involves using 30-45% plant straw, 10-20% dairy manure, 5-15% cottonseed hulls, 20-30% bran, 8-10% calcium carbonate and 5-10% auxiliary materials.    USE - The method is useful for preparing nutrition base for H.marmoreus and T.matsutake (claimed).    DETAILED DESCRIPTION - Method for preparing nutrition base for Hypsizygus marmoreus and Tricholoma matsutake, involves using 30-45% plant straw, 10-20% dairy manure, 5-15% cottonseed hulls, 20-30% bran, 8-10% calcium carbonate and 5-10% auxiliary materials. The method involves (a) crushing plant straw into particles of 1-2 cm, and mixing the crushed materials with dairy manure, cottonseed hulls, bran and 80-90% water, (b) performing primary fermentation of the mixture for 10-15 days, (c) adding calcium carbonate and auxiliary materials to the fermented mixture, and subjecting to secondary fermentation, (d) performing primary sterilization of the fermented mixture, (e) subjecting to secondary sterilization, and (f) packing the sterile mixture, where the fermentation is performed at 18-25 degrees C and humidity of 85-93%.
NOVELTY - Organic functional fertilizer for alkaline soil, comprises 25-60 pts. wt. tobacco waste, 10-50 pts. wt. livestock and poultry excrement, 10-20 pts. wt. soil pH regulator, 5-15 pts. wt. humic acid and 0.2-3 pts. wt. composite microbial inoculum. The soil pH regulator contains vinegar residue, plant ash, sulfur or calcium hydroxide. The composite microbial inoculum comprises cellulose decomposing bacteria, Bacillus subtilis, lactic acid bacteria, thermophilic fungi, rod-shaped bacteria and Trichoderma.    USE - The organic functional fertilizer is useful for alkaline soil (claimed) to regulate the soil pH.    ADVANTAGE - The organic functional fertilizer prevents heavy metal poisoning and other harmful effects on crops.    DETAILED DESCRIPTION - Organic functional fertilizer for alkaline soil, comprises 25-60 pts. wt. tobacco waste, 10-50 pts. wt. livestock and poultry excrement, 10-20 pts. wt. soil pH regulator, 5-15 pts. wt. humic acid and 0.2-3 pts. wt. composite microbial inoculum. The soil pH regulator contains vinegar residue, plant ash, sulfur or calcium hydroxide. The composite microbial inoculum comprises cellulose decomposing bacteria, Bacillus subtilis, lactic acid bacteria, thermophilic fungi, rod-shaped bacteria and Trichoderma. The tobacco waste comprises 35-55 pts. stalk, 30-40 pts. leaves and 20-40 pts. other tobacco residues. The livestock manure and poultry excrement comprises dairy manure, sheep manure and duck manure. An INDEPENDENT CLAIM is included for preparation of the above-cited organic functional fertilizer, which involves (a) crushing tobacco waste, mixing with animal waste in a ratio of 25:1, fermenting the mixture for 60-80 degrees C for 7 days, mixing the fermented mixture with soil pH regulator and granulating the mixture, (b) stacking the granulated mixture and fermenting for 3 times, and (c) drying the fermented material, sieving the dried materials, and processing with other raw materials.
NOVELTY - Microbial fertilizer is prepared by mixing bio-fertilizer and mycorrhizal fungi in a weight ratio 1:9. The bio-fertilizer comprises microbial inoculant and carrier. The microbial inoculant is obtained by mixing Mesorhizobium huakuii and Agrobacterium obtained from root nodule of milkvetch.    USE - As microbial fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) preparing liquid medium by mixing 95-99.3 %mass soy milk, 0.2-0.8 %mass yeast extract, 0.1-0.5 %mass beef extract and 0.1-0.5 %mass peptone, and sterilizing mixture at 121 degrees C, (b) obtaining M.huakuii and Agrobacterium from root nodule of milkvetch, inoculating M.huakuii and Agrobacterium in liquid medium in a volume ratio of 1:15 and performing shake culture for 24 hours, (c) inoculating culture obtained in step (b) into second culture medium in a ratio of 1:10 and culturing for 24 hours, (d) inoculating culture obtained in step (c) into third culture medium in a ratio of 1:5 and culturing for 24 hours, (e) preparing substrate by mixing soybean meal, bamboo shavings, wheat bran, and monoammonium phosphate in a weight ratio of 1:2:3:1, crushing mixture, sieving crushed raw material using 60 mesh sieve, adding mixture into tank, stirring uniformly, adding 0.02-0.08 %mass ammonium formate and 0.002-0.008 %mass sodium sulfate, mixing uniformly, sterilizing mixture at 121 degrees C for 2 hours, and cooling mixture to 28 degrees C, (f) adding liquid culture medium to substrate obtained in step (e) in a weight ratio of 1:4, adding mixture into stirred-tank reactor, stirring mixture at high temperature for 30 minutes, adding 0.05-0.2 %mass zinc sulfate, 0.01-0.05 %mass sodium sulfate and 0.01-0.05 %mass ammonium formate, stirring uniformly and fermenting mixture, and (g) mixing fermented product with mycorrhizal fungi in a weight ratio of 9:1 to obtain the product.
NOVELTY - Organic biofertilizer comprises 50-90 pts. wt. livestock and poultry manure, 4-9 pts. wt. sodium dihydrogen phosphate, 5-6 pts. wt. disodium hydrogen phosphate, 6-15 pts. wt. sodium tripolyphosphate, 12-24 pts. wt. large mustard straw, 12-24 pts. wt. flax straw, 10-13 pts. wt. hemp straw, 14-25 pts. wt. sunflower straw, 0.1-0.3 pts. wt. Bdellovibrio powder, 0.1-0.2 pts. wt. bacteriophage powder, 0.1-2 pts. wt. Oceanospirillales powder, 50-60 pts. wt. sewage sludge, and 0.1-0.2 pts. wt. fermented fungus.    USE - As organic biofertilizer.    ADVANTAGE - The biofertilizer is rich in beneficial microorganisms, has balanced nutrition and increases soil organic matter content.
NOVELTY - Fertilizer comprises livestock and poultry manure, straw, attapulgite powder, calcium superphosphate, ammonium nitrate, potassium chloride, boric acid, polyacrylamide, lignosulfonate, wintergreen oil, camphor oil, effective microorganism, film coating agent, and water. The film coating agent comprises 2-(dimethylamino)ethyl acrylate, dimethylaminoethyl methacrylate, magnesium sulfate, 2-ethylhexyl phosphate, triallyl cyanurate as cross-linker, nanocarbon, and maifan stone powder.    USE - As fertilizer in a form of granule for flowers (claimed).    ADVANTAGE - The fertilizer replenishes soil organic matter, and increases water retention capacity of soil and survival rate of flowers.    DETAILED DESCRIPTION - Fertilizer comprises 100-120 pts. wt. livestock and poultry manure, 50-55 pts. wt. straw, 12-14 pts. wt. attapulgite powder, 30-34 pts. wt. calcium superphosphate, 14-18 pts. wt. ammonium nitrate, 16-19 pts. wt. potassium chloride, 3-4 pts. wt. boric acid, 2-3 pts. wt. polyacrylamide, 1-2 pts. wt. lignosulfonate, 2-3 pts. wt. wintergreen oil, 1-2 pts. wt. camphor oil, 3-4 pts. wt. effective microorganism, 4-6 pts. wt. film coating agent, and suitable amount of water, where the fertilizer is prepared by mixing the raw materials, and grinding the mixture. The film coating agent comprises 2-3 pts. wt. 2-(dimethylamino)ethyl acrylate, 1-2 pts. wt. dimethylaminoethyl methacrylate, 1-2 pts. wt. magnesium sulfate, 2-3 pts. wt. 2-ethylhexyl phosphate, 1-2 pts. wt. triallyl cyanurate as cross-linker, 0.1-0.2 pt. wt. nanocarbon, and 2-3 pts. wt. maifan stone powder.
NOVELTY - A biomass fuel pellet is produced by directly using or drying waste slurry from paper mill, crushing into less than or equal to 5 mm powder using crusher, screening dried sawdust using sieve screen or screen, removing greater than or equal to 5 mm timber, drying combustible crop straw, such as agricultural wasted peanut shell, rice hull, and corn straw, crushing into less than or equal to 5 mm powder, mixing waste paper pulp and sawdust or crop straw, extruding, and adding non-toxic and odorless adhesive or combustion improver.    USE - Production of biomass fuel pellet (claimed).    ADVANTAGE - Process is simple, energy-saving, and smooth and has fast speed and high production efficiency, product does not emit toxic sulfur gas and has improved adhesion, better combustion effect, and good quality, and raw material is low cost and environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows an image of produced biomass fuel pellet using environment-friendly waste paper pulp. (Drawing includes non-English language text).
NOVELTY - A granular solid biomass fuel is prepared by drying blue-green algae from Taihu Lake and other wasted biomass material having moisture content of 8-25%, mechanically crushing other wasted biomass material into 5-10 mm, uniformly mixing 10-100 wt.% dried blue-green algae from Taihu Lake and 0-90 wt.% other wasted biomass material, and molding into molding machine at 70-170 degrees C having pressure of 100-300 MPa.    USE - Preparation of granular solid biomass fuel (claimed).    ADVANTAGE - Process is simple and environment-friendly, reduces production cost, and uses stable machine, raw material is low cost and has rich source, and product has improved combustion property, high yield, and long service life.
NOVELTY - Microbial decomposition environmentally-friendly biomass fuel contains 0.0003-0.0006 pt. wt. phosphobacterial powder, 0.0003-0.0006 pt. wt. potassium bacterial powder, 0.0003-0.0006 pt. wt. silicate bacterial powder, 10-16 pts. wt. ethanol, 80-95 pts. wt. furfural residue, 4-8 pts. wt. Syzygium branches, 9-16 pts. wt. Davidia involucrate branches, 8-13 pts. wt. Kapok branches, 11-17 pts. wt. mulberry branches, 15-20 pts. wt. pine branches, 1-3 2p dry sandalwood tree branches, 6-14 pts. wt. peach branches and 5-9 pts. wt. oak branches.    USE - Microbial decomposition environmentally-friendly biomass fuel (claimed).    ADVANTAGE - The biomass fuel is lightweight and economical, has high flammable value, prolongs the combustion time, improves thermal efficiency, and reduces the generation of sulfur dioxide and carbon dioxide.    DETAILED DESCRIPTION - Microbial decomposition environmentally-friendly biomass fuel comprises 0.0003-0.0006 pt. wt. phosphobacteria powder, 0.0003-0.0006 pt. wt. potassium bacteria powder, 0.0003-0.0006 pt. wt. silicate bacteria powder, 10-16 pts. wt. ethanol, 80-95 pts. wt. furfural residue, 4-8 pts. wt. Syzygium branches, 9-16 pts. wt. Davidia involucrate branches, 8-13 pts. wt. Kapok branches, 11-17 pts. wt. mulberry branches, 15-20 pts. wt. pine branches, 1-3 2p dry sandalwood tree branches, 6-14 pts. wt. peach branches, 5-9 pts. wt. oak branches, 6-10 pts. wt. apricot branches, 55-60 pts. wt. soybean straw powder, 5-8 pts. wt. tert-butanol, 25-40 pts. wt. potato straw powder, 30-45 pts. wt. barley straw powder, 23-46 pts. wt. broad bean powder, and 45-50 pts. wt. wheat straw powder.
NOVELTY - Granular biofuel comprises 33-46 pts. wt. rice straw powder, 40-55 pts. wt. corn straw powder, 5-10 pts. wt. birch branches, 5-10 pts. wt. Sophora japonica branches, 5-10 pts. wt. dry Beech tree branches, 5-10 pts. wt. dry mangrove branches, 5-10 pts. wt. dry oak branches, 5-10 pts. wt. willow branches, 20-30 pts. wt. anthracite, 25-30 pts. wt. slime, 15-25 pts. wt. animal fat, 5-15 pts. wt. food waste, 9-16 pts. wt. sunflower straw powder, 20-30 pts. wt. rice husk powder, 10-15 pts. wt. chicken manure and 5-10 pts. wt. peat.    USE - Granular biofuel (claimed).    ADVANTAGE - The granular biofuel has calorific value of up to 5000 kcal, low ignition, excellent air permeability, high thermal efficiency, and increases combustion time from 1.5 hours to 3 hours.
NOVELTY - A biofuel formulation comprises 25-32 pts. wt. coal slurry, 30-40 pts. wt. rice straw powder, 44-50 pts. wt. corn straw powder, 50-60 pts. wt. soybean straw powder, 14-20 pts. wt. orange extract, 14-23 pts. wt. rice barn, 6-9 pts. wt. camphor tree branches, 1-2 pts. wt. cedar branches, 2-3 pts. wt. emulsifier, 4-6 pts. wt. methylhydroquinone and 1-3 pts. wt. di-tert-butylhydroquinone.    USE - Biofuel formulation (claimed).    ADVANTAGE - The biofuel formulation has excellent fluidity and storage stability for long period of time, and low pour point.
NOVELTY - A clean energy biofuel contains 13-25 pts. wt. oil seed straw powder, 25-30 pts. wt. coal powder, 33-46 pts. wt. sunflower straw powder, 40-56 pts. wt. rice husk, 15-30 pts. wt. soybean straw, 10-16 pts. wt. peat, 20-23 pts. wt. bauhinia branch, 11-17 pts. wt. rain dried twigs, 5-9 pts. wt. cortex albiziae branches, 1-3 pts. wt. patrinia scabiosaefolia branches, 5-9 pts. wt. isopropanol, 9-16 pts. wt. camphor wood, 8-13 pts. wt. oak tree chips, 10-15 pts. wt. large Yehuang Yang sawdust, 11-13 pts. wt. larch wood, and 12-16 pts. wt. herba schizonepetae chips.    USE - A clean energy biofuel (claimed).    ADVANTAGE - The biofuel is safe for the environment, raw materials are easy to obtain, and preparation process is simple.    DETAILED DESCRIPTION - A clean energy biofuel comprises 13-25 pts. wt. oil seed straw powder, 25-30 pts. wt. coal powder, 33-46 pts. wt. sunflower straw powder, 40-56 pts. wt. rice husk, 15-30 pts. wt. soybean straw, 10-16 pts. wt. peat, 20-23 pts. wt. bauhinia branch, 11-17 pts. wt. rain dried twigs, 5-9 pts. wt. cortex albiziae branches, 1-3 pts. wt. patrinia scabiosaefolia branches, 5-9 pts. wt. isopropanol, 9-16 pts. wt. camphor wood, 8-13 pts. wt. oak tree chips, 10-15 pts. wt. large Yehuang Yang sawdust, 11-13 pts. wt. larch wood, 12-16 pts. wt. herba schizonepetae chips, 12-18 pts. wt. masson pine sawdust, and 11-15 pts. wt. simao pine sawdust.
NOVELTY - Biofuel comprises 15-20 pts. wt. industrial ethanol, 1-2 pts. wt. combustion improver, 15-25 pts. wt. willow, 25-35 pts. wt. locust branches, 11-18 pts. wt. mustard straw powder, 10-16 pts. wt. flax straw powder, 20-25 pts. wt. waste cooking oil, 40-55 pts. wt. biomass, 5-9 pts. wt. Yunnan pine branches, 6-19 pts. wt. Platanus sawdust, 9-19 pts. wt. Davidia involucrata sawdust, 9-16 pts. wt. cotton sawdust, 3-8 pts. wt. kapok tree sawdust and 4-7 pts. wt. Bauhinia sawdust.    USE - As biofuel.    ADVANTAGE - The biofuel is environmentally-friendly and prepared without using chemicals and suitable for long time storage.
NOVELTY - Biomass fuel is prepared using industrial ethanol, combustion improver, broad bean straw powder, wheat straw powder, peanut straw powder, mung bean straw powder, cotton straw powder, oilseed straw powder, black walnut meal, lemon sawdust, sycamore tree wood meal, Davidia wooden meal, cotton wooden meal, java fern wooden meal, and Bauhinia wooden meal.    USE - As biomass fuel.    ADVANTAGE - The biomass fuel is environmentally-friendly and suitable for long-term storage.    DETAILED DESCRIPTION - Biomass fuel is prepared using 15-20 pts. wt. industrial ethanol, 1-2 pts. wt. combustion improver, 5-10 pts. wt. broad bean straw powder, 45-55 pts. wt. wheat straw powder, 30-45 pts. wt. peanut straw powder, 10-15 pts. wt. mung bean straw powder, 35-45 pts. wt. cotton straw powder, 19-26 pts. wt. oilseed straw powder, 3-5 pts. wt. black walnut meal, 4-8 pts. wt. lemon sawdust, 6-19 pts. wt. sycamore tree wood meal, 9-19 pts. wt. Davidia wooden meal, 9-16 pts. wt. cotton wooden meal, 3-8 pts. wt. java fern wooden meal, and 4-7 pts. wt. Bauhinia wooden meal.
NOVELTY - A composite biofuel formulation comprises 13-25 pts. wt. oil seed straw powder, 14-20 pts. wt. vine green straw powder, 15-20 pts. wt. mustard straw powder, 10-15 pts. wt. sesame straw powder, 14-16 pts. wt. sunflower straw powder, 5-9 pts. wt. biomass carbon, 1-2 pts. wt. chemical combustion improver, 3-5 pts. wt. coal, 11-17 pts. wt. rain dried twigs, 5-9 pts. wt. cortex albiziae branch, 1-3 pts. wt. patrinia scabiosaefolia flower stems, 5-9 pts. wt. isopropanol, 5-8 pts. wt. tert.-butanol, 1-6 pts. wt. methanol, and 9-16 pts. wt. ethanol.    USE - A composite biofuel formulation (claimed).    ADVANTAGE - The biofuel formulation has low carbon monoxide discharge and low production cost.
NOVELTY - Biological source fuel prescription comprises 5-10 pts. wt. broad bean straw powder, 45-55 pts. wt. wheat rice powder, 30-45 pts. wt. peanut rice powder, 10-15 pts. wt. mung bean rice powder, 35-45 pts. wt. cotton rice powder, 19-26 pts. wt. oil seed straw stick powder, 3-5 pts. wt. black walnut meal, 4-8 pts. wt. lemon wooden meal, 10-15 pts. wt. olive trees crumbs, 10-15 pts. wt. Elm wood, 1-6 pts. wt. methyl alcohol and 9-16 pts. wt. ethyl alcohol.    USE - Biological source fuel prescription.    ADVANTAGE - The biological source fuel prescription has less emissions of carbon monoxide, very low production cost, and is only obtained from a biological source, as compared with conventional fuels.
NOVELTY - Biofuel source comprises oilseed straw powder, rice straw powder, Sophora japonica branch, Beech branch, mangrove branch, dry oak branch, willow branch, anthracite coal, coal slime, animal fat, food waste, sunflower stalk powder, camphor wood, sawdust, larch wood, black wattle, masson pine sawdust and Simao pine sawdust.    USE - As biofuel source.    ADVANTAGE - The biofuel source is easily prepared, and environmentally-friendly and thus it is safe.    DETAILED DESCRIPTION - Biofuel source comprises 13-25 pts. wt. oilseed straw powder, 14-20 pts. wt. rice straw powder, 5-10 pts. wt. Sophora japonica branch, 5-10 pts. wt. Beech branch, 5-10 pts. wt. mangrove branch, 5-10 pts. wt. dry oak branch, 5-10 pts. wt. willow branch, 20-30 pts. wt. anthracite coal, 25-30 pts. wt. coal slime, 15-25 pts. wt. animal fat, 5-15 pts. wt. food waste, 9-16 pts. wt. sunflower stalk powder, 9-16 pts. wt. camphor wood, 10-15 pts. wt. sawdust, 11-13 pts. wt. larch wood, 12-16 pts. wt. black wattle, 12-18 pts. wt. masson pine sawdust and 11-15 pts. wt. Simao pine sawdust.
NOVELTY - Composite biomass fuel comprises 11-13 pts. wt. bagasse, 15-25 pts. wt. rice stick powder, 65-70 pts. wt. soybean rice powder, 50-55 pts. wt. potato rice powder, 40-50 pts. wt. highland barley rice powder, 20-35 pts. wt. broad bean rice powder, 80-90 pts. wt. wheat rice powder, 0.0001-0.0003 pts. wt. photosynthetic bacterium powder, 0.0001-0.0003 pts. wt. Rhizopus stolonifer silk fungus powder, 0.0001-0.0003 pts. wt. Bacillus licheniformis powder, 0.0001-0.0003 pts. wt. Bacillus circulans powder, 2-9 pts. wt. ammonium sulfate and 5-9 pts. wt. monoammonium phosphate.    USE - Composite biomass fuel.    ADVANTAGE - The composite biomass fuel can be economically prepared with increased combustion efficiency, low thermal efficiency and reduced energy consumption and without pollution.
NOVELTY - Biofuel comprises 10-16 pts. wt. ethanol, 30-46 pts. wt. oilseed straw powder, 19-26 pts. wt. Veronica tenuifolia straw powder, 10-15 pts. wt. hemp straw powder, 20-30 pts. wt. sunflower straw powder, 35-45 pts. wt. castor stalks, 16-25 pts. wt. rice husk powder, 30-45 pts. wt. peat, 55-60 pts. wt. soybean powder, 25-40 pts. wt. rice straw powder, 30-45 pts. wt. barley straw powder, 23-46 pts. wt. pole beans powder, and 45-50 pts. wt. wheat straw powder.    USE - As biofuel.    ADVANTAGE - The biofuel is clean, cost-effective, and highly flammable, prolongs combustion time, and reduces smoke, sulfur dioxide and carbon dioxide emission concentration and thus protects environment.
NOVELTY - An agricultural straw-based biological fuel comprises 5-10 pts. wt. birch branch, 12-16 pts. wt. chicken manure, 10-15 pts. wt. rice bran, 10-15 pts. wt. wheat bran, 5-10 pts. wt. potato, 2-3 pts. wt. sucrose, 1-3 pts. wt. agar, 25-30 pts. wt. olive tree small leaf meal, 15-20 pts. wt. cypress wood meal, 1-6 pts. wt. Bodhi tree wooden meal, 5-16 pts. wt. phoenix wood meal, 5-10 pts. wt. Ficus microcarpa, 16-29 pts. wt. peanut straw stick powder, 30-45 pts. wt. castor straw stick powder, 15-25 pts. wt. poplar branch, 11-16 pts. wt. oak-type branch, and 1-3 pts. wt. combustion improver.    USE - Agricultural straw-based biological fuel for industrial boiler.    ADVANTAGE - The fuel is green, has reduced dust pollution and combustion cost and enhanced strength, reduces friction, increases capacity and bonding character in product after cooling, and effectively uses biomass energy.
NOVELTY - A biomass fuel comprises 60-80 pts. wt. biomass material having moisture content of 20-30% and 26-34 pts. wt. bamboo having moisture content of 6%.    USE - Biomass fuel (claimed).    ADVANTAGE - The biomass fuel is manufactured by simple method in short time with reduced energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of biomass fuel, which involves crushing biomass material into 20-40-mesh granules, crushing bamboo into 40-100-mesh powder, mixing bamboo powder and biomass granules for 4-6 minutes, and placing obtained mixture into granulator, to obtain particles having diameter of 0.8 mu m.
NOVELTY - Fuel comprises 10-15 pts. wt. poplar tree meal, 10-15 pts. wt. olive tree sawdust, 10-15 pts. wt. elm wood, 16-29 pts. wt. hemp straw powder, 33-46 pts. wt. sunflower straw powder, 40-56 pts. wt. husk powder, 15-30 pts. wt. soybean straw, 12-20 pts. wt. goose dung, 10-15 pts. wt. pig manure, 9-16 pts. wt. Juniperus meal, 1-3 pts. wt. Pinus bungeana sawdust, 11-18 pts. wt. silver oak branch and 14-30 pts. wt. willow tree stem.    USE - As fuel.    ADVANTAGE - The fuel is environmentally-friendly and energy-saving, and exhibits prolonged combustion time and improved calorific value.
NOVELTY - Biofuel granule comprises 25-30 pts. wt. cotton straw powder, 35-55 pts. wt. oilseed straw powder, 15-25 pts. wt. rice straw powder, 15-20 pts. wt. mustard straw powder, 25-30 pts. wt. duck manure, 12-20 pts. wt. goose droppings, 10-15 pts. wt. pig manure, 40-65 pts. wt. coal powder, 55-60 pts. wt. mulberry branch, 15-25 pts. wt. willow branch, 25-35 pts. wt. Sophora japonica branch, 11-18 pts. wt. silver birch branch and 14-30 pts. wt. stem of willow tree.    USE - As biofuel granule.    ADVANTAGE - The biofuel granule saves energy, is environmentally-friendly, utilizes waste biomass, and prolongs combustion time as the content of carbon in the granule is increased. The calorific value of the biofuel granule is enhanced.
NOVELTY - Pellet fuel comprises 10-15 pts. wt. hemp straw powder, 20-30 pts. wt. sunflower straw powder, 35-45 pts. wt. castor straw powder, 16-25 pts. wt. rice hull powder, 30-45 pts. wt. peat, 40-65 pts. wt. coal powder, 55-60 pts. wt. mulberry branch, 15-25 pts. wt. willow, 25-35 pts. wt. Sophora japonica branch, 11-18 pts. wt. silver birch branch, and 14-30 pts. wt. Panicum stem.    USE - As pellet fuel.    ADVANTAGE - The pellet fuel is prepared by simple method using biomass waste, and hence is environmentally friendly, and saves energy.
NOVELTY - A plant oil is recovered from waste clay by extracting plant oil in waste clay until waste clay oil rate is less than or equal to 2%, separating extraction solvent and oil by fractionation, reusing extraction solvent, adding methanol and sulfuric acid in oil in which molar ratio of methanol:oil is 8-9 and weight ratio of sulfuric acid:oil is 0.01-0.02, performing esterification at 30-65 degrees C for 30-120 minutes until free fatty acid content is less than or equal to 2%, and adding methanol and basic catalyst in which molar ratio of methanol:oil is 6 and weight ratio of basic catalyst:oil is 0.01.    USE - Recovery of plant oil from waste clay (claimed).    ADVANTAGE - Recovery process has no spontaneous combustion risk, low cost, increased yield, and high conversion rate.    DETAILED DESCRIPTION - A plant oil is recovered from waste clay by extracting plant oil in waste clay until waste clay oil rate is less than or equal to 2%, separating extraction solvent and oil by fractionation, reusing extraction solvent, adding methanol and sulfuric acid in oil in which molar ratio of methanol:oil is 8-9 and weight ratio of sulfuric acid:oil is 0.01-0.02, performing esterification at 30-65 degrees C for 30-120 minutes until free fatty acid content is less than or equal to 2%, adding methanol and basic catalyst in which molar ratio of methanol:oil is 6 and weight ratio of basic catalyst:oil is 0.01, performing transesterification at 60 degrees C for 90 minutes to convert oil to methyl ester and glycerol, separating methyl ester and glycerol, standing to deposit large proportion of glycerol to bottom by gravity, isolating methyl ester with lighter weight, neutralizing, washing, separating water, and distilling at 105-120 degrees C to remove residual basic catalyst, methanol, and water in which neutralizing agent used is acetic acid and molar ratio of acetic acid:oil is 0.015-0.03 and molar ratio of water:oil is 3-9.
NOVELTY - Method for preparing microemulsion involves adding diethyl ether to water and stirring at normal temperature, adding 2-methyl-4-chlorophenoxyacetic acid to stirred mixture, reacting obtained mixture for 0.5-0.7 hours, adding methylene chloride to reacted mixture, stirring mixture, and adding fluroxypyr, reacting mixture for 0.3-0.5 hours, adding water to mixture and stirring mixture, adding fatty alcohol sulfate to stirred mixture, and stirring mixture at 210-220 revolutions/minute for 1.1-1.3 hours.    USE - The method is useful for preparing microemulsion (claimed) which is used for controlling weeds in Veronica, Euphorbia, purslane, Cardamine, and Chenopodium quinoa.    ADVANTAGE - The method enables to prepare product simply and in an environmentally-friendly manner with mild reaction conditions, and which has high dispersibility.    DETAILED DESCRIPTION - Method for preparing microemulsion involves using 11-13 wt.% fluroxypyr, 25-27 wt.% methylene chloride, 3-4 wt.% 2-methyl-4-chlorophenoxyacetic acid, 8-9 wt.% diethyl ether, 4 wt.% fatty alcohol sulfate, and water (remainder), adding diethyl ether to water and stirring at normal temperature and 30-35 revolutions/minute, adding 2-methyl-4-chlorophenoxyacetic acid to stirred mixture, reacting obtained mixture for 0.5-0.7 hours, adding methylene chloride to reacted mixture, stirring mixture at 30-35 revolutions/minute, adding fluroxypyr to stirred mixture, reacting mixture for 0.3-0.5 hours, adding water to mixture and stirring mixture at 30-35 revolutions/minute, adding fatty alcohol sulfate to stirred mixture, and stirring obtained mixture at 210-220 revolutions/minute for 1.1-1.3 hours.
NOVELTY - A maple tree cultivating method involves selecting loam soil with high alkali and calcium content, applying base fertilizer to the soil before planting, plowing the soil to remove weeds and other plant residue, transplanting the maple seedlings into the soil, irrigating the field properly to obtain robust growth of seedlings, applying additional fertilizer such as nitrogen, potassium and phosphorus fertilizer to the field, weeding the field to promote seedling growth, applying pesticides to prevent insect pests and diseases, followed by cultivating maple tree according to soil conditions.    USE - Method for cultivating maple tree.    ADVANTAGE - The method enables cultivating maple tree with high survival rate in an eco-friendly manner.    DETAILED DESCRIPTION - A maple tree cultivating method involves selecting loam soil with high alkali and calcium content, applying base fertilizer to the soil to depth of 45-55 cm before planting, plowing the soil to remove weeds and other plant residue, transplanting the maple seedlings with trunk diameter of 35-80 cm into the soil to depth of 30-50 cm, irrigating the field properly to obtain robust growth of seedlings, performing pruning process on the seedling growth to remove dead or over grown branches or stem, applying additional fertilizer such as nitrogen, potassium and phosphorus fertilizer to the field, weeding the field to promote seedling growth, spraying herbicide such as bentazone and traditional chinese medicine liquid to the leaf blade, applying pesticides such as 15% hymexazol, 20% phosphorus missible oil, 50% fernasan wettable powder, 10% imidacloprid powder and 4.5% cypermethrin to prevent insect pests and diseases, followed by cultivating maple tree according to soil conditions.
NOVELTY - In the proposed method processing is performed in a circulating flow by hydrodynamic and ultrasonic cavitation action in cyclically repeated sequence consisting of two phases. A phase of hydrodynamic action involves mechanical destruction of liquid and (or) solid parts of components to the sizes that do not exceed the value of about 1 mm, and a phase of ultrasonic action involves ultrafine destruction of liquid and (or) solid particles of components, which are produced during the first destruction phase. Frequency of acoustic ultrasonic field fT is measured depending on temperature of processed multicomponent medium according to the following expression: fT=fN/(1+alphadeltaT), where fN - resonance frequency of an ultrasonic emitter at normal temperature TN=25 degrees C, deltaT -difference between actual values of temperature and TN, alpha - thermal expansion coefficient of material from which an ultrasonic emitter is made, and two-phase cyclic processing sequence of multicomponent medium is continued till more than 5% of suspended solid and/or liquid particles with a size of more than 25 mcm is left in it. The invention also describes a plant for implementation of the specified method.    USE - Power industry.    ADVANTAGE - Method improvement.2 cl, 1 dwg, 1 tbl
NOVELTY - Use of nicotine-resistant housefly larva, is claimed for performing biological conversion of tobacco leaves to obtain bioorganic fertilizer and biological protein. The nicotine-resistant housefly larva is obtained by placing nicotine-resistant housefly eggs in culture material, and breeding obtained larva for biological conversion process, where the culture material comprises 60-85 %mass fresh tobacco leaves, 0-25 %mass wheat bran, 5 %mass chaff powder, 5 %mass sawdust and 5 %mass fish meal, and the fresh tobacco leaves are chopped to size having grain diameter of 2-3 cm.    USE - The nicotine-resistant housefly larva is useful for performing biological conversion of tobacco leaves to obtain bioorganic fertilizer and biological protein (claimed).    ADVANTAGE - The nicotine-resistant housefly larva cost-effectively produces fertilizer and protein having excellent quality, recycles tobacco leaves, prevents accumulation of tobacco leaves, and consumes minimal energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for obtaining bioorganic fertilizer and biological protein, which involves collecting fresh tobacco leaves, cutting the leaves, adding remaining materials to the leaves, stirring the mixture to obtain the culture material, placing the nicotine-resistant housefly eggs on the culture material, obtaining larvae from the eggs after 2 days, performing biological conversion, feeding the obtained housefly larvae for 4-5 days which converts the culture materials to bioorganic fertilizer, and obtaining mature pupa.
NOVELTY - A molybdenum disulfide and graphitic carbon nanostructure-graphene composite carbon paper catalyst material is prepared by soaking graphitic carbon nanostructure-graphene composite carbon paper in molybdenum and sulfur precursor solution, performing hydrothermal or solvothermal reaction, and repeatedly washing.    USE - Preparation of molybdenum disulfide and graphitic carbon nanostructure-graphene composite carbon paper catalyst material for hydrogen-producing water electrolysis (claimed).    ADVANTAGE - Catalyst material is environment-friendly and safe. Process is simple, has low raw material cost, and does not require use of glassy carbon electrode coating process.    DESCRIPTION OF DRAWING(S) - The drawing shows a scanning electron microscope photograph of molybdenum disulfide and graphitic carbon nanostructure-graphene composite carbon paper catalyst material.
NOVELTY - Organic fertilizer comprises (in pts.): fresh chicken manure (100-150), corncob (20-40), river silt (10-20), dry cow dung (20-40), montmorillonite (5-10), bean dregs (5-10), lignin (1-3), fresh straw (20-40), traditional Chinese medicinal additive (10-20), phosphate rock (5-10), bentonite (5-10), asphalt emulsion (1-3), potassium fulvate (1-3), distiller grains (5-10), bone meal (5-10), seaweed (5-10), rice husk (5-10), Rehmannia rhizome (2-5), vermiculite (5-10).    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer improve soil aggregation property, and easy to use.    DETAILED DESCRIPTION - Organic fertilizer comprises (in pts.): fresh chicken manure (100-150), corncob (20-40), river silt (10-20), dry cow dung (20-40), montmorillonite (5-10), bean dregs (5-10), lignin (1-3), fresh straw stick (20-40), traditional Chinese medicinal additive (10-20), phosphonium powder (5-10), bentonite (5-10), asphalt emulsion (1-3), potassium fulvate (1-3), distiller grains (5-10), bone meal (5-10), seaweed (5-10), rice husk (5-10), Rehmannia rhizome (2-5), vermiculite (5-10). The traditionalChinese medicinal additive comprises sulfur, Apocynum venetum, Polygonum aviculare, cluster mallow fruit, fortune Eupatorium herb, Clerodendrum trichotomum, Glauber's s salt, rhizoma smilacis glabrae, bark of tree of heaven, herba equiseti hiemalis, gordon euryale seed in mass ratio of 1:1:3:2:2:4:5:5:4:3:3 respectively.    An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves    (A) extracting thrice all herbal components in water and then leaching to obtain the additive;    (B) mixing the additive with remaining components and then naturally fermenting in a covered jar for 10-15 days to obtain a product; and    (C) granulating the product and then drying to obtain final product.
NOVELTY - Preparation of cationic protein material comprises adjusting pH of 2-14 wt.% collagen peptide aqueous solution to 7-13, and heating to 30-65?oC; mixing epoxy quaternary ammonium salt and collagen polypeptide at volume ratio 1-2:1, dropping into collagen peptide aqueous solution, stirring while maintaining temperature to 30-65?oC for 1-8 hours, stopping reaction, and adjusting pH to neutral; and vacuum-distilling to remove 60-90% moisture, and freeze-drying to - 60?oC to - 40?oC for 1-2 days.    USE - Method for preparation of cationic protein material (claimed).    ADVANTAGE - The material is nontoxic and environment-friendly, and it has large positive charge and excellent antibacterial character.
NOVELTY - A carbon powder preparation method comprises taking raw material at 8-12% water content, drying, cutting to grain size of 0.5-5 cm, putting into carbonization furnace, heating for 10-30 minutes at 200-250 degrees C, 250-300 degrees C and 300-400 degrees C, respectively, and crushing into fineness of 100-150 mesh.    USE - Carbon powder preparation method (claimed).    ADVANTAGE - The method has high product yield and quality.
NOVELTY - Passivating agent comprises 5-15 wt.% rotten chicken manure, 5-15 wt.% rice bran, 5-15 wt.% peat, 10-20 wt.% silicon-calcium-magnesium fertilizer, 5-15 wt.% talc, 25-35 wt.% sepiolite, 10-20 wt.% sugarcane filter mud and 1.5-2.5 wt.% microbial fermented liquid comprising Paenibacillus polymyxa (CCTCC NO: M2014319).    USE - The passivating agent is useful for reducing cadmium and lead content in soil (claimed).    ADVANTAGE - The passivating agent reduces cadmium and lead content in paddy soil to 51.5-51.6% and 52.6-58.8%, respectively, and cadmium and lead content in polished rice to 48.8-51.6% and 52.7-56%, increases soil pH to 0.97-1.04, and improves soil fertility and physical and chemical properties of the soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned passivating agent, which involves (a) crushing the rotten chicken manure and rice bran, (b) adding organic material decomposition agent to the crushed rotten chicken manure and rice bran, composting the mixture and aging the compost, (c) crushing the peat, silicon-calcium-magnesium fertilizer, talc, sepiolite and sugarcane filter mud, adding the crushed peat, silicon-calcium-magnesium fertilizer, talc, sepiolite and sugarcane filter mud to the aged compost, crushing and drying the mixture and fermenting the crushed mixture, (d) sterilizing the peat and mixing the sterilized peat and the microbial fermented liquid, and (e) uniformly mixing the products obtained in steps (a)-(d).
NOVELTY - Fluorine-free refrigerant comprises 30-60 pts. wt. propane, 40-60 pts. wt. propylene, 20-30 pts. wt. isobutane, 10-15 pts. wt. 1,1,1,2-tetrafluoroethane, 10-18 pts. wt. 1,1,2,2-tetrafluoroethane, 2-8 pts. wt. trifluoroiodomethane, 3-12 pts. wt. pentafluoroethyl iodide, 5-15 pts. wt. tetramethyl-cyclobutane, 20-30 pts. wt. liquid carbon dioxide, and 4-7 pts. frozen lubricant; where the pour point of frozen lubricant is -30 to -35 degrees C.    USE - Used as a fluorine-free refrigerant.    ADVANTAGE - The refrigerant has zero ODP value, does not damage ozone layer upon long-term use, has low global warming potential (GWP) value, considerable working pressure and R22, ensures that the cooling effect is not reduced, and has fuel suppression and explosion suppression effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the fluorine-free refrigerant, comprising evenly mixing the mentioned components at 20-25 degrees C.
NOVELTY - A straw liquefied oil producing method involves processing straw, preparing bed material. The processed straw and bed materials are added into thermal cracking reaction tank under vacuum at 45-50 degrees C for 0.3-0.5 seconds, followed by condensing splitting gas into liquid bio-oil in a condenser, and adding animal additive during straw processing step, where the animal additive comprises carbonized wheat straw powder, rubber powder and animal bone charring powder, and the bed material comprises clay powder and catalyst.    USE - Method for producing straw liquefied oil.    ADVANTAGE - The method enables producing straw liquefied oil with increased conversion rate and heat value, in a cost-effective manner.    DETAILED DESCRIPTION - A straw liquefied oil producing method involves processing straw, preparing bed material. The processed straw and bed materials are added into thermal cracking reaction tank under vacuum at 450-500 degrees C for 0.3-0.5 seconds, followed by condensing splitting gas into liquid bio-oil in a condenser, and adding animal additive during straw processing step, where the animal additive comprises carbonized wheat straw powder, rubber powder and animal bone charring powder, the bed material comprises clay powder and catalyst, the catalyst is molybdenum, nickel, cerium oxide powder, iron powder or tourmaline powder, and the mass ratio of the straw and bed material in thermal cracking tank is 7:3. An INDEPENDENT CLAIM is included for a device comprising a thermal cracking reaction tank connected to a storage tank for preparing storage bed material, a mixer for mixing straw and additive, a vacuum cooling tower for cooling gaseous product, a stirrer and a vacuum drying chamber between the stirrer and the cracking tank.
NOVELTY - This new type utility claims one of a bucket type oil acid pneuma flat air treatment system, in that is applied to wood or a wood dry distillation carbonization process, separating one device extracting a distillation tank discharging of the wood tar and wood acetic acid and wood coal mix in a gas. This system comprising tar bucket and acetic acid bucket, wherein, a bucket set with tar water circulation cooling device, acetic acid bucket by 80 caliber steel tube inner one a set 70 of small calibre steel pipe compose the upper lower two end forming a ring, big steel pipe inner wall and small steel tube outside wall compose one cylindrical cavity structure, the small steel pipe upper part set with inner fan, wind direction is upward mounted, through design of the present embodiment, having a good cooling separating extraction effect, structure is simple and practical, and is suitable for wide popularization.
NOVELTY - This utility new type relates to one a gasification organic waste treatment system, comprising solar energy generator, solar energy generator through a pipeline and air pump and organic waste collection tank, an air pump of the solar energy generator inner produce a gas pipeline through a dust remover, a gas input gas collecting tank rear by dust, a gas inner gas collecting tank and filter rear to combustible gas collecting tank by filter. This utility new type design is reasonable, use is convenient, through this a treatment system, fully use the solar energy, the solar energy generator to decompose the gasification household organic garbage, which not only fully valid use of domestic garbage, but also can use the household garbage produce a combustion gas, which can be used for generation or as energy, avoids the waste of resource, increase the valid use rate of resource, at the same time protect the ecological environment.
NOVELTY - Synergistic agent comprises 10-16 pts. wt. microelement, 20-30 pts. wt. lignic acid, 5-15 pts. wt. zeolite powder, 10 pts. wt. bentonite, 3-8 pts. wt. complex amino acid, 0.1-2 pts. wt. urease inhibitor, 4-10 pts. wt. traditional Chinese medicine component, 0.5-1.5 pts. wt. biological agent, 1-3 pts. wt. insecticide and 0.3-0.8 pts. wt. biological growth promoter.    USE - The synergistic agent is useful as fertilizer for walnut trees (claimed).    ADVANTAGE - The synergistic agent inhibits growth of harmful bacteria, is suitable for soil improvement, and easily supplements missing nutrients.
NOVELTY - Invention relates to field of application of renewable sources of raw material - biomass. Claimed is method of catalytic gasification of biomass with obtaining gaseous fuels. Method includes milling biomass and its thermal processing in air medium at 600 divide by 800 degrees C and pressure 1.2-2.0 atm, catalytic thermal degradation of gaseous products in presence of transition metals, method differs by the fact that catalytic thermal degradation is realised at temperature 500 divide by 550 degrees C, weight ratio of catalyst and biomass is 0.01 divide by 0.05 and air consumption 1.0 divide by 2.5 m3 per 1 kg of biomass, and as catalyst is applied mixture of oxides of chrome and vanadium, applied on natural aluminosilicate in quantity 1 divide by 20 wt % and 1 divide by 5 wt % respectively, or as catalyst applied is mixture of oxides of molybdenum and manganese, applied on natural aluminosilicate in quantity 1 divide by 10 wt % and 10 divide by 30 wt % respectively, or as catalyst applied is mixture of cobalt and nickel oxides, applied on natural aluminosilicate in quantity 5 divide by 25 wt % and 1 divide by 40 wt % respectively.    USE - Chemistry.    ADVANTAGE - Increased output of flammable hydrocarbons, achievement of good efficiency of gasification.6 tbl, 6 ex
NOVELTY - Organic fertilizer comprises 800-1200 pts. wt. chicken manure, 20-40 pts. wt. black carbon, 80-120 pts. wt. melamine and 70-80 pts. wt. potassium fertilizer.    USE - The fertilizer is useful for various crops including greenhouse vegetable, fruit trees, economic crops, grain crops, medicinal materials, flowers, lawn and nursery stock.    ADVANTAGE - The fertilizer is rich in nutritional components, has input-output ratio of 1:10-30, can be applied to all types of soil and produces high benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer, comprising (i) taking chicken manure in a pre-fermenting device, mixing uniform, inoculating, pre-fermenting for 6-12 days, adding biological strain using horizontal type anaerobic fermentation device, and performing primary fermentation at 50-60 degrees C for 7-15 days to obtain compost and marsh gas, collecting marsh gas and recycling, (ii) mixing black carbon, melamine and potassium fertilizer, crushing into 2-3 cm particles, adding compost and mixing uniformly in a mixer, and (iii) granulating, drying, cooling and sieving.
NOVELTY - The apparatus (1) has a gas detection part (23) for detecting change of electrical resistance of a gas sense layer. A temperature detection part (214) detects and outputs a detection signal according to temperature of circumference of gas sensors (10, 30). A humidity detection part (215) detects humidity of circumference of the gas sense layer based on output from the humidity detection part. A correction part (216) computes a correction value based on temperature. A determination part (217) determines presence or absence of gas by amended sensor output.    USE - Low-power-consumption type apparatus for detecting gas such as carbon monoxide, methane, dimethylmethane and ethanol, in a gas-leakage alarm unit.    ADVANTAGE - The apparatus achieves high accurate detection of the gas when influence by temperature or humidity can be excluded.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gas detection method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a gas detection apparatus.'(Drawing includes non-English language text)'    Gas detection apparatus (1)    Gas sensors (10, 30)    Gas detection part (23)    Temperature detection part (214)    Humidity detection part (215)    Correction part (216)    Determination part (217)
NOVELTY - This utility new type relates to a sewage treatment energy-saving one pig farm, comprising a piggery sewage treatment system using the pigsty comprising a pigsty, a wall body, pigsty transverse a direction into a plurality of pig, a pig per column close to the inner wall of the ground is provided with a drain wherein the drain wherein the through pipeline and sewage collecting pool connected between a drain and wherein pipeline set with barriers, inner the swinery set with electric heating pipe, a sewage treatment system comprising using stack fertilizer pool, solid-liquid separating machine, UASB pool, an aeration pool, fluidization bed biological film reactor, filtering pool, a steam-water separator, a pneuma cabinet and a marsh gas generator. This utility new type of pig farm is equipped with sewage treatment using system can conveniently realize a dirt of inner pig farm, is energy-saving, environment-friendly, green, clean and so on.
NOVELTY - A one output pure hydrogen is a hydrogen and machine, comprises one power supply unit, and one power source unit electrical connection of this electrolysis unit, one electric connection b this power supply unit and adjusting unit of this electrolysis unit, and one and this electrolysis unit connected a filter unit. This electrolysis unit including electrolytic groove is one containing electrolyte, and a phase interval is set with multi-b of a plate in this electrolytic groove, the electrode plate can be electrolyte containing b of electrolyte in this electrolytic groove to generate hydrogen and oxygen. This adjusting unit can control this power source unit a power force to this electrolysis unit of positive electrode and a difference is nagetive, adjust the produce of hydrogen and oxygen ratio, and this oxygen is a ratio adjustment is close to zero, to a pure hydrogen. The output of pure hydrogen by this filter unit filter removing moisture, that is, can one respiratory mask human body directly.
NOVELTY - This utility model claims a system for extracting taxol by elution solvent, and comprises elution solvent tank (5), vacuum concentrator (1), first-stage condenser (2), second level condenser (3), a solvent recovery tank A (4), a vacuum pipeline (6), a vacuum condenser (7) and solvent recovery tank B (8). This utility model can be a taxol crude product chromatography separating process in the product of elution solvent recovery process, a rate of elution solvent is a 99%, it not only can reduce the chromatography separating purification of taxol production cost, but also can reduce the elution solvent for a cause of pollute.
NOVELTY - This utility new type relates to one a hydrogen producing device, this device comprises hydrogen oxygen output part, the proton exchange film is divided into hydrogen containing area and oxygen containing area, main pure water inner box body in insulation box body, the height of the bottom is greater than equal to hydrogen oxygen output part of the top part of the height, oxygen containing area connected pure water tank main body, Y-shaped separating tube, a gas-liquid entrance and a second hydrogen outlet is upward, the pure water outlet is downward, the distribution of Y-shaped separating tube of the height greater than equal to main pure water box is full water level of the height, a gas-liquid entrance connected hydrogen, pure water outlet connected pure water tank main body, a power part, a proton exchange film, a power switch and a power supply part. Therefore, this utility new type of hydrogen generating device does not need to fluid driving device, simple structure is convenient to maintain and time operation noise and high safety and produce a pure hydrogen.
NOVELTY - This utility model claims a horizontal flow fermentation device in a collective air supply biogas engineering, the characteristic is, including fermentation jar group, and pump power pump for future use, fermenting jar group by a plurality of fermentation jar one between the fermenting jar through a feeding pipe, a material discharging pipe and stir pipe connected together. This utility new type following advantages: 1. Fermentation and stable continuous supply, two electric pump, a electric pump operation, and the other one table as for future use, each a key are equipped with manual valve and electric valve, a the device maintain a service time for the pneuma is, each fermentation jar at the same time a operation, or a independent operation, 2. How many and arranged a fermentation jar a according to engineering scale size and a 3. Fermentation jar mounted in inner room, and transverse a cement mound, each fermentation jar are use of insulating foam, temperature drop, 4. Fermentation jar inside has jet stirrer, inner jar material liquid stir uniform, without dead angle, 5. Biogas residue discharging zero pollute.
NOVELTY - This utility new type relates to a kitchen garbage and excrement waste water integrated processing device, it comprises the forage, two phase Anaerobic processor, a water outlet sedimentation jar and boiler, mixing inner tank is equipped with a small stirrer, two Anaerobic phase through an overflow plate and a transition plate for the Anaerobic processor in turn dividing into two acid-producing area, a transition area and a producing area, a transition area and producing a acid-producing area, and acid-producing area and for producing a area, big inner stirrer in a producing area, acid-producing area stirrer in acid production area, transition zone stirrer is provided with a transition area, a acid-producing area and producing a area of two phase Anaerobic a side of a wall is provided with acid-producing a sampling area wherein a producing a sampling area wherein, forage through feeding pipe and acid-producing area of two Anaerobic processor is connected, the water outlet sedimentation jar through the water overflow pipe and two Anaerobic a phase of producing a area connected, at the top end of two phase Anaerobic a producing area is provided with a marsh gas collection pipe, marsh gas storage bag and a boiler wherein connected air inlet.
NOVELTY - The system has an absorptive tower for absorbing acidic gas by utilizing absorbent. The absorptive tower is equipped with a side of a regenerator that separates process gas from the absorbent. A separation supply line is separated from a water separator. A condensed water supply line is connected to a side of a condenser. A process gas line passes through a heat-exchanger. An absorbent supply line is connected with another side of the regenerator. The separation supply line is fixed to another heat-exchanger that heat-exchanges dilute solution.    USE - Energy-saving-type system for collecting acidic gas e.g. carbon dioxide, methane, hydrogen sulfide, carbonylsulfide and mercapto, in a dust scrubber of a reboiler (all claimed).    ADVANTAGE - The separation supply line is separated from the water separator, and the condensed water supply line is connected to the side of the condenser so as to easily condense water by heat-exchanging the water with the dilute solution through the heat-exchanger, so that smooth preheating process about process gas with high-temperature can be facilitated, thus performing an absorbent salvage process by utilizing water with low-temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an energy-saving-type acidic gas collecting method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an energy-saving-type system for collecting acidic gas in a dust scrubber of a reboiler.
NOVELTY - The method involves filling raw material in a bag. The raw material is mixed and stirred with water, where the raw material contains 646-787 pts. wt. fresh soybean straw, 10-200 pts. wt. corn powder, 10-200 pts. wt. molasses, 50 pts. wt. calcium formate and 30-70 pts. wt. composite material based on fermentation condition, grain diameter of the fresh soybean straw is 4-10 mm and the raw material contains 25-45 wt. % of the water and fermentation temperature and fermentation time of the fermentation condition are 25-35 degrees Celsius and 15 to 35 min.    USE - Composite probiotic fermented fresh soybean straw feed preparing method.    ADVANTAGE - The method enables effectively obtaining composite probiotic fermented fresh soybean straw feed without need more materials, ensuring fermenting process, trypsin restrain factor content and lactic acid content effect and high recovery rate, reducing urease activity rate and production cost, improving feed quality and strong fragrance effect, which greatly increases feeding efficiency of ruminant animal.
NOVELTY - Producing a hydrogel composition, comprises: (a) providing titanium dioxide nanorods and loading carbon quantum dots onto the titanium dioxide nanorods to form a first mixture; (b) providing a second mixture of dispersed graphene oxide; (c) mixing the first and second mixture by ultrasonic dispersion to form a third mixture; and (d) adding a reducing agent to the third mixture to form the hydrogel composition that defines a three-dimensional porous and continuous crosslinked structure.    USE - The method is useful for producing a hydrogel composition which is useful for photocatalytic hydrogen production and storage, and in an electrode, capacitor, fuel cell, solar cell, sensor, battery (all claimed).    ADVANTAGE - The method utilizes carbon dots that are derived from alternate green carbon source (e.g. vitamin C) instead of graphitic precursor such green carbon source, which serves an inexpensive precursor and could easily be realized by a one-pot hydrothermal synthesis.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a hydrogel composition comprising: a graphene; a titanium dioxide nanotube array; and a carbon quantum dot, where the hydrogel composition defines a three-dimensional porous and continuous crosslinked structure.
NOVELTY - The system (1) has a sedimentation tank (14) for precipitating activated sludge contained in natural water. A sludge return path (15) returns the activated sludge deposited in the sedimentation tank to an anaerobic tank (12). A density detection part detects density of nitrous oxide gas emitted within the aerobic tank. A gas sending control apparatus controls supply-amount-rate of the nitrous oxide gas in the aerobic tank based on generation amount of the gas detected by the density detection part such that generation amount of the gas in the aerobic tank is lesser than predetermined value.    USE - Sewage-treatment system for nitrifying ammonia nitrogen contained in sewages e.g. domestic waste water, industrial waste-water and closed bodies of water such as lakes and marshes, to nitrite nitrogen or nitrate nitrogen, in a sewage-treatment installation.    ADVANTAGE - The system suppresses discharge of the nitrous oxide gas to an inner side of air at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a sewage-treatment system.'(Drawing includes non-English language text)'    Sewage-treatment system (1)    Anaerobic tank (12)    Sedimentation tank (14)    Sludge return path (15)    Digestive-fluid circuit (16)
NOVELTY - Producing iron chopsticks containing saponin extract comprises taking medicinal herbs and then grinding, passing powder over sieve, adding petroleum ether to sieved product, degreasing mixture using microwave device, filtering degreased product, ultrasonicating filtrate, adding ethanol solution to ultrasonicated product and then extracting, filtering and then collecting filtrate, concentrating filtrate, adsorbing filtrate using macroporous resin and then distilling, adding ethanol to distilled product and eluting, concentrating eluent, and vacuum drying.    USE - The method is useful for producing iron chopsticks containing saponin extract, which is useful in a medicine for treating leukemia (all claimed).    ADVANTAGE - The method is capable of easily producing the iron chopsticks containing saponin extract with improved yield in an economical and eco-friendly manner.    DETAILED DESCRIPTION - Producing iron chopsticks containing saponin extract comprises taking medicinal herbs and then grinding, passing the powder over a sieve of 40 meshes, adding 1-3 times of petroleum ether to the sieved product, degreasing the mixture using a microwave device having a power of 600 Watts for 6-8 minutes, filtering the degreased product, ultrasonicating the filtrate at a frequency of 40 KHz using a ultrasound device, adding 60-70% of ethanol solution to the ultrasonicated product and then extracting at 70-80 degrees C for 2-3 hours, filtering and then collecting the filtrate, concentrating the filtrate, adsorbing the filtrate using macroporous resin and then distilling to remove impurities, adding 60-70% of ethanol to the distilled product and then eluting, concentrating the eluent under reduced pressure, and vacuum drying to obtain iron chopsticks containing saponin extract.
NOVELTY - Synthesizing anticancer drug vorinostat, comprises (i) reacting suberic acid and aniline in presence of perfluorinated sulfonic acid resin, to obtain suberanilic acid; (ii) reacting suberanilic acid with hydroxylamine as a condensing agent in the presence of 1,3-dicyclohexylcarbodiimide; and (iii) separating the product.    USE - The method is useful for synthesizing anticancer drug vorinostat (claimed).    ADVANTAGE - The method produces high purity product, and less amount of impurities; has good production yield; and is environmental friendly.
NOVELTY - The crushing device has a loosening device (1) that is provided for pre-crushing compacted biomass which is fed via a transport device (8) from a biomass storage container. The crushed biomass is supplied to a fermenter for processing the biomass to a biogas. The loosening device is arranged with an angle-shaped separating plate having an edge connected to an angle edge of shaft in parallel and driven rotatably.    USE - Biomass crushing device for production of biogas in agricultural biogas plant.    ADVANTAGE - Since the crushed biomass is supplied to a fermenter for processing the biomass to a biogas, the damage to the tools of the crushing device is prevented and biomass processing efficiency is improved. Hence, stability of the crushing device is enhanced and wear resistance of the components of the crushing device is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the crushing device.    Loosening device (1)    Transport device (8)    Pulping container (9)
NOVELTY - The apparatus (10) has a main portion that is provided with a container and a heat medium. The heat medium is arranged in the periphery of the container, for heating the liquid to evaporate within the housing (11). The upper end of the container is provided with a discharge opening for escape of the steam generated from the liquid. The discharge opening is provided in fluid communication with the container. A steam outlet (13) is arranged on the top side (12) of the housing.    USE - Apparatus for vaporizing liquid such as process water, biomass, fermentation residue, slurry, separated liquid, exhaust gas from biogas plant and combine heat and power plant (all claimed), used in agricultural field.    ADVANTAGE - The interior of the device is serviced or cleaned in simple and effective way. The complex design of the apparatus is reduced. The operating, maintenance and cleaning facilities are improved. The full flow around the container with the heat medium can be achieved. The risk of clogging of the container is reduced. The unwanted heat losses to the environment can be reduced. The mixing of the heat medium in the interior space with the vapor from the containers is prevented. The amount of liquid supplied is controlled so that the overflow of the container is prevented. The unwanted escape of liquid can be avoided from the steam outlet of the housing.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for vaporizing liquid.    Apparatus for vaporizing liquid (10)    Housing (11)    Top side of housing (12)    Steam outlet (13)    Fluid inlet port (30)
NOVELTY - This new utility model claims of a kind of one animal died transformation for processing device of high efficient fertilizer, comprising a cylindrical bucket body, bucket body of the cylindrical bucket body is equipped with feedstock port and hot air circulation port, the left side set with motor and speed reducer, provided with semi-mould axis ball and moving the discharging mouth, the internal set with ball bearing, the ball bearing on the axes via screw connected with the crushed teeth, wherein two end respectively connected with speed reducer and ball axis, the motor through belt and the speed reducer connected with, the cylindrical bucket body periphery for fixing rectangle frame set with the bucket body, the rectangular frame provided with frame leg. This new utility model structure is simple, using suitable, by the device for animal died by crushing, then carrying out high pressure sterilization and heating for drying animal died of crushing, hair and bone series material drying after carrying out carbonizing treatment, nature cooling after lipid series material, biological diesel oil as raw material, the material after the rest powder granular grain fermented into high efficient organic agricultural fertile, it not only saves of energy at the same time can be too spread and pollute and reducing disease, state accord with environmental protection and energy saving, with good practicability, and convenient to popularize.
NOVELTY - Catching carbon. This utility new type relates to a coke furnace coal synthesis one of natural gas, comprising a blind plate, a flue gas collector, an absorption tower and a regeneration tower, plate set in the coking enterprise chimney smoke, gas collector gas entrance through pipeline connected chimney, flue gas collector is set with fixed in inner cavity of the rotating shaft is provided with a small blade, a gas absorption tower entrance a flue gas collector gas outlet; entrance regeneration absorbing solution outlet and a flue gas collector absorber reflux wherein, one branch absorbing agent outlet of a flue gas catcher cavity of rotating shaft, and the other one branch a absorption tower. Use this device family for coking enterprise chimney is carbon dioxide process, using a carbon dioxide and a coke furnace coal raw material after purification supplementing carbon.
NOVELTY - This utility new type claims a one using Anaerobic fermentation process of sewage generation system, compose by generation system and a primary settling tank, a generation system a primary settling tank, a generation system including Anaerobic fermentation jar, gas pre-processing system and combustion pneuma generation unit, said Anaerobic fermentation jar a primary settling tank and a gas pre-processing system, a gas pre-processing system a combustion pneuma generation set, further comprising the Anaerobic fermentation jar is connecting a sludge treatment system, a sludge processing system including sludge concentrate pool, a sludge pump and plate frame filter press, a sludge outlet end of the fermentation jar connect entrance of Anaerobic sludge concentrate pool, outlet of the sludge concentrate pool sludge pump through a plate frame filter press, the utility model is new type containing organic substance of waste water process Anaerobic fermentation to the utmost extent is produce with a gas, used for marsh gas generation, use clean energy is maximum, saves resource, avoids resource waste.
NOVELTY - A mobile compost one aeration device, comprising a circular air inlet pipe, circular baffle plate, cylindrical aeration pipe and conical pipe head, a round baffle and the round air inlet pipe tail end welded one end a cylindrical aeration pipe and a circular baffle is welded and the other end aeration pipe is cylindrical and conical tube head welded one end a cylindrical aeration pipe and conical pipe head is connected is set with a plurality of aeration hole. This utility new type of device high aeration efficiency, an aeration than a buried pipeline efficiency more than 26%, this utility new type aeration device is air travelling path after a first horizontal direction, an air walking path is longer, stack aeration volume. This utility new type is a movable aeration tube, mounting dismounting is simple, which saves energy consumption and time use flexible and convenient, and the compost field without need to cement, compost factory and moved , effective to protect the land resource.
NOVELTY - Preparing an alkylfuran compound (I), comprises forming a reaction mixture comprising a catalyst, a hydrogen source, and a furan compound (II) under sufficient conditions.    USE - The method is useful for preparing (I) (claimed), which is useful as a biofuel or a chemical feedstock.    ADVANTAGE - The method allows straightforward conversion of biomass-derived starting materials, into simple derivatives which can be hydrogenated quickly and under very mild conditions, thus economically producing 2,5-dimethyl furfural that avoids the handling of less tractable, commonly-used intermediates such as 5-(hydromethyl)furfural.    DETAILED DESCRIPTION - Preparing an alkylfuran compound of formula (I), comprises forming a reaction mixture comprising a catalyst, a hydrogen source, and a furan compound of formula (II) under sufficient conditions.    R1, R2 = 1-18C-alkyl;    R1a = H or 1-17C-alkyl;    R2a = 1-18C-haloalkyl, preferably chloromethyl; either    R3 = OR3a; and    R4 = OR4a; or    R3R4 = oxo (=O); either    R3a = H, 1-6C-alkyl or 1-6C-acyl; and    R4a = 1-6C-alkyl or 1-6C-acyl; or    R3aR4a = 2-4C-alkylene.
NOVELTY - Preparation of bromfenac sodium dimer impurity comprises hydrolyzing 7-(4-bromo-benzoyl)-1,3-dihydro-indol-2-one in alkali metal hydroxide solution, adding acetic acid and extracting with methylene chloride; adding alkali metal hydroxide solution, heating, refluxing, cooling, adding acetic acid, crystallizing, filtering, washing filter cake, filtering, collecting filtrate, vacuum concentrating, and adding acetone or acetonitrile; and adding ethyl acetate, refluxing, adding hydrohalic acid, cooling, filtering, adjusting pH, adding organic alcohol, and filtering.    USE - Method for preparing bromfenac sodium dimer impurity (claimed).    ADVANTAGE - The method is simple and efficient and has high yield and good environment benefit. The compound has purity of more than 99%.    DETAILED DESCRIPTION - Preparation of bromfenac sodium dimer impurity comprises hydrolyzing 7-(4-bromo-benzoyl)-1,3-dihydro-indol-2-one in alkali metal hydroxide solution, adding acetic acid and extracting with methylene chloride; adding 40-80 wt.% alkali metal hydroxide solution, heating at 70-80 degrees C for 1-3 hours, refluxing for 2-4 hours, cooling, adding acetic acid to adjust pH to 5-8, crystallizing, filtering, washing filter cake with water and ethyl acetate, filtering, collecting filtrate, vacuum concentrating, and adding acetone or acetonitrile to crystallize dimer impurities; and adding ethyl acetate, heat refluxing, adding hydrohalic acid to adjust pH to 1-2, cooling, filtering, adding alkali metal hydroxide solution to adjust pH to 8-10, adding organic alcohol to crystallize, and filtering.
NOVELTY - The ram has a first actuator (40) mounted on a frame (12) in operative communication with a stoking ram (20). A churning device (30) is positionable relative to the stoking ram between retracted and extended positions. A second actuator (50) is in operative communication with the churning device in an arrangement to position the churning device between the positions. A third actuator is in operative communication with the stoking ram in an arrangement to rotate the stoking ram and the churning device. The churning device and the second actuator are housed in an internal void.    USE - Churning and stoking ram for a furnace (claimed) i.e. static or fixed hearth, to mechanically agitate content i.e. municipal solid waste.    ADVANTAGE - The rams are configured in parallel alignment with one another such that churning devices can simultaneously rotate in opposing directions to assist in improved mechanical agitation of the contents of the furnace. The rams allows positioning of the stoking ram between internal and external positions relative to the furnace, and positioning of the churning device between the extended and retracted positions to be entirely independent, thus leading to possibility of different configurations to effect efficient churning of contents of the furnace.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a system for facilitating low temperature gasification of waste solids    (2) a method for pyroiyising solid municipal waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a churning and stoking ram with a stoking ram and churning device in an external position and a retracted position, respectively.    Frame (12)    Stoking ram (20)    Fixed end of stoking ram (24)    Churning device (30)    Actuators (40, 50)
NOVELTY - Preparation of juvenile hormone analog comprises adding (2E,4E)-11-H-3,7,11-trimethyl-2,4-docosadienoic acid or (2E,4E)-11-methoxy-3,7,11-trimethyl-2,4-docosadienoic acid, organic alkali catalyst and organic solvent into reaction container, stirring, adding dropwise pyrocarbonate solution, reacting at 0-30 degrees C for 0-3 hours, adding water to stop reaction, separating organic phase, vacuum-concentrating and distilling. The pyrocarbonate is diethyl pyrocarbonate or diisopropyl pyrocarbonate.    USE - Method for preparing juvenile hormone analog, particularly S-methoprene or S-hydroprene (claimed).    ADVANTAGE - The green, safe and environment-friendly method has mild reaction condition, high product purity and high yield. It is good for industrial production.
NOVELTY - Preparing a 7-hydroxy-3,6,7,7a-tetrahydro-1H-imidazo(1,5-c)thiazol-5-one compound (I), comprises (a) reacting a (7aR)-3,7a-dihydro-1H-imidazo(1,5-c)thiazole-5,7-dione compound (II) with zinc powder and alcohol compound under acidic conditions.    USE - The method is useful for preparing (I) (claimed).    ADVANTAGE - The method economically prepares (I) with good reaction selectivity, good quality and high yield of greater than 90% under mild reaction in an eco-friendly manner.    DETAILED DESCRIPTION - Preparing a 7-hydroxy-3,6,7,7a-tetrahydro-1H-imidazo(1,5-c)thiazol-5-one compound of formula (I), comprises (a) reacting a (7aR)-3,7a-dihydro-1H-imidazo(1,5-c)thiazole-5,7-dione compound of formula (II) with zinc powder and an alcohol compound of formula (R3OH) under acidic conditions.    R1 = phenyl (optionally substituted with 1-5C-alkyl, 1-5C-alkoxy, F, Cl or Br);    R2 = benzyl, benzhydryl (both optionally substituted with 1-5C-alkyl, 1-5C-alkoxy, OH, methylenedioxy or phenyl), tert-butyl or tert-amyl; and    R3 = 1-7 C-hydrocarbyl.
NOVELTY - Method for providing improved anaerobic digestion, involves mixing volume of waste material with water to form a feedstock mixture, where the volume of waste material includes initial amount of biomass, the feedstock mixture includes methanogenic bacteria either naturally present in waste material or introduced artificially and introducing one or more promoter substances to feedstock mixture, where one or more promoter substances are capable of modifying methanogenic bacteria and modifying includes stimulating novel enzyme production in methanogenic bacteria.    USE - The method is useful for providing improved anaerobic digestion (claimed) for modifying methanogenic bacteria.    ADVANTAGE - The method reduces hydraulic retention time from 60 days to 5 days. The system is more resilient to environmental changes, such as temperature and pH changes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for improved anaerobic digestion.
NOVELTY - Composite ionic liquid comprises: ammonium cations; and composite coordinate anions derived from at least two metal salts. At least one metal salt is an aluminum salt and any further metal salt is a salt of a metal comprising group-IB elements, group-IIB elements and transition elements. The ammonium cation is a N,N'-di substituted imidazolium cation, optionally further substituted at the 2-, 4- and/or 5- positions. The substituents comprise 1-10C alkyl and 6-10C aryl.    USE - The composite ionic liquid is useful for preparing an alkylate (claimed).    ADVANTAGE - The composite ionic liquid: shows improved stability, thus showing longer lifetime; in ionic liquid alkylation process, produces less solids and an alkylate product comprising less organic chlorides as side products; reduces organic chlorides in the alkylate product; and shows selectivity towards the production of trimethylpentanes.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a process (P1) for preparing an alkylate, comprising contacting in a reaction zone a hydrocarbon mixture comprising at least an isoparaffin and an olefin with a composite ionic liquid; and    (2) a process (P2) for preparing the composite ionic liquid, comprising mixing the metal salts with the ammonium cations, in the form of an ammonium salt, and keeping the mixture at 120-170 degrees C while stirring until all solids have completely converted into the liquid phase.
NOVELTY - The system (100) has a mobile gasification system (120) that is configured to gasify feedstock generated from a residual biomass (110) to provide syngas. The mobile gasification system is configured to generate electrical power using the syngas, and mobile gasification system is further configured to be installed in a transportable structure. The transportable structure is a shipping container. The mobile gasification system is configured to provide power to an irrigation system (170). The residual biomass is wheat straw.    USE - System e.g. agricultural system for gasifying residual biomass.    ADVANTAGE - The mobile gasification system saves the farmer both power and tillage costs with minimal requirements for maintenance, while providing the advantages of baling and stacking the residue from their field in proximity to the power generation system. The need to manage crop waste is effectively eliminated or reduced using mobile gasification system to convert the residual biomass into a valuable commodity addresses residue and tillage problems. The temperature of the syngas during the heat exchange is reduced to reduce stress on downstream components, such as cyclone and/or heat exchanger, thus the overall efficiency of the system is improved. Column agitation, waste removal, and maintaining open gas flow allow a gasifier to run for longer periods of time between maintenance and allow it to produce higher quality syngas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for gasifying residual biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the agricultural system.    Agricultural system (100)    Residual biomass (110)    Mobile gasification system (120)    Grid power (150)    Irrigation system (170)
NOVELTY - Pelletized fuel product comprises pelletized fuel and a metal compound effective to react with hydrochloric acid formed during burning of the fuel product.    USE - The pelletized fuel product is useful for combustion in stoker, circulating fluidized bed, rotary kiln and pre-heaters to make steam, electricity, or heat for manufacturing products, such as cement, lime and refractory.    ADVANTAGE - The pelletized fuel product can be readily obtained from the packaging and labeling industries, preferably from municipal refuse.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method of generating heat by combusting the pelletized fuel in a stoker boiler or a fluidized bed combustor; and    (2) a method of scrubbing combustion gas, comprising combusting a fuel pellet comprising a fuel source blended with a sorbent effective to absorb at least one of hydrochloric acid, hydrogen fluoride, sulfur oxide or mercury vapor.
NOVELTY - The system has an electrochemical compressor (120) that compresses a fuel source (110). A low pressure compressed fuel reservoir (LPCFR) (140) is fluidly connected to the electrochemical compressor. A high pressure compressed fuel reservoir (HPCFR) (160) is fluidly connected to the electrochemical compressor. A medium pressure compressed fuel reservoir (MPCFR) (150) is fluidly connected to compressor (120). The fuel dispensing units (130) are fluidly connected to the LPCFR, HPCFR and MPCFR.    USE - Compressed fuel storage system used for refueling hydrogen powered vehicles.    ADVANTAGE - The hydrogen tank is rated for a design pressure and filling to the design pressure so as to maximize the range of the vehicle. The pressure changes felt by the stacks of membrane-electrode assembly (MEA) of compressor are reduced in order to reduce damage to compressor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of maintaining pressure within compressed fuel storage system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a compressed fuel dispensing station.    Fuel source (110)    Electrochemical compressor (120)    Fuel dispensing unit (130)    LPCFR (140)    MPCFR (150)    HPCFR (160)
NOVELTY - A catalyst comprises a molybdenum catalyst encaged in a zeolite support comprising one or more components chosen from HZSM-5, Y-type mordenite, MCM-22, MCM-41, H-Y-type faujasite, and H-( beta ) zeolite.    USE - Catalyst is used for catalyst system (claimed) for producing hydrocarbon fuel products e.g. hydrocarbon liquid and ethylene-rich and propylene-rich hydrocarbon gas.    ADVANTAGE - The catalyst enables simple production of hydrocarbon fuel products having excellent purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for catalyst system, which comprises metal on zeolite support comprising HZSM-5 zeolite. The system produces a hydrocarbon liquid having aromatic content of 90 mol% or more.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the production of hydrocarbon fuel products.
NOVELTY - Bio-oil is produced which involves providing a catalyst bed in a fluid state, where the catalyst bed comprises red mud; heating the catalyst bed to a temperature suitable for pyrolysis; providing a flow of a non-reactive fluid onto the catalyst bed; providing feedstock in the flow of non-reactive fluid; and pyrolyzing the feedstock.    USE - The method is useful for producing bio-oil (claimed).    ADVANTAGE - In producing bio-oil, the major advantage of the red mud catalyst is its apparent rejection of oxygen through carbon dioxide (CO2) instead of carbon monoxide (CO) and hence less consumption of carbon for oxygen rejection. The physico-chemical properties of the red mud oil also appeared to be slightly better than the HZSM-5 oils. Further, red mud is a waste product of the Bayer alumina process and could be procured at minimal cost and hence improve the economics of biomass catalytic pyrolysis process. Red mud could be potentially used to replace HZSM-5 for catalytic biomass pyrolysis. The red mud appeared to be stable and regenerable for catalytic pyrolysis reactions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a bio-oil prepared from the method; and    (2) a pyrolysis catalyst comprising red mud.
NOVELTY - The combined quenching- and washing system has a gasification reactor (1), in which fuel is implemented to raw gas and liquid slag at a specific temperature and pressure, where the raw gas and the liquid slag is transferred to a quencher (6) arranged below the gasification reactor via a gas and slag discharge (3). The raw gas leaves the quencher by a raw gas outlet (15) arranged in the upper region of the quencher.    USE - Combined quenching- and washing system for use in entrained-flow gasification reactor for the implementation of ash-containing fuels with a free-oxygen gasification agent to a raw gas having a high hydrogen content.    ADVANTAGE - The combined quenching- and washing system has a gasification reactor, in which fuel is implemented to raw gas and liquid slag at a specific temperature and pressure, where the raw gas and the liquid slag is transferred to a quencher arranged below the gasification reactor via a gas and slag discharge, and hence enable cooling the hot gasification gas and the entrained liquid slag in an efficient manner, and thus obtaining high degree of separation of dust.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a quench system with a central tube and a water impinged inner sheath.    Gasification reactor (1)    Cooling screen (2)    Gas and slag discharge (3)    Quencher (6)    Raw gas outlet (15)
NOVELTY - The system has a gasification reactor (1) that is operable at temperatures of 1200 to 1900 degrees C. A quencher is arranged beneath the reactor. The gas and slag outlet (3) is provided for transferring the crude gas and liquid slag into a quencher. A central tube (5) is dipped into a water bath at a lower end of quencher. The crude gas outlet is provided for leaving crude gas. A nozzle ring (13,14) is provided between a surface of the water bath and the crude gas outlet, and is configured to spray water into crude gas. A guide tube (4) concentrically surrounds a lower end of central tube.    USE - Crude gas scrubbing system for high separation level of dust in entrained flow gasification unit for reaction of ash-containing fuels with gasifying agent containing free oxygen to produce crude gas having high hydrogen content.    ADVANTAGE - The dusts formed from biomasses, products of thermal pre-treatment such as cokes, torrefaction products and fractions having high calorific values from communal and commercial residual and waste materials are separated. The fuel dusts can be supplied to the gasification as a gas/solid or liquid/solid suspension. The wear in the separators and crude gas-conducting lines are reduced. The safety-relevant leaks can be avoided. The lifetime of the scrubbing system is prolonged. The inner casing is fitted for protection of the pressure casing against erosion and corrosion.    DETAILED DESCRIPTION - The upper end of the central tube is configured to introduce water into the stream of crude gas and slag. The lower end is configured to separate the slag into the water bath while the crude gas rises upward within a bubble column outside the central tube.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the crude gas scrubbing system.    Gasification reactor (1)    Gas and slag outlet (3)    Guide tube (4)    Central tube (5)    Nozzle rings (13,14)
NOVELTY - This utility new type claims a one inner eutrophic waste water and a microorganism fuel cell is a power generation, comprising an anode room and cathode room, anode room and cathode room through proton exchange film, anode room set with anode electrode, an anode room is an anode liquid and active sludge solution, a cathode room set with cathode electrode, inner cathode room is cathode liquid and anode electrode and cathode electrode a connection and a bottom anode room set with water inlet, the water inlet through the water pump regulating pool and a bottom cathode room set with aeration pipe, an aeration pipe and a air blower, an anode electrode is carbon felt, the cathode electrode is graphite anode room side wall upper part and side wall are set with anode liquid circulation wherein the anode room side wall liquid circulation wherein the anode of anode liquid circulation wherein a side wall lower part of upper part through circulation pump connected, anode room top set with biological pneuma collecting wherein, anode room side wall upper part set with the water wherein. This utility new type can properly treat eutrophic wastewater.
NOVELTY - The method involves providing an exhaust gas sensor (17) for detecting the exhaust gas of each cylinder (11) of the internal combustion engine (10). The exhaust gas in the respective cylinders is detected meteorologically and individually. The detected exhaust gas is compared with the set point value, so as to determine the cylinder-specific deviation between the target value and the exhaust gas. The cylinder misfire for each cylinder is determined individually on the basis of each individual cylinder-specific deviation.    USE - Operating method for performing specific detection of misfires in cylinder of internal combustion engine such as gas engine constructed as marine engine of exhaust after-treatment system.    ADVANTAGE - The detection accuracy of the misfires in the cylinder is improved. The device to detect sporadic misfiring is safe and reliable. The exhaust of the gas from each cylinder in different crankshaft angle ranges can be avoided. The low-speed internal combustion engines can be guaranteed due to the low frequencies of the exhaust gas of the individual cylinders with a single exhaust gas sensor so as to attain sufficient accuracy of the cylinder-selective detection of misfiring. The emissions of exhaust components such as soot, carbon monoxide, nitrogen oxide and hydrocarbons are reduced. The high risk of damage to the internal combustion engine is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the internal combustion engine.    Internal combustion engine (10)    Cylinder (11)    Compressor (13)    Turbocharger (14)    Exhaust gas sensor (17)
NOVELTY - Preparation of incanone comprises taking spearmint, crushing, adding biological enzyme, enzymolyzing for 8-10 hours, adding 60-80% ethanol, microwave or ultrasonic extracting for 2-3 times, and concentrating extract; adding water, dispersing, absorbing in macroporous resin column, eluting with water, eluting with 50-70% ethanol, and collecting eluate; and separating using liquid phase chromatography, UV on-line detecting, collecting target component, and drying at low temperature.    USE - Method for preparing incanone used for preparing medicine for treating leukemia, particularly lymphatic leukemia and myeloid leukemia (claimed).    ADVANTAGE - The method is simple and has high yield and less pollution. The incanone has high purity.
NOVELTY - The system has a raw gas and liquid slag discharger for discharging raw gas and a slag into a quencher (6) arranged under a gasification reactor (1), and a central tube provided into a water bath (9). The central tube is double-walled to form a ring channel, and an annular channel supplies cooling water at an annular gap in the water bath. The raw gas is sprayed with water between the water bath and the raw gas output (15) by nozzle rings (13, 14). The central tube is connected over a conduit tube (4).    USE - Raw gas washing system for an airborne current gasification reactor for conversion of ash-containing fuel with free oxygen containing gasification part to a raw gas under recovery of a high hydrogen portion.    ADVANTAGE - The system cools the raw gas up to temperature of water vapor saturation easily. The system performs conversion reaction between carbon monoxide and water vapor, thus ensuring a higher hydrogen portion in the raw gas. The system protects pressure cladding against abrasion and corrosion by an inner jacket.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a raw gas washing system with a central tube and an inner jacket.    Gasification reactor (1)    Conduit tube (4)    Quencher (6)    Water bath (9)    Nozzle rings (13, 14)    Raw gas output (15)
NOVELTY - An oral controlled release tablet comprises paliperidone or its salt or ester; first coating layer comprising 0-61% polyvinyl acetate, 22-54% polyethylene glycol, 12-40% polyethylene alcohol copolymer, 2-7% talc powder, and 5-20% citric acid; and second coating layer comprising 60.6-69% polyvinyl acetate, 10-18.2% polyethylene glycol-polyethylene alcohol copolymer, 12.9-20% talc powder, and 3-7% citric acid.    USE - Paliperidone oral controlled release tablet.    ADVANTAGE - The tablet has simple production process without using organic solvent, making it green and environment-friendly, and suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the tablet comprising mixing and sieving paliperidone and polyoxyethylene, adding stearic acid magnesium or sodium stearyl fumarate, adding the rest of the materials, and tableting.
NOVELTY - A temperature- and pH-responsive xylan-based hydrogel is prepared by dissolving xylan in hot water to obtain xylan solution, adding N-isopropylacrylamide and acrylamide, adding crosslinking agent, performing nitrogen gas bubbling, adding photopolymerization initiator, mixing, cooling at room temperature, placing in UV radiation reactor, performing UV irradiation at room temperature, and washing with deionized water to remove residual reagents and obtain resulting solid.    USE - Preparation of temperature- and pH-responsive xylan-based hydrogel for manufacture of drug delivery agent (claimed).    ADVANTAGE - Preparation process is simple, easy to operate, and environment-friendly. Product has good biocompatibility and good drug slow-release.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of drug delivery agent which involves soaking temperature- and pH-responsive xylan-based hydrogel in drug-ethanol solution, sealing, placing in dark place for 20-28 hours, taking out, placing in vacuum drying oven, and drying.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of drug delivery effects of simulated intestinal fluid and simulated gastric fluid in a physiological environment at different pH. (Drawing includes non-English language text).
NOVELTY - Sustained-release chlorine dioxide powder comprises 5-10 wt.% chlorine dioxide precursor, 12-20 wt.% activating agent, 5-10 wt.% slow release agent, 12-20 wt.% gel, 43-47 wt.% filling agent and 5-10 wt.% inert agent.    USE - Sustained-release chlorine dioxide powder used as disinfectant for purifying air by removing formaldehyde (claimed).    ADVANTAGE - The sustained-release chlorine dioxide powder is prepared in a simple, eco-friendly and cost-effective manner, has wide industrial applicability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing sustained-release chlorine dioxide powder, which involves:    (A) drying chlorine dioxide precursor at 60-70 degrees C for 8-10 hours, activating agent at 50-70 degrees C for 10-15 hours, filling agent at 60-80 degrees C for 4-7 hours and inert agent at 80-90 degrees C for 4-6 hours in a drying tank, and mixing them to obtain a mixture; and    (B) adding gel uniformly in the mixture in a container to obtain final product.
NOVELTY - A biological organic fertilizer comprises 17-18 pts. wt. organic fertilizer, 2-3 pts. wt. inorganic nutrient composition, and microbial inoculum. The organic fertilizer is obtained by heating organic raw materials, drying, crushing, sterilizing, adding fermentation microbial inoculum, and fermenting at 25-35 degrees C for 7-10 days. The fermentation microbial inoculum comprises 20-30 wt.% actinomycetes, 10-20 wt.% Lactobacillus and 50-70 wt.% activated yeast.    USE - Biological organic fertilizer used for promoting plant growth.    ADVANTAGE - The fertilizer has pH of 5.5-8.5 and water content of 20-30%. It has insect eggs death rate of more than 95%.
NOVELTY - Bio-organic fertilizer comprises 80-88 pts. wt. organic matter raw material, 2-3 pts. wt. microbial inoculum, 5-8 pts. wt. tobacco stalk powder, and 3-6 pts. wt. adhesive.    USE - Used as bio-organic fertilizer.    ADVANTAGE - The fertilizer uses various materials with synergistic effect, improves water retention and fertilizing efficiency, can retain water and nutrients in soil to be absorbed, and exhibits insecticidal effect. The method has proper controlled preparation process parameter, and can reduce fertilizer application cost and production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing bio-organic fertilizer comprising (i) raw material processing: adding raw material according to the ratio in microbial inoculum, obtaining microbial inoculum containing organic raw material, stacking the organic raw material in a fermentation room, adjusting temperature of the fermentation room at 20-25 degrees C, spraying 11-17% of water in the stacked raw materials, carrying out fermentation, turning 1-3 times the raw heap during fermentation process, after 30-40 days of fermentation process, obtaining the fermentation product, (ii) placing the resulting end product of fermentation in a mill and crushing into powder of 100-130 meshes, in the crushing process, adding tobacco stalk powder in fermentation product and mixing uniformly, (iii) granulating: mixing the step (ii) processed material and adhesive, stirring at a speed of 50-70 revolutions/minute for 20-30 minutes, granulating to obtain granules, (iv) drying: placing the step (iii) processed granules in a drier and drying using a steam flow at 190-210 degrees C to a moisture content of 4-5%, and (v) packing: passing the step (iv) processed granule by 100-120-mesh sieve, returning bottom sieve particles into step (ii) fermentation and circulation process, screening and packaging into 25-50 kg/bag, namely obtaining biological organic fertilizer.
NOVELTY - A solid base catalyst comprises an active component including alkaline earth metal oxide, transition metal oxide, and other metal oxide or optionally other complex metal oxide. The alkaline earth metal is calcium or magnesium. The transition metal is lanthanum or zirconium. The other metal is aluminum.    USE - Solid base catalyst used for the synthesis of urea and ethanol diethyl carbonate (claimed).    ADVANTAGE - The catalyst has simple preparation method, high activity, and good stability, and is environment-friendly and easy to separate and recover.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of solid base catalyst comprising adding alkaline earth metal, transition metal or other metal to soluble metal salt to prepare aqueous solution, dropping into the precipitator, and adjusting pH value to 8-12, carrying out precipitation method and co-precipitation method to obtain a precursor metal hydroxide or composite metal hydroxide, drying at 50-150 degrees C for 2-24 hours, sintering for 2-10 hours and calcining at 200-1000 degrees C to obtain a metal oxide or composite metal oxide, where the soluble metal salt is halide, nitrate or carbonate; and    (2) a method for preparing dimethyl carbonate ethyl ester comprising adding the urea and ethyl alcohol in high pressure reaction kettle, where the mol ratio of the added urea and ethyl alcohol is 2:1-20:1, the catalyst dosage is 0.1-90 mass%; and draining air within the reactor with nitrogen, control reaction at 150-300 degrees C and 1-5 MPa, reacting for 1-10 hours to obtain the dimethyl carbonate ethyl ester.
NOVELTY - Preparing a controlled release nitrogen carbon source composite particle comprises adding biodegradable polymer, a natural solid-phase organic matter, a reinforcing material, a crosslinking agent, a pH adjusting agent, an oxygen scavenger and a trace element into a reaction container, uniformly mixing, melting the mixture, extruding the melted mixture, granulating the extruded mixture, and uniformly stirring.    USE - The method is useful for preparing a controlled release nitrogen carbon source composite particle, which is useful for biological denitrification process (claimed) in underground water.    ADVANTAGE - The method simply and easily prepares the controlled release nitrogen carbon source composite particle with good mechanical properties and denitrification efficiency and reduced secondary pollution, and does not cause harm to human health.
NOVELTY - The small portable hydrogen oxygen generator has electrolytic groove which is connected with oxygen pipe (5), hydrogen pipe and cable conduit. The oxygen pipe is connected to main oxygen collection pipe (8). The hydrogen pipe is connected to main hydrogen pipe. A water tank (3) is provided with closed circulation fluid path. The collecting water pipe (7) is connected to the main water pipe. A pump portion (4) is provided on the main water pipe so as to drive the fluid flow.    USE - Small portable hydrogen oxygen generator for on-vehicle.    ADVANTAGE - The structure of the hydrogen oxygen generator is simplified easily. The size of the hydrogen oxygen generator is reduced. The circulation waterways within the gas cell are removed immediately. The efficiency of the electrolysis is increased. The electrolysis process is filtered to exclude water vapor, oxygen and hydrogen. The design structure of gas path from electrolytic groove is timely output.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the small portable hydrogen oxygen generator.    Water tank (3)    Pump portion (4)    Oxygen pipe (5)    Collecting water pipe (7)    Main oxygen collection pipe (8)
NOVELTY - This new utility model relates to one of artificial biological water filter pool, wherein the biological filter pool comprises a regulating pool and a filtering pool, the regulation pool bottom through hole and a filter pool connected, part of the regulating pool is set with a water inlet, the water filter pool provided with micro-pore aeration pipe, cement plate and filler layer, the cement board at lower part is set with the water filter pool, the cement board and laying upper part with micro-pore aeration pipe, said micro-hole aeration pipe and upper part is set with filler layer. This new utility model is simple structure, small aeration, can consume low, can adsorb microorganism in plant, for growing the plant supply carbon dioxide, plant through photosynthesis effect for microorganism oxygen supply, and the two common degradable organic waste water, the reinforcing of the ability to treat waste water, has the good popularization value.
NOVELTY - This utility new type belongs to the outside sewage purification and water ecological restoration technology field, claims a one aritificial water of a device, including aritificial float grass, connecting cylinder and rod. and; the aritificial float grass is a part cut into several rectangular strip lower connecting part is a cloth grid main body integrally, the connecting cylinder cloth-shaped object is set on main body of lower part, a rod or rope passes through connecting cylinder, two end connecting cylinder is exposed. This utility new type aritificial water grass device, using non-woven cloth material, this material use life is long, the effect is for absorbing water in impurities is good, it can effective purification of water quality, a degradation; at the same time aritificial float grass is a part cut into several rectangular strip lower part is a cloth grid main body, without need to welding, not in a line corrosion and a long fall of condition, it will not cause a secondary pollution.
NOVELTY - This utility new type belongs to the sewage purification and water ecological restoration technology field, specific relates to a one aritificial float module, including aritificial float grass used for a heavy object and a fixed bag; the aritificial float grass is a part cut into several rectangular strip lower part is a cloth grid main body, lower part of the cloth-shaped material main body and fixing a bag. This utility new type aritificial float module, fill stone, brick or steel block in inner fixing bag, so can effectively make the aritificial float a fixed in a water stream, the fixed bag can sink bottom or in suspension in water, each fit a water area, the utility model is new type aritificial float module, using non-woven cloth material, this material use life is long, the effect is for absorbing water in impurities is good, it can effective purification of water quality, a degradation.
NOVELTY - This utility new type relates to design of large-scale marsh gas pool for a one of a a temperature control pressure, wherein comprising at least one a marsh gas pool, mounted with at least a chain wheel two inner each in a marsh gas pool (1), a upper chain wheel (1) mounted with a transmission chain (2) with at least 1 a cage in a transmission chain (2) (3) containing methane fermentation material, wherein one chain wheel (1) of a chain wheel shaft through transmission mechanism and motor transmission connected, wherein each in a marsh gas pool are set with material entrance is set with liquid outlet in the bottom. This utility new type provide the one a temperature control pressure of a large-scale marsh gas fermentation pool is a design, use a after the planting of crop straw and cultivation farm dung dirt comprehensive treatment, the waste is valuable, eliminate the pollution source, solves the problem that the part energy.
NOVELTY - Degumming and/or refining crude oil containing impurities, comprises: providing (110) a flow-through, hydrodynamic cavitation device having a flow path; mixing (112) the crude oil with a degumming agent to form mixed fluid having an oil phase and a water phase; pumping (114) the mixed fluid into the flow path of the cavitation device at a pre-determined pump pressure; generating (116) cavitational features in the mixed fluid such that the impurities are transferred from the oil phase to the water phase; and separating (118) the oil phase from the water phase.    USE - The method is useful for degumming and/or refining crude oil comprising edible vegetable oil, animal fat or tallow, and oil from bacteria, yeast, algae, prokaryotes or eukaryotes containing impurities e.g. phosphatides and free fatty acids (claimed), which is useful in food, chemical and pharmaceutical industries and for producing biodiesel. The vegetable oil is crude vegetable oil comprising canola, coconut, corn, cottonseed, grape seed, ground nut, linseed, palm, peanut, rapeseed, rice bran, safflower, soybean and sunflower.    ADVANTAGE - The method is capable of efficiently and rapidly degumming and/or refining crude oil with less accumulation of waste harmful to environment, reduced energy consumption and low levels of phosphorus and metals, thus improving taste, smell, appearance and shelf life of the oils.    DESCRIPTION OF DRAWING(S) - The figure shows a flowchart of a method for degumming and/or refining crude oil.    Providing a flow-through, hydrodynamic cavitation device having a flow path (110)    Mixing the crude oil with a degumming agent, (112)    Pumping the mixed fluid into the flow path of the cavitation device, (114)    Generating cavitational features in the mixed fluid (116)    Separating the oil phase from the water phase. (118)
NOVELTY - The system has a first stage comprising a first reaction chamber (101) to receive feedstock from feedstock sources, process gas from process gas sources (107) and energy from energy generators. The first stage converts the feedstock into an intermediate product for delivery to a second stage. The second stage comprises a second reaction chamber that receives the product from the first stage and the process gases from the process gas sources. An intermediate stage is placed between the first stage and the second stage in which the product from the first stage is processed.    USE - System for converting hydrocarbon material e.g. fossil hydrocarbons such as coal, bitumen, oil sand, tar sand, oil shale, petroleum reside, asphaltenes, pre-asphaltenes or vitrinite and kerogen-containing materials, and biomass, into a product e.g. petroleum product such as synthetic crude oil.    ADVANTAGE - The system converts and upgrades hydrocarbon fuel products in an efficient manner. The system allows the second reaction chamber to improve quality of intermediate product stream and to form a final product stream in an efficient manner.    DETAILED DESCRIPTION - The intermediate product is coke. The energy generators comprise a microwave generator (111). The feedstock is in powder form i.e. coal particle. The gas is selected from a group consisting of argon, helium, krypton, neon or xenon, carbon monoxide, carbon dioxide, water vapor methane, hydrocarbon gas and hydrogen gas. An INDEPENDENT CLAIM is also included for a method for converting hydrocarbon materials into a product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a system for processing hydrocarbons.    Reaction chamber (101)    Reaction tube (103)    Process gas sources (107)    Product storage vessels (109)    Microwave generator (111)    Waveguide (113)    Injection device (118)
NOVELTY - A reactor (100) consists of a housing (101) as reactor component (106). The housing comprises a plasma source and a catalyst. The catalyst contains a mesoporous support and a metal carried by the mesoporous support as catalyst components. The metal is chosen from palladium, nickel, and silver. A portion of plasma source in the housing is located in the upstream of catalyst.    USE - Reactor is used in preparation of hydrogen and/or ethene used for preparing downstream product e.g. polythene used for forming molded product (all claimed). Uses include but are not limited to electronic device, bumper, dashboard, furniture, merchandise, plastic bag, film, and container.    ADVANTAGE - The reactor enables efficient preparation of hydrogen and/or ethene with high yield and selectivity with respect to desired products due to presence of catalyst having excellent durability, by fast and economical process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of ethene and/or hydrogen, which involves feeding methane into the reactor, reacting methane in the reactor, and obtaining ethene and/or hydrogen; and    (2) preparation of downstream product, which involves preparing ethene, and reacting ethene.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of reactor.    Reactor (100)    Housing (101)    Reactant (102)    Product (103)    Reactor entrance (104)    Reactor component (106)
NOVELTY - Bio-oil is hydrogenated with a catalyst comprising metal on solid support at preset hydrogen pressure to remove preset amount of oxygen-containing heteroatoms from the bio-oil. Then the bio-oil is subjected to hydrodeoxygenation process in presence of bifunctional catalyst comprising a metal on solid support and solid acid or metal on solid acid support at preset hydrogen pressure and temperature to obtain bio-oil product (20) comprising fuel-range hydrocarbons.    USE - Process of upgrading bio-oil used for producing fuel-range hydrocarbons used in petroleum refineries for producing jet fuel, gasoline, and diesel.    ADVANTAGE - The method enables upgrading of bio-oil without using sulfide-containing catalyst at low operating temperature, by an economical process. The upgrading process is performed continuously or batch-wise. The catalyst used for upgrading bio-oil has high activity and durability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) bifunctional catalyst, which consists of a metal on solid metal oxide-support combined with solid acid comprising acidic metal oxide and/or acid zeolite having preset concentration, or a metal on acidic metal oxide support and/or acid zeolite support; and    (2) system (100) for upgrading bio-oils, which has reactor (r1) pressurized with hydrogen gas, and reactor (r2) pressurized with hydrogen gas. The reactor (r1) comprises a catalyst comprising metal on solid support. The reactor (r2) comprises bifunctional catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of two-stage reactor used for upgrading bio-oil.    Reactor stages (2,4)    Introduction device (10)    Liquid feed (12)    Bio-oil product (20)    System (100)
NOVELTY - Producing fuel from a renewable feedstock, comprises: deoxygenating the renewable feedstock in a deoxygenation reaction zone (20) to produce normal paraffins; isomerizing the normal paraffins in an isomerization reaction zone (40) to produce isomerized paraffins; and forming aromatic compounds from non-aromatic compounds in an aromatic production zone (60) that is downstream from the deoxygenation reaction zone.    USE - The method is useful for producing fuel from a renewable feedstock (claimed).    ADVANTAGE - The method: produces fuel with lower environmental impact and improved cold flow properties; utilizes the renewable feed stock that exhibits fewer green house gas emissions, thus is more environmentally friendly; and increases the fuel yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for producing fuel from a renewable feedstock, comprising: a renewable feedstock feed system; a deoxygenation reaction zone comprising a hydrogenation catalyst, where the deoxygenation reaction zone is downstream from the renewable feedstock feed system; an aromatic production zone comprising an aromatic catalyst, where the aromatic production zone is downstream from the deoxygenation reaction zone; and an isomerization reaction zone comprising an isomerization catalyst, where the isomerization reaction zone is downstream from the deoxygenation reaction zone.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of the renewable feedstock feed system.    Pretreatment zone (16)    Deoxygenation reaction zone (20)    Isomerization reaction zone (40)    Aromatic production zone (60)    Aromatic distillation column (70)
NOVELTY - A photoelectrode has protecting layer and photoactive semiconductor layer(s). The protecting layer is water-resistant, has visible light transparency, and is arranged on light incident side of the photoactive semiconductor layer. The protecting layer comprises silicon nitride, silicon oxide, silicon carbide or alumina, and has holes having diameter in nanometers. The holes are filled with catalyst.    USE - Photoelectrode is used for photoelectrocatalytic process for production of hydrogen and water purification.    ADVANTAGE - The material contained in protecting layer in photoelectrode is economical. The protecting layer is transparent.    DETAILED DESCRIPTION - A photoelectrode has protecting layer and photoactive semiconductor layer(s). The protecting layer is water-resistant, has visible light transparency, and is arranged on light incident side of the photoactive semiconductor layer. The protecting layer comprises silicon nitride (SiNx, where x is not defined), silicon oxide (SiOx), silicon carbide (SiCx) or alumina, and has holes having diameter in nanometers. The holes are filled with catalyst.
NOVELTY - This new utility model claims of one kind of hydropower station water surface garbage processing system, including via transmission belt in turn connected with the garbage stacking chamber, cutting system, mixing agitator, compressor, drying room, a granulator, and finished product bin, also comprising mixing stirrer and separately connected with the combustion improver and adhesive material. This new utility model for rubbish change into new fuel, forming fine fuel of unified specification, changes waste into valuable, solves of garbage is then accumulated by the second time pollute equal problem, which is good for protecting the environment, then obtaining of lasting can of fuel resource, with relatively wide society value and economic value.
NOVELTY - Improved synthesis of ammonia involves degreasing alkylated gas, supplying into ammonia condenser, performing ammonia gas exchange separation of liquid ammonia, supplying compressed gas into separator, separating oil, reacting nitrogen and hydrogen in presence of catalyst, recovery waste, heating using water-heater, cooling the ammonia gas using condenser, performing cold exchange separation, recovering ammonia from compressor, separating ammonia, spraying soft water, absorbing remaining ammonia by soft water to generate high-quality high-purity ammonia, and recovering ammonia.    USE - Improved synthesis of ammonia (claimed).    ADVANTAGE - The method enables efficient improved synthesis of ammonia with high purity, high quality, high productivity and reduced energy and power consumption.
NOVELTY - Preparation of quinolone compound involves carrying out hydrogen amination reaction of aromatic amine compound (I) and alkyne compound (II) in absence of solvent to obtain aromatic vinylamine compound (III) as intermediate compound, and subjecting the resultant product to direct intramolecular cyclization reaction in presence of catalyst to obtain quinolone compound (IV). The catalyst comprises polyphosphoric acid, concentrated sulfuric acid, diphenyl ether and/or Eaton's reagent.    USE - Preparation of quinolone compound (claimed).    ADVANTAGE - The method provides quinolone compound by environmentally-friendly, safe, economical and efficient process.    DETAILED DESCRIPTION - Preparation of quinolone compound involves carrying out hydrogen amination reaction of aromatic amine compound of formula (I) and alkyne compound of formula (II) in absence of solvent to obtain aromatic vinylamine compound of formula (III) as intermediate compound, and subjecting the resultant product to direct intramolecular cyclization reaction in presence of catalyst to obtain quinolone compound of formula (IV). The catalyst comprises polyphosphoric acid, concentrated sulfuric acid, diphenyl ether and/or Eaton's reagent.    R1-R4=H, halo, methoxy, trifluoromethyl, nitro, alkyl or aryl;    R5=H, alkyl or cycloalkyl;    R6=H, ester group, alkyl or aryl;and    R7=alkyl.
NOVELTY - Preparation of olmesartan medoxomil (I) involves removing trityl protecting group of trityl olmesartan medoxomil (A) in organic solvent containing macroporous acidic ion-exchange resin.    USE - Preparation of olmesartan medoxomil (claimed).    ADVANTAGE - The method provides olmesartan medoxomil having excellent stability, heat resistance, durability and mechanical strength, by environmentally-friendly and economical process under mild reaction condition without requiring neutralization reaction and reduced side reaction.    DETAILED DESCRIPTION - Preparation of olmesartan medoxomil of formula (I) involves removing trityl protecting group of trityl olmesartan medoxomil of formula (A) in organic solvent containing macroporous acidic ion-exchange resin.
NOVELTY - Methanol gasoline rubber swelling inhibitor comprises 12-13 pts. wt. 2-mercaptobenzothiazole, 6-9 pts. wt. iodopropynyl butylcarbamate, 1-2 pts. wt. butylhydroxyanisole, 15-18 pts. wt. 2,6-di-tert.-butyl-p-cresol, 7-10 pts. wt. sodium dodecyl sulfate, 12-15 pts. wt. 2-ethyl-imidazole, 6-9 pts. wt. cyclooctadiene ruthenium dichloride, 8-12 pts. wt. p-methoxypropiophenone, 2-3 pts. wt. polyisobutylene succinimide, 3-4 pts. wt. tert.-butyl-dimethyl-chlorosilane and 12-13 pts. wt. methyl tert.-butyl ether.    USE - Methanol gasoline rubber swelling inhibitor.    ADVANTAGE - The methanol gasoline rubber swelling inhibitor has excellent oxidation resistance, good anti-corrosive property, prevents abrasion and corrosion, and maintain flexibility.
NOVELTY - This utility new type claims a biogas purification one drying device, comprising purification drying tube, purification drying tube by purification chamber and drying chamber, the purification chamber and the drying chamber through gas channel is set on the top of connecting part and purification cavity inner cavity is set with sedimentation pool, purification cavity one side set with air inlet, the pneuma wherein a top of the pneuma pipeline, a pneuma channel set on the bottom inner sedimentation pool, purification cavity one side set with liquid inlet, the bottom of the cavity set with purification purification cavity drainage barrel, drying the inner cavity set with guide plate, the guide plate interval set on drying cavity, the cavity is set with drying chamber discharging drying cylinder, the drying cavity is one side a gas condensing channel, gas condensing channel connecting the air outlet. This utility new type of advantages is: it prolongs use life of gas increase operation efficiency, prevent the marsh gas discharge harm human and animal health of cleaner.
NOVELTY - This utility new type claims a circulation heat biogas heat pump heating system, to increase the utilization rate of the energy. Comprising a pump working fluid circulation system, a methane supply system and waste heat recovery purification system, two outlet of the heat pump working medium circulation system comprise marsh gas internal combustion engine, a compressor, a condenser, a throttle valve, an evaporator, an air source heat exchanger and three-way valve, three-way valve a and a refrigerant entrance and air source heat exchanger of evaporator is a entrance, an evaporator refrigerant outlet of the air source heat exchanger and a rear exit and entrance of compressor in parallel connection, marsh gas internal combustion engine is compressor supply power, waste heat recovery purification system comprising a jar set is used for the marsh gas internal combustion engine jar set heat cooling water heat exchanger and tail pneuma. This utility new type is a marsh gas using the one second energy driving a heat pump heating, and using the heat recovery device, which can reduce the consumption of one energy, which is good for energy saving and emission reduction, at the same time, increase the utilization rate of the energy.
NOVELTY - This utility model new supply of one use of float grass in biomass grain and production line, it can be for fishing the grass onto local, rapid reduction treatment, and biomass grain in the later stage can be not only biomass as fuel, organic fertilizer base material and feed base material, also can be as animal and plant, ensure the float grass to obtain full use, in addition, through after the grass planting method process, it will not produce odour ensure of environmental quality. It comprises upper part hopper, the upper part and the lower part outlet arranged with hopper, the upper part and the lower part hopper alignment feedstock outlet port of said extrusion device, a discharge port of the extrusion device is input end and the second transport belt and the second transport belt and the output end connected to feeding port of the pulverizer, a discharging port of the pulverizer through material transporting tube connected to import the separator, outlet of said separator connected to said grain machine and feeding port, a grain machine and the discharging port by the third transporting belt connected to canning sealing machine.
NOVELTY - This utility new type claims a lignite processing system one, positoin b including the top of feeding mechanism is located at the bottom of the discharging mechanism, set with a feeding mechanism and a discharging mechanism is between two or more lengthways a single brown coal extracting substance and device, used for supporting each single brown coal extracting substance and device of support frame, set with a connection between two adjacent a single brown coal extracting substance and c is a lengthways extension of the compensation device, and adjacent to the discharging mechanism of single brown coal extracting substance and device of hot air supply mechanism, extracting lignite device both comprise a multi-heat conducting pipe, the heat conducting pipe along horizontal direction and are set with a hot air supply mechanism and connection. This utility new type heat guide pipe along the horizontal direction set, extracting lignite part by a lignite device compose a multi-way air path extension, increase heat efficiency, but also can prevent the heat pipe and fin cracking of, at the same time saving and saving the set of compensation, a along the lengthways, the buffer effect, reduce the heat stress, increase use of safety.
NOVELTY - This utility new type claims a one anti-blocking air inlet and an air outlet filter of biomass gasification furnace, belonging to the gasification furnace technology field, comprising feed inlet cover, outside furnace cylinder, furnace inner cylinder, a slag outlet door, a slag outlet, a pedestal, a supporting leg, a pressure material pole, the first air outlet and second air outlet, outside cylinder and inner furnace said furnace form one cavity, the first furnace inner cylinder upper end is air outlet, the second air outlet is located outside furnace cylinder lower part, in pedestal set with the pneuma channel, air inlet channel connected and a bottom inner outside a furnace, a furnace the pneuma channel of inner cylinder end is set with exit guide pneuma disk. The technology scheme through the first air outlet and second air outlet are set, the gas flowing outside furnace and furnace inner cylinder is a cylinder, a buffer of a certain degree, cooling, depositing, discharging a gas more clean, at the same time through set with inner air inlet channel, and a the pneuma channel outlet end setting the pneuma disk, and the air inlet furnace chamber, avoiding the blocking hole, air inlet at the same time, uniform, a stable effect.
NOVELTY - This utility new type relates to biomass pyrolysis gasification device, especially a low nitrogen one biomass combustible gas preparing device. Carrier including a heater, a heater carrier comprising shell, wherein, further comprising dividing efficient separator and pneumatic cyclone gasification furnace, the carrier of heater is volute carrier heater, the top part is set with shell cover, and the shell inner by up to below in turn is divided into carrier channel, carrier heating room and wind room, heating the bottom carrier of room set with worm shell, with a burner mounted in the notch of worm shell, a device condition does not use oxygen and oxygen-enriched air is low, obtain a low nitrogen, high heat value of a combustion gas, and this device has a single furnace gas amount is large, a process is simple and reliable, device manufacturing cost and operation cost is low, without phenol water produce a tar content of at least can be a biomass of clean efficient use provide the technology condition.
NOVELTY - This new type utility claims one with a filter function of biomass gas furnace, belonging to gas furnace tool technology field, including hearth panel, a bracket, a , support leg, gas air inlet pipe, a furnace end and furnace end supporting base, a cooking bench panel through the bracket mounting a gas tank, a furnace head is located between the cooking bench panel and gas tank, furnace end through support base mounted in gas tank upper, is one a closeness, and through leg support of the bottom of a gas tank with a terminal hole pneuma, through air inlet pipe and gas furnace end connected, lower end with pneuma hole, set with cold plate in a gas tank, condensing the gas tank inner separating a multi-space layer, and each layer of space are a close part, cold plate under plane set with the radiating piece. The technology scheme through condensing plate structure is set with inclined arrangement, setting radiating fin and lower a condensing plate structure, inner bottom is increased biomass pneuma from tank to tank after entering into a gas tank in circulation flow time to reach the filter tar, dust and water a is effect.
NOVELTY - Production of enhanced fertilizer, involves (a) mixing phosphoric acid with carbamide in a reaction vessel, heating the mixture, stirring the mixture, cooling and centrifuging the mixture to obtain intermediate, (b) preparing potassium dihydrogen phosphate by reacting the intermediate with a basic potassium salt, crystallizing and filtering to obtain potassium dihydrogen phosphate, and (c) mixing potassium dihydrogen phosphate with other trace elements, drying the mixture at 26-32 degrees C and heating rate of 5 degrees C/minute and maintaining a moisture content of 3-5%.    USE - The method is useful for production of enhanced fertilizer (claimed).    ADVANTAGE - The method lowers production cost and discharges no environmental waste.    DETAILED DESCRIPTION - Production of enhanced fertilizer, involves (a) mixing phosphoric acid with carbamide in a molar ratio of (1.2-1.4):1 in a reaction vessel, heating the mixture at heating rate of 4 degrees C per minute until the temperature is 120-150 degrees C, stirring the mixture for 130-150 minutes, cooling the mixture to 30-40 degrees C and centrifuging the mixture to obtain intermediate, (b) preparing potassium dihydrogen phosphate by reacting the intermediate with a basic potassium salt in a molar ratio of 1:(1.2-1.4) in a reaction vessel, stirring at 220-260 revolutions per minute for 50-70 minutes, regulating the pH of the mixture to be 9-10, obtaining slurry containing nitrogen, phosphorus and potash (NPK), cooling the slurry, crystallizing and filtering to obtain potassium dihydrogen phosphate, where the nitrogen content of the filtrate is 9-11%, phosphorus content of the filtrate 2.6-2.8% and the potassium content of filtrate is 5-6%, and (c) mixing potassium dihydrogen phosphate with other trace elements, drying the mixture at 26-32 degrees C and heating rate of 5 degrees C/minute for 40-60 minutes, and maintaining a moisture content of 3-5%.
NOVELTY - Production of carbon based fertilizer, involves (a) crushing wheat straw after drying, mixing and incinerating the mixture, (b) sieving and biologically treating the incinerated ash, (c) mixing 40-50 pts. incinerated ash, 15-18 pts. ammonium sulfate, 9-12 pts. urea, 6-8 pts. potassium sulfate, 1-2 pts. monoammonium phosphate, 9-13 pts. bentonite and 1-3 pts. binder with stirring, and (d) granulating the mixture.    USE - The method is useful for production of carbon based fertilizer (claimed).    ADVANTAGE - The method prevents the pollution caused by straw incineration.
NOVELTY - An oil sludge pyrolysis device comprises oil sludge heat transfer heat carrier (3), pyrolysis chamber (24) having close-open flashboard (4) in bottom or side wall, pyrolysis reactor (1) which is set with heat chamber which is connected to 1st oil sludge inlet (6), pyrolysis gas outlet (7) which is used for discharging pyrolysis gas, 2nd oil sludge inlet (8) of heat carrier which is connected to pyrolysis gas outlet and pyrolysis chamber, and filter element (5) which is provided below flashboard in which area of filter element is smaller than cross-sectional area of heat carrier upper screen.    USE - An oil sludge pyrolysis device (claimed).    ADVANTAGE - The device is efficient, and solves coking problem.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of oil sludge pyrolysis device.    Pyrolysis reactor (1)    Heat transfer heat carrier (3)    Close-open flashboard (4)    Filter element (5)    1st oil sludge inlet (6)    Pyrolysis gas outlet (7)    2nd oil sludge inlet (8)    Pyrolysis chamber (24)
NOVELTY - A d-delta-tocopherol purifying method involves mixing d-delta-tocopherol concentrate liquid with non-polar or low polar solvent. The mixture is heated and transferred into silicon glue column. The heated solution is completely absorbed by a silicon glue column. Elution is carried out on the absorbed solution, followed by transferring the eluted concentrate liquid into alkaline anion exchange resin column to carry out ion exchange absorbing process by utilizing carbon dioxide to obtain purified d-delta-tocopherol.    USE - Method for purifying d-delta-tocopherol.    ADVANTAGE - The method enables purifying the d-delta-tocopherol with high yield and low energy consumption.    DETAILED DESCRIPTION - A d-delta-tocopherol purifying method involves mixing d-delta-tocopherol concentrate liquid with non-polar or low polar solvent at ratio of 1:1-2 (m/v). The mixture is heated and transferred into silicon glue column that is filled with 10-45 mass% silicon glue. The heated solution is completely absorbed by a silicon glue column. Elution is carried out on the absorbed solution by adding 3-5 mass% non-polar or low polar solvent to remove polar solvent, followed by transferring the eluted concentrate liquid into alkaline anion exchange resin column to carry out ion exchange absorbing process by utilizing carbon dioxide to obtain purified d-delta-tocopherol.
NOVELTY - Method for promoting production of acid using residual sewage sludge, involves (a) adding residual sewage sludge into digestion flask, and adding alkyl glucosides and iron into the flask, and (b) maintaining the flask under oxygen-nitrogen atmosphere, sealing the flask after 1 minute, placing the flask in shaker, and subjecting to anaerobic fermentation.    USE - The method is useful for promoting production of acid using residual sewage sludge (claimed). The acid is short-chain fatty acids.    ADVANTAGE - The method is environmentally-friendly and recycles sewage sludge.
NOVELTY - Method for preparing carotenoids using food organic wastewater, involves (a) adjusting pH of food organic wastewater to 6.5-8, and adding 360 mg Rhodobacter sphaeroides and plant growth promoting rhizobacteria (logarithmic phase) to 1 l food organic wastewater, (b) micro-processing the mixture of step (a) at light intensity of 500-3000 lux, and temperature of 25-30 degrees C for 72-96 hours under aerobic conditions, and (c) extracting carotenoids. The concentration of the R.sphaeroides is 6.2-7x 108 colony-forming unit (cfu)/ml.    USE - The method is useful for preparing carotenoids using food organic wastewater (claimed).    ADVANTAGE - The method prepares carotenoid with yield of more than 25% and COD removing rate of more than 78%.    DETAILED DESCRIPTION - Method for preparing carotenoids using food organic wastewater, involves (a) adjusting pH of food organic wastewater to 6.5-8, and adding 360 mg Rhodobacter sphaeroides and plant growth promoting rhizobacteria (logarithmic phase) to 1 l food organic wastewater, (b) micro-processing the mixture of step (a) at light intensity of 500-3000 lux, and temperature of 25-30 degrees C for 72-96 hours under aerobic conditions, and (c) extracting carotenoids. The concentration of the R.sphaeroides is 6.2-7x 108 colony-forming unit (cfu)/ml. The plant growth promoting rhizobacteria is Bacillus cereus. The concentration of the B.cereus is 1.4-27x 107 cfu/ml. In step (b), the dissolved oxygen concentration is 0.5-1 mg/l.
NOVELTY - A one inside and outside double-circulation anaerobic reactor is set outside a cylinder in a bottom plate, outside cylinder lower end right side wall is set a water inlet pipe, the bottom of outside cylinder is set emptying pipe, outside cylinder inner part is a supporting plate, a supporting plate is extended outside the top part end part of three phase separator, three phase separator lower end outside cylinder inner wall is a sludge guide plate, a lower guide plate sludge outside barrel side wall is set a mud discharge pipe, three phase separator outside cylinder inner wall along the circumferential groove, water groove is set at one side of the water pipe, the waste water is set outside circulation pipe, outside the top end outside three phase separator is a gas-liquid separator, a gas-liquid separator end is a marsh gas outlet pipe, the side wall gas reflux tube, liquid return tube is set at the bottom, supporting frame in a bottom plate of inner cylinder, a supporting frame is set outside inner cylinder, outside cylinder side upper wall is extended to inner cylinder mounted with inner gas distributor of biogas backflow main pipe. Waste water form inner circulation, increasing the waste water in outside cylinder inner of residence time, increase of this utility new type processing efficiency of waste water in inner and outside cylinder.
NOVELTY - Method for extracting biofuel raw material involves mixing 0.1-20 wt.% microalgae and 80-99.9 wt.% water, forming a mixture, irradiating the mixture with radiation of 50-100000 kGy to remove cell wall of microalgae, crushing resultant product, and stirring with a mechanical stirrer at speed of 50-3000 rpm for 10-60 minutes.    USE - Method for extracting biofuel raw material (claimed).    ADVANTAGE - The method enables extraction of biofuel raw material with reduced energy consumption.
NOVELTY - Polymer embedded hydrophobic anti-tumor medicine nano-composite microsphere preparation involves taking hydrophobic anti-tumor medicine in a magnetic stirrer. Acrylic ester monomer is added in the magnetic stirrer to dissolve medicine. Initiator and additives are added to the obtained material, and then mixed uniformly. Oil phase comprises component A, emulsifying agent and deionized water. Aqueous phase comprises component B. Oil phase is added slowly to the aqueous phase at room temperature, and then stirred for 0.5 hours.    USE - Method for preparing polymer embedded hydrophobic anti-tumor medicine nano-composite microsphere (claimed) used for preparing medicine.    ADVANTAGE - The method is environment-friendly, and enables to prepare the product that is distributed uniformly, and has improved drug loading and entrapment efficiency.    DETAILED DESCRIPTION - Polymer embedded hydrophobic anti-tumor medicine nano-composite microsphere preparation involves taking hydrophobic anti-tumor medicine in a magnetic stirrer. Acrylic ester monomer is added in the magnetic stirrer to dissolve medicine. Initiator and additives are added to the obtained material, and then mixed uniformly. Oil phase comprises component A, emulsifying agent and deionized water. Aqueous phase comprises component B. Oil phase is added slowly to the aqueous phase at room temperature, and then stirred for 0.5 hours. The obtained mixture is emulsified under ultrasonic wave in an ice water bath for 15 minutes to form thin liquid. The obtained thin liquid is reacted under nitrogen gas at 60-80 degrees C for 6 hours to obtain the desired product, where the grain diameter of polymer embedded hydrophobic antineoplastic drug nano-composite microsphere is 80 nu m.
NOVELTY - Odontella BS-003 strain (I) having a preservation number of KCTC 12401BP is new.    USE - (I) is useful for preparing: a lipophilicity extract, which is useful in a cosmetic composition; fatty acid methyl ester, which is useful in a food composition (all claimed); and biodiesel.    ADVANTAGE - (I) prepares large amount of the fatty acid methyl ester with purity of more than 95%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing a lipophilicity extract comprising cultivating (I) and then extracting lipid, using an organic solvent, from (I); and    (2) preparing fatty acid methyl ester comprising (1) cultivating (I), (2) adding a methylation reagent to the cultivated (I) and then reacting, and (3)adding a saponification reagent and an extraction reagent to the mixture.
NOVELTY - Preparation of nickel-iron bimetallic methanation catalyst involves adding dilute acid solution to boehmite powder, mixing, extruding, drying, calcining, obtaining alumina support, impregnating resultant material with 0.7-1 ml salt solution containing additive, leaving still for 5-30 minutes, drying, calcining, obtaining additive-containing carrier, impregnating resultant carrier with 0.7-1 ml nickel salt solution, leaving still, drying, obtaining nickel-containing carrier, impregnating resultant carrier with 0.7-1 ml iron salt solution, leaving still, drying and calcining.    USE - Preparation of nickel-iron bimetallic methanation catalyst (claimed).    ADVANTAGE - The method enables economical preparation of nickel-iron bimetallic methanation catalyst having high activity, stability and selectivity.    DETAILED DESCRIPTION - Preparation of nickel-iron bimetallic methanation catalyst involves adding dilute acid solution to boehmite powder, mixing, extruding, drying, calcining at 400-700 degrees C for 2-5 hours, obtaining alumina support, impregnating resultant material with 0.7-1 ml soluble salt solution (A) containing additive, leaving still for 5-30 minutes, drying at 80-120 degrees C for 10-60 minutes, calcining at 400-700 degrees C for 2-5 hours, obtaining additive-containing carrier, impregnating resultant carrier with 0.7-1 ml nickel salt solution, leaving still for 5-30 minutes, drying at 80-120 degrees C for 10-60 minutes, obtaining nickel-containing carrier, impregnating resultant carrier with 0.7-1 ml iron salt solution, leaving still for 5-30 minutes, drying at 80-120 degrees C for 10-60 minutes and calcining at 400-700 degrees C for 2-5 hours. The additive is chosen from lanthanum, cerium, magnesium and barium. The usage amount of additive is 0.01-5 wt.%.
NOVELTY - A biodiesel and diesel oil blending device, comprises a body portion coated with a heat-insulating layer, a support frame, a fuel level measuring unit inside the body portion, a coil-formed fuel heater coating the outside of the body portion, and an agitating mixer comprising an agitating axis and stirring arms.    USE - A biodiesel and diesel oil blending device.    ADVANTAGE - The biodiesel and diesel oil blending device is highly suitable for agitating fuel blends having a high viscosity and for generating blends having technical criteria equivalent to those of diesel oil for used in engine, in particular in a marine boiler.
NOVELTY - Increasing production of yeast lipid, comprises (a) pre-processing cheese whey by alkali treatment or physical treatment, and (b) culturing yeast by using the pre-processed cheese whey. The alkali treatment is carried out by adding alkaline material having pH of 8-13 into the cheese whey. The physical treatment is carried out by applying pressure using hydrodynamic cavitation.    USE - The lipid is useful for producing biofuel (claimed).    ADVANTAGE - The biofuel production method produces biofuel in bulk amount, and processes waste water of cheese whey.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing biofuel, comprising (a), (b), (iii) extracting lipid from yeast, and (iv) converting lipid into biofuel.
NOVELTY - Production of biodiesel from oilseeds, involves removing dust and foreign particles from seeds, drying seeds in sunlight, extracting oil from seeds using screw-press expeller, collecting extracted oil and oil residue, storing extracted oil in storage tank for sedimentation, filtrating extracted oil using filter press and different pore size filters, carrying out pretreatment of oil to reduce free fatty acids and degumming, and carrying out transesterification of refined oil using homogeneous catalyst followed by microwave-oven heating to convert remaining glyceride into esters.    USE - Production of biodiesel (claimed).    ADVANTAGE - The method enables simple and economical production of biodiesel having high quality with high yield, using biodiesel unit which is easy to operate, and reduces the carbon emission produced from combustion of fuel.    DETAILED DESCRIPTION - Production of biodiesel from oilseeds, involves removing dust and foreign particles from seeds, drying seeds in sunlight, extracting oil from seeds by screw-press expeller, collecting extracted oil and oil residue (de-oiled cake), storing extracted oil in storage tank for sedimentation, filtrating extracted oil by filter press and different pore size filters, carrying out pretreatment of oil to reduce free fatty acids and degumming, carrying out trans-esterification of refined oil using homogeneous catalyst followed by microwave-oven heating to convert remaining glyceride into esters, separating biodiesel, excess methanol and glycerol, washing and drying biodiesel.
NOVELTY - Tetraselmis species MBEyh01L strain (I) having a preservation number of KCTC: 12429BP, is new.    USE - (I) is useful in a composition for producing biodiesel (all claimed).    ADVANTAGE - (I) produces the biodiesel under various environment conditions with less energy consumption, and has low-temperature growth capability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing biodiesel comprising culturing (I) in a culture medium, and adding catalyst to fatty acid glycerol and then converting into fatty acid ester using strain to obtain biodiesel.
NOVELTY - A Tetraselmis sp. MBEyh02L strain (KCTC 12430BP), is new.    USE - The Tetraselmis sp. MBEyh02L is useful in composition for producing biodiesel (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of producing the biodiesel, which involves inoculating Tetraselmis strain into culture medium, adding catalyst, culturing the strain under optical irradiation and converting fatty acid glycerol existing within the strain into fatty acid ester.
NOVELTY - Tetraselmis sp. MBEyh03Gc strain (KCTC 12431BP), is new.    USE - The strain is useful in composition for producing bio-diesel (claimed).    ADVANTAGE - The strain can be cultured in low temperature, various temperature conditions, and has excellent environmental adaptability and improves lipid productivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (I)composition for producing bio-diesel comprising the Tetraselmis sp. strain; and #(II)producing bio-diesel, comprising (a) introducing the strain on culture medium, and culturing the strain under light irradiation, and (b) adding catalyst into the strain, and converting fatty acid ester by fatty acid glycerol present in the strain.
NOVELTY - A solid acid catalyst is prepared by adding sulfuryl halide to biochar derived from microalgae, and plasticizing.    USE - Solid acid catalyst is used for manufacturing biodiesel (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of solid acid catalyst; and    (2) manufacture of biodiesel.
NOVELTY - Method of producing alcohol involves (a) crushing food waste, and removing impurities, (b) dewatering the crushed mixture, (c) subjecting the resulting mixture to saccharification process, (d) carrying out anaerobic fermentation of saccharified mixture using fermentation yeast, (e) subjecting the resulting fermentation product to azeotropic distillation, (f) extracting the resulting distillate using e.g. ethanol and diethyl ether, and (g) performing membrane separation and adsorption of obtained extract and removing water to obtain product.    USE - The method is useful for producing alcohol from food waste (claimed).    DETAILED DESCRIPTION - Method of producing alcohol involves (a) crushing food waste comprising wood carvings, animal shell and glass piece, and removing impurities, (b) dewatering the crushed mixture, (c) subjecting the resulting mixture to saccharification process, (d) carrying out anaerobic fermentation of saccharified mixture using fermentation yeast at 25-40 degrees C to obtain liquified food waste having pH of 4-5, (e) subjecting the resulting fermentation product to azeotropic distillation, (f) extracting the resulting distillate using ethanol, benzene, cyclohexane, and diethyl ether, and (g) performing membrane separation and adsorption of obtained extract and removing water to obtain product.
NOVELTY - An endoglucanase I variant comprising a sequence: (i) having at least 96% identity to the full length amino acid sequence set forth in SEQ ID NO: 3; and (ii) comprising at least one substitution at position corresponding to residue Glu117, Asp241, Thr7 or Met91 of SEQ ID NO: 3, where the variant exhibits an improved cellulase and/or xylanase activity compared to Trichoderma reesei endoglucanase I of SEQ ID NO: 2, is new. Sequences not defined here may be defined at ftp://ftp.wipo.int/pub/published_pct_sequences/publication.    USE - The endoglucanase I variant is useful for converting cellulosic biomass to monomeric sugars; and for producing fermentation product from cellulosic biomass (all claimed). It can also be used for simultaneous degradation of cellulosic biomass into monomeric sugars and fermentation of the sugars, for example to produce ethanol.    ADVANTAGE - The variant exhibits improved cellulase and/or xylanase activity compared to Trichoderma reesei endoglucanase I (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a nucleic acid encoding the variant;    (2) an expression cassette or vector comprising the nucleic acid;    (3) a host cell comprising the nucleic acid or the expression cassette or vector;    (4) a method of producing endoglucanase I variant;    (5) a method of converting cellulosic biomass to monomeric sugars comprising contacting the biomass with the endoglucanase I variant or the host cell; and    (6) a method of producing a fermentation product from cellulosic biomass comprising: (a) contacting the biomass with the endoglucanase I variant or the host cell, thus degrading the biomass into monomeric sugars; and (b) fermenting monomeric sugars obtained in step (a) into the fermentation product.
NOVELTY - The processing method involves dewatering the sludge to water content of less than 50% via a sludge dewatering unit (1). The dehydrated sludge is mixed with coal powder in predetermined proportion in a coal preparation unit (2). The coal gas is fed into the furnace (3), and drying and carbonization are performed to produce dry distillation coal and semi coking type coal. The semi coking type coal is introduced in high temperature for pyrolysis gasification. The burned semi coking type coal is converted into inorganic matter and ash form discharged from the discharging line on furnace bottom.    USE - Two-stage sludge gas chemical processing method using sludge gas treatment device (claimed).    ADVANTAGE - Harmful heavy metals present in the sludge are easily broken down into the molten ash and cured, thus, safe handling requirement is satisfied.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a two-stage sludge gas treatment device.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of the two-stage sludge gas chemical processing method. (Drawing includes non-English language text).    Sludge dewatering unit (1)    Coal preparation unit (2)    Two-stage gas furnace (3)    Purification unit (6)    Drying layer (31)
NOVELTY - The furnace has a furnace main body provided with a lower tube, two middle part tapered tubes, an upper tube and an end enclosure (5) that are connected with each other by a seal connection. A periphery of the lower tube is provided with a refractory lining. The lower tube is provided with a bottom liquid end, a fire plasma torch nozzle and an ignition oil gun entrance. Each middle part taper tube is formed as a high cone-shaped structure. The end enclosure is provided with a multi-pengshui chilling unit (12), an air outlet end (13) and a material position part (14).    USE - Biomass gasification furnace.    ADVANTAGE - The furnace has high gasification temperature, high reaction speed, better fuel adaptability and high heating efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of a biomass gasification furnace.    End enclosure (5)    Multi-pengshui chilling unit (12)    Air outlet end (13)    Material position part (14)
NOVELTY - Synthesizing a multi-functional salicyl imidazoline amide additive (I) is claimed.    USE - The process is useful for synthesizing (I), which is useful in biodiesel (all claimed).    ADVANTAGE - (I) enhances the oxidization resistance and corrosion resistance and lowers the concentration temperature for the biodiesel.    DETAILED DESCRIPTION - Synthesizing a multi-functional salicyl imidazoline amide additive of formula (I) is claimed. N.B. the structure is not present in the specification. An INDEPENDENT CLAIM is included for enhancing the oxidization resistance and corrosion resistance and lowering the concentration temperature of the biodiesel comprising adding 10 parts per million to 0.01 wt.% of (I) to the biodiesel.
NOVELTY - Algae based slow release urease inhibitor preparation involves obtaining iron (III) salt solution modified algae adsorbent and urease inhibitor, where the urease inhibitor is N-(n-butyl)thiophosphoric triamide, and the concentration of the urease inhibitor is 1.1-2%.    USE - Method for preparing algae based slow release urease inhibitor (claimed).    ADVANTAGE - The method is simple, easy to control, and enables to produce algae based slow release urease inhibitor that is eco-friendly and has reduced loss of N-(n-butyl)thiophosphoric triamide.
NOVELTY - Alcohol-blended fuel is prepared by distilling fuel according to national and international standards at different temperature fractions, splitting into multiple fractions, and adding 1 or 2 lubricants to alcohol-containing fuel fractions.    USE - Preparation of alcohol-blended fuels for vehicles (claimed).    ADVANTAGE - Process enhances fuel performance. Fuel avoids air resistance, reduces starting temperature of engine, improves quality of engine operation, and has high quality.
NOVELTY - A silicon carbide-based synthesis gas methanation catalyst comprises 40-95 pts. wt. beta -silicon carbide honeycomb carrier and 5-40 pts. wt. nickel.    USE - Silicon carbide-based synthesis gas methanation catalyst.    ADVANTAGE - The catalyst has good heat conductivity, high machinery strength, low pressure and long service life, and is suitable under high temperature high air speed condition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of silicon carbide-based synthesis gas methanation catalyst comprising mixing 70 pts. wt. silicon powder, 30 pts. wt. carbon black, 0-5 pts. wt. binder and 1-10 pts. wt. pore-forming agent to obtain dry powder mixture, adding 5-80 pts. wt. water-soluble resin, 1-10 pts. wt. lubricant, 0-5 pts. wt. surfactant, 0-5 pts. wt. plasticizer and 0-80 pts. wt. deionized water, stirring to obtain liquid mixture, kneading for 0.5-2 hours, mixing in pug mill for 0.5-3 hours to obtain mud, extruding under extrusion pressure of l-16 MPa to form cellular biscuit, cutting, drying at room temperature for 4-10 hours and at 60-150 degrees C for 4-24 hours, sintering at 1200-1500 degrees C for 0.5-4 hours under normal pressure with 1-10% of the hydrogen mixed gas at flow rate of 50-500 mL/minute, heating and cooling rate of 0.5-5 degrees C/minute, calcining at 500-900 degrees C for 1-8 hours under air atmosphere to obtain silicon carbide honeycomb substrate, preparing aqueous solution or ethanol-soluble nickel salt solution as dipping solution by optionally adding additives, oxidizing silicon carbide honeycomb substrate in dipping solution for 0.5-4 hours, purging suspended solution, drying at 60-150 degrees C for 1-10 hours, and calcining at 400-800 degrees C for 1-6 hours.
NOVELTY - Celecoxib preparation involves adding ethyl trifluoroacetate and sodium alcohol in an organic solvent, and then adding acetophenone at 40-50 degrees C. The resulting mixture stirred at room temperature after adding petroleum ether to crystallize to obtain an intermediate. The organic solvent is selected from tetrahydrofuran, ethanol or isopropanol. The sodium alcohol is sodium methoxide or sodium ethoxide.    USE - Method for preparing celecoxib (claimed).    ADVANTAGE - The method prepares celecoxib reaction in simple, cost-effective and eco-friendly manner under mild reaction condition with high yield and high purity. The prepares celecoxib has wide market prospect and economic benefit.    DETAILED DESCRIPTION - Celecoxib preparation involves adding ethyl trifluoroacetate and sodium alcohol in an organic solvent, and then adding acetophenone at 40-50 degrees C. The resulting mixture stirred at room temperature after adding petroleum ether to crystallize to obtain an intermediate. The organic solvent is selected from tetrahydrofuran, ethanol or isopropanol. The sodium alcohol is sodium methoxide or sodium ethoxide. The obtained intermediate, ethyl acetate, isopropyl alcohol, hydrochloric acid and 4-hydrazino-benzenesulfonamide hydrochloride are mixed at 50-80 degrees C for 1-2 hours. The reaction mixture is cooled to room temperature and crystallized to obtain a crude product, which is dissolved in ethanol by heating. Active carbon is added at 10-30 degrees C and then water is also added to crystallize, where the resulting product is filtered as the finished product.
NOVELTY - Preparing (1S,2S,5S)-2-(2-amino-6-benzyloxy-purin-9-yl)-1,5-bis-hydroxymethyl-cyclopentanol compound (I) comprises ring-opening reacting ((1R,2S)-2-(hydroxymethyl)-6-oxabicyclo(3.1.0)hexan-1-yl)methanol compound (II) with 6-Benzyloxy-9H-purin-2-ylamine compound (III) in the presence of non-proton organic solvent.    USE - The method is useful for preparing (I).    ADVANTAGE - The method is capable of simply and economically preparing (I) with easily available raw material and high product yield under mild reaction condition in an eco-friendly manner.    DETAILED DESCRIPTION - Preparing (1S,2S,5S)-2-(2-amino-6-benzyloxy-purin-9-yl)-1,5-bis-hydroxymethyl-cyclopentanol compound of formula (I) comprises ring-opening reacting ((1R,2S)-2-(hydroxymethyl)-6-oxabicyclo(3.1.0)hexan-1-yl)methanol compound of formula (II) with 6-Benzyloxy-9H-purin-2-ylamine compound of formula (III) in the presence of non-proton organic solvent.    R2 = monovalent group of formula (Ia);    R21 = pyridyl or 6-10C-aryl (both optionally substituted by 1-3C-alkyl, halo or 1-3C-alkoxy);    Y1 = optionally substituted 3-9 membered ring to connected with Si bond to form a optionally substituted 4-10-membered carbocyclic ring, or Y1 is optionally substituted 3-9 membered ring to connected with heteroatoms comprising Si, O, S or N to form a optionally saturated 4-10-membered ring or 1-3C-alkyl;    P2 = Ethyl-benzene compound of formula (Ib), But-1-yne compound of formula (Ic), 1-6C-alkoxy, 1-6C-alkyl, trimethyl or ethoxymethyl;    R4, R5 = linear or branched 1-6C-alkyl, H, halo or nitro;    R6 = H or linear or branched 1-6C-alkoxy; and    X = 1-6C-linear or branched alkyl or halo.
NOVELTY - This utility new type provide a one synthesis ammonia technology cold in a use system, including for mixed gas mixed room and a low temperature nitrogen, a mixed room air inlet end of a connection tube and process gas outlet end of gas pipeline, heat exchanger, air inlet end of the heat exchanger and nitrogen pipeline connecting the outlet end of the mixed room in turn and a shell, a methanation heat exchanger regulator, sulphur groove, in a furnace, outlet end of the methanation furnace in turn and a pass of the methanation heat exchanger, pneuma water cooler, an air outlet end of the refined pneuma water cooler and the heat exchanger shell side air inlet end is a, the heat exchanger shell pass outlet end in turn and separator, a compressor, a sieve, synthesis tower connection. The cold quantity of low temperature nitrogen changing in a hot process is taking a use pneuma, increase temperature and nitrogen for reaction of methanation. At the same time greatly reduces process temperature pneuma, increase load of compressor, for reducing water damage of compressor and catalyst.
NOVELTY - This utility new type relates to one a small biomass waste gasification generating device, comprising housing, the housing upper end set with receiving material wherein, receiving material and wherein adjacent set with motor, motor and first-stage feeder is connected below the first-stage feeding machine set with drying cavity, the inner cavity is set with a level drying machine, drying chamber of the lower part set with high temperature thermal decomposition plate, high temperature thermal decomposition plate through pipeline and filter, the filter through heat exchanger and internal combustion engine. This utility new type design is reasonable, use is convenient, through this a generating device, not only can high power generation efficiency, which can use biomass waste, increase biomass waste use rate, and generating a device miniaturized and integrated design, which is good for popularization and application.
NOVELTY - The domestic sewage purification biogas pool has a pre-processing area and a post-processing area that are divided into a specific level. A cylindrical marsh gas pool of base is designed. The sludge is deposited in the pool bottom. A rectangular baffled biological filter pool is formed.    USE - Domestic sewage purification biogas pool.    ADVANTAGE - The marsh gas pool recovery rate is high.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the Domestic sewage purification biogas pool. (Drawing includes non-English language text)
NOVELTY - Method of obtaining biodiesel fuel includes preparation of vegetable oil with heating to temperature 80 degrees C, carrying out alkaline ethanolysis by means of potassium hydroxide with obtaining ether-glycerol mixture, which is separated with obtaining two fractions of glycerol and mixture of ethers, mixture of ethers is subjected to filtration, sorption purification and dehydration, obtained biodiesel fuel is stored. Filtration, sorption purification and dehydration are performed in two stages, at the first stage mixture of ethers is placed into centrifuge, rotated at angular velocity 0.5-0.7 rev/min for 0.5-0.6 hour, with mixture being separated into light and heavy fractions, heavy fraction is drained, at the second stage light fraction is placed into another centrifuge, charge, consisting in wt % of carbon nanomaterial "Taunit" - 1-1.5% and natural bentonite material - the remaining part, is added into it with volume ratio 1:10, centrifuge is rotated at angular velocity 1.1-1.3 rev/min for 1.0-1.2 hour, with removal of heavy fraction remains.    USE - Chemistry.    ADVANTAGE - Application of two-stage filtration of mixture of ethers with charge makes it possible to increase quality of biodiesel fuel, output, prolong resource of engine operation with reduction of harmful emissions into atmosphere and economical consumption of fuel resources.1 ex
NOVELTY - A tail gas treating method involves utilizing a processing system including an interconnected primary fermentation tank, an interconnected secondary fermentation tank, and a treatment pond that is connected at an end of the primary and secondary tank. 1-2% liquid methane is passed into the fermentation tanks and the treatment pond to produce biogas. The obtained gas is treated in the pond.    USE - Method for treating a tail gas.    ADVANTAGE - The method enables treating the tail gas in a simple and economical manner with high recovery rate.
NOVELTY - This utility new type claims a one pig farm waste water recovery sedimentation filter device, belonging to the aquaculture waste treatment field, the device comprising primary settling sedimentation pool, fertilizer regulating pool, a material pump, water pump, pH monitoring device, pH neutralizing device and medicine-adding device, primary settling pool is primary-secondary pool structure, comprising subloop, , a sub-pool solid-liquid mixture feeding and discharging port, the material pump, the set up with a liquid outlet, through water pump and sedimentation pool is connected in sedimentation pool set with a pH monitoring device and pH neutralizing device, a sedimentation pool through water pump and the regulating pool is connected with the fertilizer in the fertilizer regulating pool set with medicine adding device, the utility model is new type primary-secondary pool principle the precipitate by a solid-liquid separate processing, using and absorbing, and biological fermentation filter self-purification, the pig of the high concentration waste liquid proceed fast purification is discharged, and organic fertilizer, at the same time, process is simple, the cost is low, solving the problem of valid scale environment and pig waste liquid pollution.
NOVELTY - This utility new type claims a methanol water reforming one generating a refrigerator, said refrigerator system comprising: a hydrogen generating device, a, preparing hydrogen through a water methanol reforming hydrogen preparation to obtain a hydrogen supply to the electricity generating device to generate electricity, sending electric energy for a refrigerator device operation, a refrigerator device is a movable refrigerator device. This utility new type claims a methanol water reforming generating refrigerator system, it does not need extra power source can be a refrigerator system, there is no convenient power source of outdoor use.
NOVELTY - This utility new type claims a new-type one livestock manure anaerobic fermentation system, comprising material pool, a fermentation tank, a gas outlet pipe, electric generator and marsh liquid pool, a material pool mounting with a packing auger and a packing auger to a fermentation tank, fermentation tank inner set with baffled stirrer, fermentation tank rear end a material discharging tank, a material discharging tank connect solid-liquid separate machine, solid-liquid separate machine set with solid discharging pipe and liquid discharging pipe, a liquid discharging pipe a marsh liquid pool, end and water return end of a pipe connecting a circulation water generator, a circulation water in pipe section through a heat exchanger and a fermentation tank, a circulation hot water pipe set with circulation water pump and heating disk pipe. This utility new type technology compared with the existing of the advantages is: using this utility new type of fermenting system, continuously feeding, discharging, high corrosion, PH neutral and stability, efficient organic fertilizer raw material, organic fertilizer processing technology can continuously supply raw material, at the same time it can continuous uninterrupted gas, and collecting.
NOVELTY - An alpha-quaternary carbon alpha,beta-diamine acid derivative with threo and erythro conformation (I) and (II), is new.    USE - New alpha-quaternary carbon alpha,beta-diamine acid derivative is useful for drug screening, and in pharmaceuticals.    ADVANTAGE - The alpha-quaternary carbon alpha,beta-diamine acid derivative is economically prepared with high yield, under mild reaction conditions, by simple and environmentally-friendly method.    DETAILED DESCRIPTION - An alpha-quaternary carbon alpha,beta-diamine acid derivative with threo and erythro conformation of formula (I) and (II), is new.    Ar1-Ar3=optionally substituted phenyl group;and    R=p-toluenesulfonyl or nitrobenzenesulfonyl.    An INDEPENDENT CLAIM is included for preparation of alpha-quaternary carbon alpha,beta-diamine acid derivative with threo and erythro conformation (I) and (II).
NOVELTY - Methanol alternative fuel comprises gasoline, methanol, n-hexane, acetone, chloroform, solubilizing agent, oxidation anticoagulant, and corrosion expansion inhibitor.    USE - Used as methanol alternative fuel.    ADVANTAGE - The fuel reduces emission of pollutants e.g. hydrocarbons, carbon monoxide and nitrogen oxides (NOx) and so is environmentally friendly, has high octane number, and improves acceleration of vehicle.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing methanol alternative fuel, comprising mixing gasoline, methanol, n-hexane, acetone, chloroform, solubilizing agent, oxidation anticoagulant and corrosion expansion inhibitor.
NOVELTY - The method involves performing micro and macro flake formation by a multistage controllable flocculation device before performing a two-stage flocculation formation. Controllable two-stage flocculation shear-stable flakes are produced by revolution processes. An inlet of a membrane plant is diluted according to separation stage.    USE - Two-stage separation method for extensively depleting a fermenting residue or a liquid manure from a biological gas facility.    ADVANTAGE - The method enables obtaining quality ingredients from the fermenting residue or the liquid manure, and processing a filtrate without farther treatment in a membrane plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a two-stage separation method for extensively depleting a fermenting residue from a biological gas facility.'(Drawing includes non-English language text)'    Separation machines (1, 12)    Volumetric flow (2)    Depleted phase (3)    Flocculant (8)    Directed structure of macro flocculation (10)
NOVELTY - Synthesizing an electrode additive for a fuel cell, comprises (a) dissolving at least one metal salt in ethylene glycol to generate a metal salt solution, (b) dispersing carbon in the generated metal salt solution to obtain a suspension of carbon and metal salt, (c) heating the suspension of carbon and metal salt, and cooling, (d) filtering, cleaning and drying the metal powder supported on carbon, and (e) heat treating metal powder supported on carbon at 300-1000 degrees C by supplying water vapor to obtain metal oxide powder supported on carbon.    USE - The method is useful for synthesizing an electrode additive for anode of a fuel cell (all claimed).    ADVANTAGE - The electrode additive improves synthesis of oxygen generating catalyst, and prevents oxidation of carbon.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) an anode comprising metal oxide powder supported on carbon arranged on a carrier; and    (2) electrode additive produced using the above method.
NOVELTY - This utility model claims a fertilizer tail pneuma dust-removing device, comprising a shell of the internal space, a plurality of swirl nozzle; the water curtain dust remover outlet inside the shell set with water curtain dirt catcher and distribute in the water screen duster periphery is connected to a raw material pipeline, the shell comprise outside wall, inner wall and by this outside wall and inner wall defining a upper cavity, the outside wall can be set with this cavity and connected a entrance and exit, the outside wall is heat-insulating layer, the inner wall is heat-conducting layer, molasses alcohol fermentation liquid connected to the entrance, the heat energy of high temperature gas from the outlet, a guide tube to a water curtain dust-removing of sprinkle liquid device. This new utility model saves energy, reasonable design, and it is easy to popularize.
NOVELTY - This new type utility claims one a horizontal spiral stirring straw compost happen device, set with fermentation jar, stir system, air blower and discharge system, wherein the fermentation jar fixed mounted in a machine frame, a stir system comprising packing auger shaft and drive the packing auger shaft positive rotation and reversing a drive motor, a transverse horizontal auger set in the fermentation jar inner, and the packing auger shaft upper left and right two side of blade structure symmetrically, the bottom of the ferment jar is arc-shaped, the fermentation jar bottom inner set with separating plate, said separating plate set with a ventilation or penetrate water is used for through hole, the fermentation jar is stop cavity is set below the water tank, the water tank bottom end is set with water outlet, the air blower through gas pipeline and the water tank is connected. This utility new type happen device a for a uniform, fully stir is of compost fermentation material, and a stable operation to save space and reduces the operation cost.
NOVELTY - This utility model provides a stirring pedestal device of stirring system of biogas fermentation reactor, comprising pedestal, a base, a pressing cover, an outer cover and stir shaft, the bearing base through bolt fixed at a pedestal, a base and gland bush through a bolt, inner bearing base is provided with a filled and yellow oil, bearing inner ring and stir shaft head tightly matching, and stir shaft between the inner pressing cover is provided with two channel seal ring, a pressing cover and outer cover through a labyrinth, stir shaft and inner ring matching the outer cover, the outer cover and stir shaft through screw connection. This utility model is beneficial effect is: the seal effect is good, the dust protecting protecting sand grain, a long-term normal rotating stir work inner in biogas fermentation reactor.
NOVELTY - This new utility model claims of one use of power generation device of biomass of microorganism decomposing sewage, mainly composed of by power generation system, biological compost system, microorganism decomposing and settling pool, the power generation system connected with the air outlet and microorganism decomposing pool, a sludge outlet of the microorganism decomposing pool connected with biological compost system, entrance of the power generation system and the settling pool connected with microorganism decomposing comprises gas pre-processing system and fuel gas power generation unit, fuel gas power generation unit connected with the gas pre-processing system, air inlet gas pre-processing system is connected with the air outlet and microorganism decomposing pool, biological compost system comprises fermentation room, thin channel, fertile chamber, for containing object and organic waste water by Anaerobic fermentation, the product containing methane gas to the utmost extent, used for marsh gas power generation, and for the production of sludge carry out compost treatment, manufacture nutrition and good organic fertile, using clean energy to the utmost extent, the reasonable resource again using, saves resource, avoids resource waste.
NOVELTY - Fermentation process device is one a town sewage treatment plant sludge, including heavy metal curing agent metering groove, a spiral conveyer heating heavy metal curing agent by metering groove, heating through a spiral conveyer heating after entering into mixer, a mixed machine inner sludge fully stir and mix, using transport machinery stack paving mixture b fermentation pool inner sunshine, sunshine fermentation pool bottom part uniform arrangement with a vent pipe, after air through heat conducting oil heating of air heat exchanger heating by air blower blowing fermentation pool bottom part to make the mixture of heavy metal curing agent and sludge process aerobic fermentation, fermentation produce a tail pneuma and generations of water steam by a discharge pipe mounting part of fermentation pool by a water washing tank, a draught fan and room, sunshine fermentation pool with a remote control and mounting. This utility new type device operation cost is low, does not produce pollution for environment, it can ensure the efficient aerobic fermentation operation, is suitable for large-scale production under a condition the outside temperature is low.
NOVELTY - This utility new type relates to biological sterilizing technology field, specific a one refers to a sewage sterilizing device, comprising tube, a liquid inlet end and a liquid outlet end, the tube is divided into front chamber and rear chamber two part, the two part has a small hole with a baffle; storehouse and vertical inner rear cabin or horizontally set with a single layer or multi layer network is convenient to microorganism growing, breeding,. This utility new type satisfying the domestic sewage treatment The small land occupation, low investment and operation cost is low, a simple structure, long service life and use environment of magnesium.
NOVELTY - This utility new type claims a one use sewage processing the collecting of a generation of ozone device, by a generation system, biological compost system, Anaerobic fermentation jar and compose primary settling tank, the air outlet of the generation system a Anaerobic fermentation jar, Anaerobic fermentation jar is mud outlet a biological compost system, entrance, the generation system including gas pre-processing system and combustion pneuma generation unit, a combustion pneuma generation set a gas pre-processing system, the air outlet of the air inlet connecting Anaerobic fermentation jar of the gas pre-processing system, further comprising waste heat boiler and heat supply system, the waste heat boiler a combustion pneuma generation set and a heat supply system, the organic substance of waste water of the primary connection Anaerobic fermentation jar Anaerobic fermentation process, produce a maximum limit with a gas, used for marsh gas generation, residual heat of the produce process generation in combustion pneuma is in is a waste heat of a municipal heat supply type and use, reasonable resource and is use to avoid resource waste.
NOVELTY - The fuel cell apparatus (3000) comprises a fuel cell (100) for producing electricity using the fuel including carbon and producing the oxide including the carbon monoxide and carbon dioxide. Another fuel cell (200) is provided for producing electricity by utilizing the oxide generated in the former fuel cell. The latter fuel cell is provided with solid oxide fuel cell (210) and direct carbon fuel cell. The former fuel cell supplies the carbon monoxide to an anode (102,212,222) of the latter fuel cell. A carbon monoxide separator (400,500) separates the carbon monoxide.    USE - Fuel cell apparatus for producing electricity with direct electrochemical reaction.    ADVANTAGE - The fuel cell apparatus comprises a fuel cell for producing electricity using the fuel including carbon and producing the oxide including the carbon monoxide and carbon dioxide, and thus enables improving the efficiency of the fuel cell apparatus. The electricity production of the fuel cell is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel cell apparatus. (Drawing includes non-English language text).    Fuel cells (100,200)    Anodes (102,212,222)    Solid oxide fuel cell (210)    Carbon monoxide separators (400,500)    Fuel cell apparatus (3000)
NOVELTY - This utility new type relates to a liquid catalyst smoke purification integrated system, comprising an absorption tower, wherein the flue gas inlet of the absorption tower and a device supplying oxidizer gas are connected, ammonia water and ammonia water supply device inlet of the absorption tower are connected, pneuma outlet chimney and the absorption tower is connected, a gas and liquid catalyst inner tower, ammonia water carrying out counter-current contact reaction, mixed salt liquid outlet of the absorption tower orderly connected and filter, separator, a liquid catalyst liquid catalyst inlet and outlet of absorption tower is a separator connected. This utility new type has high efficiency, low energy consumption, convenient operation, operation cost is low, without second time pollute and waste discharge, a high value of fertilizer by-product equal advantages, besides, it can remove sulfur dioxide and nitrogen oxide in flue gas, mercury, dioxin, micro dust etc.
NOVELTY - Enzymatic hydrolysis involves: treating microalgae with enzymes to produce digested biomass, where the enzymes comprise a mixture of at least one protease and at least one amylase; and separating the digested biomass into an organic phase and an aqueous phase, where the organic phase contains lipids and the aqueous phase contains solids, carbohydrates, and peptides.    USE - The method is useful for enzymatic hydrolysis to obtain lipids, solids, or bio-based products (claimed).    ADVANTAGE - The method provides more effective and cost-efficient method of enzyme hydrolysis.
NOVELTY - This utility model claims a methionine crystal separating system, comprising feeding port, a heat exchanger, a crystallizer, a separate system and cause solution flow of circulation pump, under action of a circulation device, raw material by feeding wherein entering into heat exchanger, a heat exchanger after heat exchange enter into crystallizer and crystallizing the obtained mixed liquid return heat exchanger continuously circulation part and the other part enter into a separate system carrying out separating, separating the obtained solid product discharging system, exiting the circulation, liquid product return heat exchanger to continue circulation. This utility model new methionine crystallizing separation system in the whole processing process of processing are in closed environment, and no need to outside heating power, can save a lot of energy and pollute the environment, this utility new type of heat exchanger is set with front in crystallizer, is notable increase final production performance, this utility new type crystal system separation can be continuous stable production, at last obtain methionine and stack density more than 0.6.
NOVELTY - This utility model new supply of one of domestic sludge extracting humic acid and equipment, belonging to environmental protection technology area, the domestic sludge extracting humic acid and device includes fermentation tank, the fermentation tank is set with upper sludge with injection entrance, alkali liquid injection port, a sludge outlet, upper layer clear liquid outlet and stirring device, the upper layer clear liquid outlet through pipeline connected with centrifuge, the centrifuge through pipeline connected with dryer. The domestic sludge extraction device operating the humic acid is suitable, is high efficient extraction of humic acid from domestic sludge and.
NOVELTY - Extraction and separation of rebaudioside A comprises preparing phase extraction solvent; mixing Stevia leaves and extraction solvent; heat extracting; filtering, centrifuging, and cooling; absorbing in macroporous resin, washing with ethanol, and desorbing; film separating, carrying out HPLC tracking analysis, and collecting rebaudioside A; vacuum concentrating; standing; centrifuging or plate frame filter pressing and filtering; washing solid material with ethanol solution; centrifuging or plate frame filter pressing and filtering material; and drying.    USE - Method for extracting and separating rebaudioside A (claimed).    ADVANTAGE - The rebaudioside A has purity of more than 97% and is stable. The method is simple, does not need high requirements of device, has low energy consumption and high output, and completely removes bitter taste of Stevia leaves.    DETAILED DESCRIPTION - Extraction and separation of rebaudioside A comprises: (A) preparing phase extraction solvent; (B) mixing Stevia leaves and extraction solvent at mass ratio of 1:10-20; (C) heat extracting at 80-90 degrees C for 1.5-2.0 hours; (D) filtering, centrifuging at rotating speed of 4000 revolutions/minute, and cooling to 40 degrees C; (F) absorbing in macroporous resin, washing with 50-80% ethanol, and desorbing; (H) film separating, carrying out HPLC tracking analysis, and collecting more than 85% purity rebaudioside A; (I) vacuum concentrating to specific gravity of 1.1-1.5; (J) standing for 12-24 hours at 40 degrees C; (K) centrifuging or plate frame filter pressing and filtering; (L) washing solid material with 2-4 times 95-100% ethanol solution for 15-30 minutes; (M) centrifuging or plate frame filter pressing and filtering material; and (N) normal drying or spray drying.
NOVELTY - Veterinary drug composition comprises 1-100 pts. wt. root of Chinese Pulsatilla, 1-50 pts. wt. dandelion, 1-50 pts. wt. radix scutellariae, 1-50 pts. wt. honeysuckle, 1-30 pts. wt. Phellodendron, 1-50 pts. wt. radix sophorae flavescentis, 1-30 pts. wt. Gentiana scabra Bge, 1-30 pts. wt. bighead Atractylodes rhizome, 1-30 pts. wt. tuckahoe, 1-30 pts. wt. radix paeoniae alba, 1-50 pts. wt. cortex fraxini, 1-30 pts. wt. smoked plum and 1-30 pts. wt. licorice.    USE - The composition is useful for preventing and treating white diarrhea in chickens (claimed).    ADVANTAGE - The composition promotes the healthy development of pollution-free farming and non-residual green meat processing industry.
NOVELTY - (R)-propylene carbonate is prepared by mixing (S,S)-N,N'-bis(3,5-di-tert.-butylsalicylidene)-1,2-cyclohexanediamino-cobalt(II) ((S,S)-Salen Co) catalyst, toluene, and acetic acid, reacting to active catalyst, mixing with propylene oxide at 0-5 degrees C, dropping water, stirring at room temperature until reaction completion, distilling off (S)-propylene oxide under atmospheric pressure, vacuum distilling (R)-1,2-propanediol, mixing with urea and zinc oxide, completely reacting at 100-120 degrees C, removing (R)-1,2-propanediol under vacuum, and continuously distilling.    USE - Preparation of (R)-propylene carbonate for preparation of tenofovir intermediate.    ADVANTAGE - Process is simple, versatile, environment-friendly, easy to operate, low cost, and has high selectivity and high yield.
NOVELTY - Organic fertilizer fermentation comprises pool type aerobic continuous fermentation, which comprises uniformly mixing solid organic waste, microbial inoculum and auxiliary material at 70-75:29.99-24.99:0.01 ratio to obtain fermentation raw material having carbon nitrogen ratio of 25-30:1, conducting primary aerobic fermentation for 7 days at not less than 55 degrees C to obtain fermentation product, conducting secondary fermentation at room temperature for 10-15 days and drying to obtain organic fertilizer.    USE - Organic fertilizer fermentation (claimed).    ADVANTAGE - The method is safe and achieves recycling of waste materials.
NOVELTY - Special potato fertilizer comprises 6-12 wt.% dairy manure, 6-12 wt.% oil, 40-60 wt.% quail manure, 8-12 wt.% calcium magnesium phosphate, 10-20 wt.% potassium sulfate, and 2-5 wt.% biological bacteria, where total weight is 100 wt.%. It is prepared by mixing dairy manure, oil and quail manure, adding biological bacteria, uniformly stirring, maintaining water content, fermenting, entering into fermentation tower and fermenting, adding calcium-magnesium phosphate fertilizer and potassium sulfate, mixing, crushing, sieving, checking, and granulating or powderizing.    USE - Special potato fertilizer used to provide drought-resistant potato (claimed).    ADVANTAGE - The special potato fertilizer has high content of nutrients and higher yield than the normal fertilizer.    DETAILED DESCRIPTION - Special potato fertilizer comprises 6-12 wt.% dairy manure, 6-12 wt.% oil, 40-60 wt.% quail manure, 8-12 wt.% calcium magnesium phosphate, 10-20 wt.% potassium sulfate, and 2-5 wt.% biological bacteria, where total weight is 100 wt.%. It is prepared by mixing dairy manure, oil and quail manure, adding biological bacteria, uniformly stirring, maintaining water content at 45-48%, fermenting for 20 days, entering into fermentation tower and fermenting for 10 days, or conducting aerobic fermentation by mixing dairy manure, oil and quail manure, maintaining water content at 25%, conducting aerobic fermentation, adding calcium-magnesium phosphate fertilizer and potassium sulfate, uniformly mixing, crushing, sieving, checking, and granulating or powderizing to obtain the product.
NOVELTY - Fertilizer comprises 3 pts. wt. bentonite, 2 pts. wt. acetic acid, 12 pts. wt. potassium hydroxide, 2 pts. wt. humic acid, 12 pts. wt. ammonium chloride, 4 pts. wt. water retention agent, 10 pts. wt. water hyacinth ferment, 7 pts. wt. carbonate, 6 pts. wt. boron-sludge, 7 pts. wt. leavening agent, 5 pts. wt. ammonium nitrate, 4 pts. wt. emulsifier, and 1 pts. wt. silicate solubilizing bacteria.    USE - The fertilizer is useful for preserving fruit (claimed).    ADVANTAGE - The fertilizer can effectively improve soil aggregate structure, soil cation exchange capacity, fruit quality and sugar and vitamin C content, and enhances plant cold-proof and drought resistance.
NOVELTY - Efficient pesticide composition comprises 10-50 pts. wt. fenvalerate, 20-40 pts. wt. fipronil and 20-60 pts. wt. chlorfenvinphos.    USE - Efficient pesticide composition in the form of emulsifiable concentrate, suspension, wettable powder, water dispersible granules or water emulsions used for controlling agricultural pests, killing bollworm, cabbage caterpillar, tobacco budworm, soybean pod borer, armyworm class, fruit borer, leafminer moths, Cnaphalocrocis medinalis, Plutella xylostella, inchworm, bridge-building insects, aphid, leafhopper, planthopper class, stinkbugs, locusts and leaf-eating beetles (all claimed).    ADVANTAGE - The pesticide is environment-friendly, inexpensive, has obvious synergistic effect and reduced effective component dosage.
NOVELTY - Oxymatrine agent comprises 25% of radix sophorae flavescentis extracting liquid, 1.5% of inorganic elements, 5% of vegetable fat, 5% of sugar, and 60.5% of water.    USE - The oxymatrine agent is useful for killing aphid, planthopper and spider mites.    ADVANTAGE - The oxymatrine agent can be rapidly prepared without residue and pollution in an economical manner, and has reduced toxicity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the oxymatrine agent, comprising extracting the radix sophorae flavescentis and then washing with water, mixing with inorganic elements, vegetable fat, sugar, and water, drying, grinding and sieving.
NOVELTY - A reactor (200) comprises fluid tight tank (208) which has interior and exterior, heat transfer media (215) which is positioned within tank, greater than or equal to 1 reaction line (202) which is positioned within tank, in thermal communication with heat transfer media, and in fluid communication with exterior of tank, greater than or equal to 1 heater (213) in thermal communication with heat transfer media, and greater than or equal to 1 pump (216) configured to drive reactant fluids through the reaction line.    USE - A reactor for biodiesel production (claimed).    ADVANTAGE - Reaction is fast, efficient with regard to energy input and waste generation, and requires minimal alcohol. Biodiesel is produced with high quality and low sulfur without using supplemental catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of biodiesel which involves emulsifying mixture containing alcohol and source of fatty acids, pressurizing and heating emulsion until alcohol is supercritical, pumping emulsion through vessel under non-laminar flow, and maintaining non-laminar flow of emulsion and supercriticality of alcohol in emulsion for greater than or equal to 1.5 minutes.    DESCRIPTION OF DRAWING(S) - The drawing shows a side cut-away view of reactor and overflow basin cut along line B-B of the perspective view of the reactor and the basin.    Reactor (200)    Reaction line (202)    Tank (208)    Heat transfer media (215)    Pump (216)
NOVELTY - The hydrogen fuel cartridge (120) has a canister. A top cap is operatively connected to the canister and has an overmolded face seal gasket that provides an offset injection point on the fuel cartridge. A reactant fuel material (177) e.g. silicides, is arranged within the canister. The top cap comprises a hydrogen output port and a cartridge valve configured to control the flow rate of hydrogen through the hydrogen output port. The cartridge valve comprises a hydrogen flow restriction orifice.    USE - Hydrogen fuel cartridge used in hydrogen fuel cell system (claimed) for generating hydrogen using sodium silicide, sodium silica gel, or multi-component mixtures, used in applications such as stationary power generation, lighting, back-up power, consumer electronics, personal mobility devices such as electric bicycles, and landscaping equipment. Can also be used in gasoline turbine, and rnal combustion engine.    ADVANTAGE - The aqueous solution e.g. water, is delivered into the fuel cartridge to generate hydrogen for the fuel cell which then produces power for the user of the electronics. The thin walled fuel cartridges are used while providing a highly robust cap restraint mechanism. The flow valve is a physical switch that is controlled by a user or an electronically controlled switch. The water feed tray and fuel cartridge are constructed to effectively function as a single sub-system with the entire sub-system is removable/replaceable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen fuel cell power system including a fuel cell, water feed tray, and a fuel cartridge.    Fuel cell (110)    Hydrogen fuel cartridge (120)    Feed tray (130)    Check valve (140)    Reactant fuel material (177)
NOVELTY - Isolating kukoamine, comprises contacting a polyamide or its derivative as an immobile phase with a solution of a crude extract of kukoamine.    USE - The process is useful for isolating kukoamine (claimed) which is used as antiinflammatory, antioxidative and hypotensive agents and for treating sepsis and autoimmune disease. No biological data given.    ADVANTAGE - The process is rapid, convenient, economical and environmental-friendly, and provides high yield of purified kukoamines.
NOVELTY - The heat exchanger (1) comprises an influx unit (20) and an exhausting unit (30), which are equipped in the lower portion and upper portion of the heat exchanger. A water supply unit (40) and fuel supply unit (50) are equipped in the one-side upper portion of the heat exchanger. A mixing gas exhausting unit (60) is equipped in the lower portion of the heat exchanger. A high temperature channel is provided for collecting heat in the exhaust gas of the high temperature. Multiple injection pipes (42) are provided for supplying water into the low temperature channel.    USE - Heat exchanger for exchanging exhaust gas of high temperature generated in a fuel cell stack.    ADVANTAGE - The heat exchanger comprises an influx unit and an exhausting unit, which are equipped in the lower portion and upper portion of the heat exchanger, and thus ensures easily mixing water or the steam of the high temperature with fuel. The evaporation of water of the exhaust gas is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a heat exchanger.    Heat exchanger (1)    Influx unit (20)    Exhausting unit (30)    Water supply unit (40)    Injection pipe (42)    Fuel supply unit (50)    Mixing gas exhausting unit (60)
NOVELTY - A scoured ramie bio-degumming wastewater is used by passing scoured ramie wastewater through filter press to obtain pure clear scoured liquid, and carrying out biological fermentation to obtain biological fermentation product which is low concentration mixed alcohol fuel liquid, or filtering pure clear scoured liquid to obtain filtrate, performing biological inoculation to obtain inoculated biological fluid, fermenting to obtain low concentration mixed alcohol fuel liquid, and standing to separate mixed alcohol fuel.    USE - Use of scoured ramie bio-degumming wastewater (claimed).    ADVANTAGE - Process is simple and low cost, saves water resource, and uses high-temperature sterilization.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for scoured ramie bio-degumming wastewater device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of use of scoured ramie bio-degumming wastewater. (Drawing includes non-English language text).
NOVELTY - A nano biofertilizer composition comprises fertilizer material nanoparticles and bacteria.    USE - Nano biofertilizer composition used for improving seed germination rate and plant growth and development.    ADVANTAGE - The composition is environment-friendly; contains nutrient element with very high purity, thus, small amount of nutrient would suffice to provide the nutrition; disperses nutrients to the plants in homogenous manner; accelerates plant growth and shortens germination time and crop yield duration; and increases yield and quality of agricultural crops. Plants exposed to the composition exhibits increase in vegetative biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of nano biofertilizer composition by:    (A) adding glacial acetic acid to aqueous solution of cupric chloride (CuCl2) and heating to predetermined temperature with stirring;    (B) adding sodium hydroxide until desired pH is reached to obtain precipitate;    (C) centrifuging to separate the precipitate;    (D) repeatedly washing the precipitate with deionized water;    (E) drying to obtain copper oxide nanoparticles; and    (F) mixing with bacteria.
NOVELTY - Preparation of high-efficiency environment-friendly pesticide comprises selecting abamectin, long-effect maintaining agent, surfactant, chlorthalidone, composite fertilizer and water as raw materials, crushing, sieving, adding into reaction kettle, adding cosolvent, stirring to completely dissolve to obtain mixture, mixing demineralized water and foaming agent, stirring to obtain additive, adding additive into mixture, heating, adding sodium alkylsulfonates, stirring, adding capsaicin and deionized water, reacting, gradually reducing temperature to room temperature and cooling.    USE - Method for preparing high-efficiency environment-friendly pesticide (claimed).    ADVANTAGE - The strong and stable pesticide has reasonable and simple composition, and provides nutritional fertilizer for plants.    DETAILED DESCRIPTION - Preparation of high-efficiency environment-friendly pesticide comprises:    (A) selecting 25 wt.% abamectin, 8 wt.% long-effect maintaining agent, 20 wt.% surfactant, 8 wt.% chlorthalidone, 2 wt.% composite fertilizer and balance water as raw materials;    (B) crushing, sieving by 20-200 mesh vibration sieve, adding into reaction kettle, adding cosolvent and stirring to completely dissolve to obtain mixture;    (C) mixing demineralized water and foaming agent at weight ratio of 3:2, stirring to obtain additive, adding additive into mixture, heating at 40-50 degrees C, adding sodium alkylsulfonates and stirring for 2 hours; and    (D) adding 2% capsaicin, adding deionized water, reacting at 80-90 degrees C for 40 minutes, gradually reducing temperature to room temperature and cooling for 40-60 minutes.
NOVELTY - Method for preparing fat and oil component, involves culturing algae of marine Chlamydomonas in culture medium containing sea salt.    USE - The method is useful for preparing fat and oil component which is used for preparing higher unsaturated fatty acid including oleic acid and linolenic acid (all claimed). The fat and oil component is useful as fuel and chemical substance raw material.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for preparing higher unsaturated fatty acid, involves hydrolyzing the fat and oil component to produce fat and oil component; and (2) Chlamydomonas strain JSC4 having fat and oil component producing ability.
NOVELTY - A cell comprising one or more heterologous polypeptides comprising the amino acid sequence of any one of SEQ ID NOs. 1-30 or one or more heterologous polypeptides with at least 90% sequence identity to any one of SEQ ID NOs. 1-30, is new.    USE - The cell and polypeptide are useful for processing one or more of polysaccharides, oligosaccharides, or monosaccharides (claimed) and for producing industrially useful compounds, including biofuels, such as ethanol.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) an isolated polypeptide comprising the amino acid sequence of any one of SEQ ID NOs. 1-30, or an amino acid sequence with at least 90% sequence identity to any one of SEQ ID NOs. 1-30;    (2) an isolated nucleic acid comprising the nucleic acid sequence of any one of SEQ ID NOs. 31-60 or a nucleic acid sequence with at least 70% sequence identity to any one of SEQ ID NOs. 31-60;    (3) a vector comprising the isolated nucleic acid of (2);    (4) an isolated cell comprising the vector of (2); and    (5) a method of processing one or more of polysaccharides, oligosaccharides, or monosaccharides, by contacting a solution comprising polysaccharides, oligosaccharides, and/or monosaccharides with one or more of the cells above, one or more of the isolated polypeptides of (1), or their combination, under conditions sufficient for processing the polysaccharides, oligosaccharides, and/or monosaccharides.
NOVELTY - The method involves utilizing kitchen rubbish hydrolysis acidification liquid as an external carbon source. Water outlet nitrogen and chemical oxygen demand (COD) concentration controlling process is performed. Kitchen rubbish screening process is performed by a screen. Oil removing process is performed. Anaerobic fermentation process is performed by an anaerobic fermentation jar. Kitchen rubbish landfill leachate is filled in a SBR reaction pool. Kitchen rubbish landfill leachate biological de-nitrification and COD removing processes are performed.    USE - Kitchen rubbish landfill leachate biological de-nitrification and COD removing method.    ADVANTAGE - The method enables reducing nitrogen concentration less than 40 mg/L and COD concentration less than 100 mg/L so as to achieve national discharge standard in an efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a kitchen rubbish landfill leachate biological de-nitrification and COD removing method.'(Drawing includes non-English language text)'
NOVELTY - The poultry manure excrement machine has two side plates (1) fixed with a rectangular beam (2) mounted with a motor (4). A transmission component is welded in the upper side of rectangular beam. A target turning shaft (3) is supported in lower portion of a transmission box (9). The motor is provided to drive a speed reducer whose output shaft is equipped with the target turning shaft for rotating a chain transmission element (6) and a traveling shaft (10), to rotate a chain (7). The transmission box is provided with an elastic element (12) formed with preset thickness.    USE - Poultry manure excrement machine.    ADVANTAGE - The curing effect and fermentation effect of the poultry manure are improved, and the efficiency of the poultry manure excrement machine is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the poultry manure excrement machine.    Side plate (1)    Rectangular beam (2)    Target turning shaft (3)    Motor (4)    Chain transmission element (6)    Chain (7)    Transmission box (9)    Traveling shaft (10)    Elastic element (12)
NOVELTY - Zinc-aluminum-silicon metal oxide containing solid base catalyst, is claimed. The preparation of catalyst comprises preparing silicon dioxide-alumina composite support by sol-gel method, and loading zinc oxide by dipping method.    USE - The catalyst is useful for producing biodiesel by catalytic transesterification (claimed).    ADVANTAGE - The byproduct glycerin obtained during catalytic transesterification has high purity, and the impurities are detected by gas chromatography (claimed). The catalyst has large specific surface area, and strong alkali strength.
NOVELTY - Preparing a solid base catalyst comprises mixing sodium metasilicate nonahydrate, calcium oxide and potassium fluoride dihydrate in a molar ratio of 2:5:1.5-6, grinding the mixture to a paste, drying the paste at 70-90 degrees C for 5 7 hours and calcining the dried paste at 300-500 degrees C for 3.5-4.5 hours.    USE - The process is useful for preparing a solid base catalyst (claimed). The solid base catalyst is useful for the preparation of biodiesel.    ADVANTAGE - The process is capable of simply preparing the solid base catalyst with good catalytic effect.
NOVELTY - Preparing liquid nitrogen fertilizer comprises introducing water into the micro-plasma apparatus having an open air-source, adjusting an air flow of the open air source, turning on high voltage direct current (DC) power supply, starting a reaction between an anode and water surface to form micro-plasma, inducing chemical reaction using micro-plasma for 3-15 minutes to produce nitrite and nitrate and then discharging.    USE - The method is useful for preparing liquid nitrogen fertilizer (claimed).    ADVANTAGE - The method is capable of easily preparing the liquid nitrogen fertilizer with improved storage stability and portability in an economical and energy-efficient manner.
NOVELTY - Producing fertilizer comprises mixing phosphoric acid and carbamide and a temperature of 100-130 degrees C, stirring the mixture to obtain an intermediate slurry, mixing the slurry with alkaline potassium salt at a temperature of 65-75 degrees C and then stirring, adjusting a pH value of the mixture to 8-9.5 to obtain slurry containing nitrogen and phosphorus, placing the slurry containing nitrogen and phosphorus in a mold to cool, crystallizing the mixture and then filtering to obtain a filtrate, and adding trace elements to the filtrate and then adjusting the water content and drying.    USE - The method is useful for producing fertilizer, which is useful for tomatoes (claimed).    ADVANTAGE - The method is capable of economically producing the fertilizer with high yield in an environmentally friendly manner.    DETAILED DESCRIPTION - Producing fertilizer comprises mixing phosphoric acid and carbamide at a molar ratio of 1.5-2.1:1 and a temperature of 100-130 degrees C, stirring the mixture for 3-5 hours to obtain an intermediate slurry, mixing the slurry with alkaline potassium salt at a temperature of 65-75 degrees C and then stirring for 40-60 minutes, adjusting a pH value of the mixture to 8-9.5 to obtain slurry containing nitrogen and phosphorus, placing the slurry containing nitrogen and phosphorus in a mold to cool, crystallizing the mixture and then filtering to obtain a filtrate, and adding trace elements to the filtrate and then adjusting the water content and drying at 40-60 degrees C for 1-2 hours. A molar ratio of nitrogen and phosphorus is 0.9-1.1:2.9-3.
NOVELTY - Producing fertilizer involves utilizing 85-90 pts. wt. fresh sisal hemp waste, 0.5-1.0 pts. wt. microelement, 5-10 pts. wt. organic acid, 2-4 pts. wt. concentrate liquid of molasses and 0.1-5 pts. wt. surfactant. Fresh sisal hemp is cleaned and then cut through a blade and mixing with remaining components and then stirred uniformly in a fermenting container to carry out fermentation at 30-50 degrees C for 10-15 days to obtain fermentation liquid. The fermentation liquid is filtered to obtain filtered liquid.    USE - Method for producing fertilizer (claimed) used for promoting fruit growth.    ADVANTAGE - The method enables to produce fertilizer in a cost-effective and eco-friendly manner, and increases weight and yield of fruit by 10-20%.
NOVELTY - Fertilizer comprises 5-10 pts. wt. sodium humate, 6-8 pts. wt. ammonium oxalate, 3-6 pts. wt. borax, 15-20 pts. wt. potassium chloride, 13-18 pts. wt. phosphorus ore powder, 13-19 pts. wt. magnesium sulfate, 12-17 pts. wt. chelated zinc, 11-13 pts. wt. polyaspartic acid, 5-7 pts. wt. plant ash, 3-5 pts. wt. fermentative bacteria, 2-3 pts. wt. earthworm, 2-4 pts. wt. soil water retention agent, 5-6 pts. wt. bentonite, 1-3 pts. wt. alginic acid, 10-15 pts. wt. ferrous sulfate, 10-14 pts. wt. amino acid, and 60-80 pts. wt. water.    USE - The fertilizer is useful for potato (claimed).    ADVANTAGE - The fertilizer has enhanced water retention property, increases the nutritional substance of the potato, effectively promotes the growth of potato plant, and improves the quality of the potato.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer, comprising mixing the above raw material into a stirrer and then stirring, homogenizing, sealing and fermenting for 3 hours.
NOVELTY - Fertilizer composition comprises 21-23 pts. wt. ammonium nitrate, 18-20 pts. wt. phosphorus pentoxide, 16-19 pts. wt. plant ash, 11-13 pts. wt. zinc sulfate, 14-16 pts. wt. diammonium phosphate, 5-8 pts. wt. bentonite, 9-12 pts. wt. Bordeaux mixture, 10-13 pts. wt. potassium chloride, 9-13 pts. wt. alanine, 8-10 pts. wt. selenium humic acid fertilizer, 3-5 pts. wt. urease inhibitor, 6-9 pts. wt. Borax (RTM: Sodium tetraborate), 5-7 pts. wt. stubble agent, 6-8 pts. wt. soil conditioner, 10-15 pts. wt. animal manure and 30-40 pts. wt. water.    USE - Fertilizer composition used for corn (claimed).    ADVANTAGE - The fertilizer composition ensures improved fertility of corn, soil property, water permeability, disease resistant ability, plant survival rate and yield and quality of corn.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a fertilizer composition, which involves:    (A) crushing animal manure and Borax to obtain 20 meshes size;    (B) mixing ammonium nitrate, phosphorus pentoxide, plant ash, zinc sulfate, diammonium phosphate, bentonite, Bordeaux mixture, potassium chloride, alanine, selenium humic acid fertilizer, urease inhibitor, stubble agent, soil conditioner and water to the obtained mixture with stirring; and    (C) fermenting the obtained material for 6 hours, and then dried to obtain the finished product.
NOVELTY - Fertilizer composition comprises 24-26 pts. wt. potassium fertilizer, 21-23 pts. wt. nitrogen fertilizer, 19-22 pts. wt. phosphate fertilizer, 16-18 pts. wt. urea fertilizer, 13-15 pts. wt. fly ash, 10-13 pts. wt. calcium superphosphate, 7-9 pts. wt. green manure, 5-8 pts. wt. mushroom fertilizer, 6-9 pts. wt. potassium chloride, 4-6 pts. wt. tetramethyl glutaric acid, 3-5 pts. wt. calcium sulfate, 2 pts. wt. bacterial fertilizer, 1-3 pts. wt. Borax (RTM: Sodium tetraborate) and 60-70 pts. wt. water.    USE - Fertilizer composition used for white turnip (claimed) for promoting meat quality.    ADVANTAGE - The fertilizer composition ensures improved supplying of nutrients and improved yields.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a fertilizer composition, which involves:    (A) mixing raw materials, and then fermenting them for 6 hours in a sealed container; and    (B) drying the obtained material to obtain the finished product.
NOVELTY - Fertilizer composition comprises 23-25 pts. wt. urea, 19-21 pts. wt. ammonium bicarbonate, 17-19 pts. wt. tea seed cake fertilizer, 15-17 pts. wt. boron and magnesium fertilizer, 12-14 pts. wt. nitrogen, phosphorus and potassium (NPK) fertilizer, 10-13 pts. wt. potassium sulfate, 9-12 pts. wt. forchlorfenuron, 7-9 pts. wt. ferrous sulfate, 6-8 pts. wt. datura flower vegetable powder, 3-5 pts. wt. ammonium sulfate, 12-14 pts. wt. cattle manure, 7-9 pts. wt. fly ash, 4-6 pts. wt. humic acid, 6-9 pts. wt. calcium magnesium phosphate fertilizer, 1-3 pts. wt. mancozeb and 50-60 pts. wt. water.    USE - Fertilizer composition used for apricot (claimed) for preventing and treating plant diseases, and insects and pests infections.    ADVANTAGE - The fertilizer composition ensures improved supplying of nutrients and improved yields with improved mouth feel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a fertilizer composition, which involves:    (A) mixing raw materials, and then fermenting them for 1 hour in a sealed container; and    (B) drying the obtained material to obtain the finished product.
NOVELTY - 17-ethynyl-16-ene steroid derivative is prepared by reacting 17 alpha -ethynyl-17 beta -nitro ester steroid derivative with monovalent silver salt or monovalent copper salt in aprotic organic solvent with reaction temperature of 25 degrees C to solvent refluxing temperature and removing 17 beta -nitro ester.    USE - Preparation of 17-ethynyl-16-ene steroid derivative (claimed).    ADVANTAGE - Preparation of 17-ethynyl-16-ene steroid derivative is low-cost and environment-friendly and has high yield and product purity.    DETAILED DESCRIPTION - 17-ethynyl-16-ene steroid derivative of formula (II) is prepared by reacting 17 alpha -ethynyl-17 beta -nitro ester steroid derivative of formula (I) with monovalent silver salt or monovalent copper salt in aprotic organic solvent with reaction temperature of 25 degrees C to solvent refluxing temperature and removing 17 beta -nitro ester.    formula (a)=double bond or single bond;    formula (b)=-H or formulae (b1)-(b3); and    formula (c)=9,11-position double bond or 9 beta ,11 beta -epoxy.
NOVELTY - The device has an electrolyte circulation pump and a heat exchanger connected together. An air outlet and an air inlet of a hydrogen and oxygen storage filter pneuma jar are fixed with a stainless steel capillary pipe and a hydrogen pressure-reducing type water device. An air inlet of an oxygen pneuma water storage device is connected with a water outlet of the hydrogen and oxygen storage filter pneuma jar. A gas outlet of a hydrogen and oxygen mixed gas integrated dry-wet fire arrestor directly conveys two-gas output through a pressure control switch and a flow meter.    USE - Integrated-type hydrogen-oxygen mixed gas generation device.    ADVANTAGE - The device has compact structure, reasonable design, better pressure relief explosion property, low gas leakage loss, high working efficiency and operational safety and large gas amount, and prevents hydrogen-oxygen mixed gas tempering effect and avoids gas leakage effect, and is energy-saving and safe and reliable to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a top perspective view of an integrated-type hydrogen-oxygen mixed gas generation device.
NOVELTY - A one burning biomass carbon ash purification device, comprising burning room, the lower part set with combustion chamber and combustion room connected with a separating room, lower separating room side part has gas entrance, separating room is set with cone-shaped dust depositing chamber, depositing room has dust outlet. Inner separating room. and combustion room connected with a gas pipe, a gas entrance of gas pipe is higher than the lower end entrance, gas from the gas conduit into the combustion room. Beside the combustion room set with oxygen supply ring, between the oxygen supply ring and combustion room set with a vertical multi-supplement oxygen hole. After the beneficial effects: the gas from gas entrance entering into separating room, a dust in gas under a function of its own body weight and centrifugal force, a free fall to sedimentation chamber, then discharging a dust outlet. So as to make a carbon foam spark and dust in a combustion flame purification.
NOVELTY - Method (M1) of removing limonene in biomass saccharification liquid, involves (a) preparing a solution obtained from saccharification of biomass, and (b) contacting the prepared solution with activated carbon and cellulose fiber.    USE - The method is useful for removing limonene in biomass saccharification liquid which is used for producing bioethanol (all claimed). The biomass saccharification liquid is obtained from mandarin peel, orange peel, grapefruit peel, lemon peel or lime peel.    ADVANTAGE - The method effectively removes limonene present in the biomass saccharification liquid, and hence yield of bioethanol is increased.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) device for removing limonene in biomass saccharification liquid, comprises hollow housing inserted with activated carbon and cellulose fiber to a predetermined thickness; and    (2) method (M2) of producing bioethanol, involves fermenting the biomass saccharification liquid using yeast, where limonene is removed in the biomass saccharification liquid.
NOVELTY - This utility new type is a one Anaerobic a marsh gas desulfurization special washing tower, comprising with marsh gas inlet, lower end part of a tower body, a tower body upper end is provided with an air outlet one side is mounted with and bioreactor is used for connecting a liquid outlet pipe, a tower body and reactor is used for connecting a circulation water inlet pipe, further comprising lower end on the tower body, a terminal and a spraying device in the tower body of the spraying pipe, the circulation water inlet pipe end and inner spray pipe. Has a good effect, simple device, low investment and operation cost is low, good safety, without second time pollution, and easy management and so on. It also has small floor area, simple maintenance operation is.
NOVELTY - Preparation of calcium lactate involves mixing calcium carbonate and lactic acid, as raw material, adding water as reaction solvent, reacting the resultant product, crystallizing the resultant product using ethanol, washing the resultant product with ethanol, and drying to obtain high-purity calcium lactate crystals.    USE - Preparation of calcium lactate used in pharmaceutical and food application (all claimed).    ADVANTAGE - The method provides calcium lactate by environmentally-friendly and simple process, with high purity, yield of 87.2% and reduced heavy metal residues, in short period of time.
NOVELTY - Briquette comprises hay that is dried to a water content of up to 20 wt.% and is cutted, dedusted and then grouted to a stem length of 10-150 mm.    USE - The briquette is useful as a food product used for feeding large animals such as horses or cows and small animals such as rabbits and guinea pigs.    ADVANTAGE - The briquette can be produced with improved natural vitamins, flavor and fragrance and without any additives.
NOVELTY - Producing a homogeneous solid biomass comprises: mechanical dewatering (second stage of process) the obtained filtrate, which is not directly recycled into hydrothermal carbonization (first stage of process) and decomposed during evaporation (fourth stage of process) to form a residue and a condensate; and introducing the residue and condensate from the fourth stage of the process to the first stage of the process or second stage of the process.    USE - The process is useful for producing a homogeneous solid biomass (claimed). The biomass is useful as fertilizer and biofuels. No biological data given.    ADVANTAGE - The process is capable of producing homogeneous solid biomass with good fluidisability value and without consuming large amount of energy.    DETAILED DESCRIPTION - Producing a homogeneous solid biomass comprises: mechanical dewatering (second stage of process) the obtained filtrate, which is not directly recycled into hydrothermal carbonization (first stage of process) and decomposed during evaporation (fourth stage of process) to form a residue and a condensate; and introducing the residue and condensate from the fourth stage of the process to the first stage of the process or second stage of the process such that the solids discharged from the second stage of the process does not exceed a minimum threshold value, the filtrate discharged from the second stage of the process and residue from the first stage of the process and/or second stage of the process does not exceed a minimum threshold value, the amount of the residue from the fourth stage of the process, which is introduced in the first stage of the process and/or second stage of the process, is reduced and/or the amount of the condensate from the fourth stage of the process, which is introduced in the first stage of the process and/or second process stage, is increased.
NOVELTY - Preparation of solid base catalyst involves loading zinc oxide to zinc-aluminum hydrotalcite-type carrier comprising oxides of zinc and aluminum, coprecipitating, and curing.    USE - Preparation of solid base catalyst used for catalytic transesterification for producing biodiesel (all claimed).    ADVANTAGE - The solid base catalyst which has high quality and improves transesterification reaction conversion rate, is prepared.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of zinc-aluminum hydrotalcite-type carrier, which involves mixing precursor salt of zinc and aluminum, adding sodium carbonate solution, dripping deionized water, reacting at 60 degrees C for 6 hours, washing with deionized water, and drying; and    (2) catalytic transesterification.
NOVELTY - Preparation of solid alkali catalyst comprises mixing sodium metasilicate nonahydrate, calcium oxide, and potassium fluoride dihydrate at molar ratio of 2.0:5.0:1.5-6.0, grinding, drying at 70-90 degrees C for 5-7 hours, and baking at 300-350 degrees C for 3.5-4.5 hours.    USE - Method for preparing solid alkali catalyst (claimed) used for preparing biodiesel.    ADVANTAGE - The catalyst has good catalytic effect.
NOVELTY - Preparation of solid alkali catalyst comprises mixing sodium metasilicate nonahydrate, calcium oxide, and potassium fluoride dihydrate at molar ratio of 2.0:5.0:1.5-6.0, grinding, drying at 70-90 degrees C for 5-7 hours, and baking at 350-400 degrees C for 3.5-4.5 hours.    USE - Method for preparing solid alkali catalyst (claimed) used for preparing biodiesel.    ADVANTAGE - The catalyst has good catalytic effect.
NOVELTY - Preparing bioorganic fertilizer, by mixing weighed corn stalks, wheat straw, chicken manure, sheep manure and pig manure, fermenting mixture, drying fermented product, crushing dried product, sieving powder, adding water to sieved powder, granulating mixture, drying wet granules, adding dried granules to pneumatic suspension device, further adding water-soluble binder and Bacillus licheniformis powder, repeating the above-mentioned addition step thrice, blowing gas into pneumatic suspension, heating suspension, cooling product and packaging cooled product.    USE - The method is useful for preparing bioorganic fertilizer which is used for increasing fertility of soil, controlling bacterial and fungal root rot and pear scab disease, and killing pathogenic bacteria in soil.    ADVANTAGE - The method enables usage of the B.licheniformis in a convenient manner with high viable and survival rate for controlling diseases.    DETAILED DESCRIPTION - Method for preparing bioorganic fertilizer, involves weighing 10-50 pts. wt. Bacillus licheniformis, 20-40 pts. wt. corn stalks, 20-40 pts. wt. wheat straw, 1-5 pts. wt. chicken manure, 1-5 pts. wt. sheep manure and 1-5 pts. wt. pig manure, mixing weighed corn stalks, wheat straw, chicken manure, sheep manure and pig manure, fermenting obtained mixture for 7-15 days, drying fermented product, crushing dried product to obtain powder, sieving the powder, adding water to sieved powder, granulating mixture to obtain granules having particle diameter of 1-5 mm, drying wet granules, adding dried granules to pneumatic suspension device, further adding water-soluble binder and then B.licheniformis powder to the device, repeating the above-mentioned step of adding the water-soluble binder and B.licheniformis powder for 3 times, blowing gas into obtained pneumatic suspension, heating the suspension to 40-50 degrees C by heating device, cooling obtained product and packaging cooled product.
NOVELTY - Method for preparing organic fertilizer, involves (a) performing aerobic fermentation of organic fertilizer, and adjusting pH of the organic fertilizer to 7-8.5, (b) aging obtained fertilizer at 40 degrees C until the moisture content reaches less than 30%, adjusting pH of the aged mixture to 7-8.5, diluting 1-10 kg polyaspartic acid with water, adding acid solution to fertilizer, stirring mixture, and maintaining the moisture content of the fertilizer to 2%, and (c) spraying obtained mixture on crops.    USE - The method is useful for preparing organic fertilizer for enhancing function of crop nutrients (claimed).
NOVELTY - Preparing fertilizer involves stirring crop straw in cold water bath and then sieving to obtain straw powder. The straw powder is neutralized in a reactor by adding 50-80% acrylic acid solution, acrylamide, polyethylene glycol, urea and potassium peroxodisulfate in mass ratio of 0.04:0.16:1:15-60:0.5-2:0.005-0.02:0.5-2, and then balanced amount of water is added to obtain monomer phase. Cyclohexane and Span (RTM: Nonionic surfactant)-60 are added in the reactor at normal temperature and stirred uniformly in presence of oxygen.    USE - Method for preparing fertilizer (claimed).    ADVANTAGE - The method is simple, cost-effective, eco-friendly and energy saving, enables to prepare fertilizer that has improved water retention property and high slow-release effect.    DETAILED DESCRIPTION - Preparing fertilizer involves stirring crop straw in cold water bath and then sieving to obtain straw powder. The straw powder is neutralized in a reactor by adding 50-80% acrylic acid solution, acrylamide, polyethylene glycol, urea and potassium peroxodisulfate in mass ratio of 0.04:0.16:1:15-60:0.5-2:0.005-0.02:0.5-2, and then balanced amount of water is added to obtain monomer phase. Cyclohexane and Span (RTM: Nonionic surfactant)-60 are added in the reactor at normal temperature and stirred uniformly in presence of oxygen. Sodium sulfite is added in the reactor to emulsify monomer phase for 30 minutes, stirred it for 2 hours, and then filterd by using resin bead to obtain a product. The product is vacuum dried at 42-48 degrees C for 3-6 hours to obtain fertilizer in form of powdered. Cyclohexane and monomer phase are present in volume ratio of 2.7:3.3. Sodium sulfite is added in the monomer phase in ratio of 0.04-0.16:0.02-0.08.
NOVELTY - A methanol gasoline additive comprises 5-7 pts. wt. dispersant, 25-35 pts. wt. metal rust inhibitor, 15-20 pts. wt. solubilization-increasing agent, 18-22 pts. wt. synergistic agent, and 30-35 pts. wt. isoamyl alcohol.    USE - A methanol gasoline additive (claimed).    ADVANTAGE - The additive reduces metal corrosion, and improves fuel utilization efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of methanol gasoline additive which involves mixing synergistic agent, metal rust inhibitor, solubilization-increasing agent, isoamyl alcohol, and dispersant in reaction container, ultrasonicating at 62-65 degrees C for 40-50 minutes, and cooling.
NOVELTY - Cavitation machine comprises a connection pipeline (1) that is mounted with a throttle hole plate (2), where a cavitation base (9) is set with spray hole body. A liquid jet room is provided with the cavitation base. A valve base (10) is equipped with a sprinkle hole base (5). The sprinkle hole base is set on the liquid jet room.    USE - Cavitation machine for biodiesel (claimed).    ADVANTAGE - The machine ensures good cavitation of biodiesel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a cavitation machine.    Connection pipeline (1)    A throttle hole plate (2)    Sprinkle hole base (5)    Cavitation base (9)    Valve base (10)
NOVELTY - Producing biodiesel involves adding lipid, fatty alcohol and 1-4 wt.% sodium metasilicate-calcium oxide-potassium fluoride solid base to the reaction vessel and then performing transesterification reaction, where the mole ratio of fatty alcohol and lipid is 8-15:1. The obtained material is heated on water bath at 50-80 degrees C and at 2-6 megapascal and then the heated material is distilled to separate glycerol. The separated material is added with nonionic surface active agent. The obtained material is filtered and then the filtered material is separated through ceramic film.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method enables to produce biodiesel in simple and cost-effective manner, and with high purity, high yield and high concentration of by-product glycerol.    DETAILED DESCRIPTION - Producing biodiesel involves adding lipid, fatty alcohol and 1-4 wt.% sodium metasilicate-calcium oxide-potassium fluoride solid base to the reaction vessel and then performing transesterification reaction, where the mole ratio of fatty alcohol and lipid is 8-15:1. The obtained material is heated on water bath at 50-80 degrees C and at 2-6 megapascal and then the heated material is distilled to separate glycerol. The separated material is added with nonionic surface active agent. The obtained material is filtered and then the filtered material is separated through ceramic film to separate mono-fatty acid ester and to obtain a high purity biological diesel oil. The hydrophilic lipophilic balance value of the non-ionic surface active agent is 3-25 and non-ionic surface active agent dosage of mixture mass is 0.1-10 wt.%. The support material is a ceramic film of the ceramic and film layer material is inorganic film. The inorganic film is selected from aluminum oxide or titanium oxide. The ceramic film aperture is 0.02-1.4 microns. The film separating operation is performed at 10-120 degrees C and at 0.08-0.5 megapascal pressure.
NOVELTY - This new type utility claims one a marsh gas purifier, comprising the bottom of purification tube, purification barrel body set with drainage tube, the drainage barrel body set with a drain outlet, the inner drain tube one side set with, purification tube top part set with the pneuma channel, an air outlet channel set with an air outlet, the top of purification tube set with filtering layer and purification tube is further set with a condensation chamber, condensing chamber is set between the drain tube and filter layer, a condensing set with peripheral water condensing evaporation chamber. This utility new type of advantages is: structure is simple and practical, and install use convenient and purification effect is good, which is good for processing production, is convenient to popularize and use.
NOVELTY - This utility new type claims a one marsh gas purification device, comprising bottom tube purification, purification tube set with top drain tube, a drain tube body set with a sewage outlet, is set with inner filter purification cylinder body of one side, set with purification tube top part set with the pneuma channel, an air outlet channel set with an air outlet, the top of purification tube and inner tube set with purification filter plate, a filter plate setting b the pneuma and filter material, wherein the filter guide plate inclined set purification tube, inner material guide plate top part end is set on purification the pneuma wherein a side tube, a filter plate at the bottom end is set on purification tube far away from the internal side wherein pneuma. This utility new type of advantages is: structure is simple, the purification effect, high safety performance, suitable for each b a marsh gas system in, and it is convenient to popularize use.
NOVELTY - A coordination processing method of garbage landfill comprises growing energy plants on landfill resources to produce activated carbon, and subjecting landfill to leachate treatment using activated carbon.    USE - Method for coordination processing of garbage landfill (claimed).
NOVELTY - Crop fuel preparation device comprises a machine body, a transmission device and a cavity, where the machine body is set with a driving motor, which is connected with the transmission mechanism. The cavity is set in the machine body. The cavity includes a bottom plate, a base, a bearing base set in the upper bottom plate. The motor shaft of the driving motor is connected to the base. The transverse shaft is set in the bearing base. The cross shaft is set with a set roller. The bottom plate is set with a discharging channel. The lower discharging channel is set with vibration guide groove.    USE - Used as a crop fuel preparation device.    ADVANTAGE - The device can automatically feed and discharge, has simple structure, is convenient to maintain, reduces manufacture cost, and is economical.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the crop fuel preparation device.
NOVELTY - A 2-level food waste biochemical treatment method is performed by (1) crushing waste into microparticles, water spray screening, separating solid and liquid, dissolving organic matter, sorting, and transporting; (2) separating oil and water components of food waste slag washing liquid using separator; (3) hydrolyzing and acidifying poorly soluble macromolecules to obtain soluble small molecules while degrading organic matter; (4) performing anaerobic fermentation, and decomposing organic matter to obtain biogas; and (5) purifying biogas, dehydrating, and desulfurizing.    USE - A 2-level food waste biochemical treatment method (claimed).    ADVANTAGE - The method is simple, easy to control, and has high biogas production rate and organic biomass recovery.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of 2-level food waste biochemical treatment method. (Drawing includes non-English language text).
NOVELTY - Integrated processing-gasification of straw, comprises processing straw into bio-charcoal, and producing mixed combustible gas by using charcoal, purifying the mixed combustible gas, melting metal, and casting molten metal into fuel.    USE - The method is useful for integrated processing-gasification of straw (claimed).    ADVANTAGE - The method is simple, environmental friendly, and economical; has easy operation procedure; prevents the production of waste agricultural straw, and clogging of pipes caused by dry tar; not only can produce charcoal, but also can produce charcoal by harvesting mixed combustible gas; and retains gas by removing gas from tar.
NOVELTY - A biomass-based fuel comprises mixture (A) comprising biomass and biomass additive and mixture (B) comprising low-sulfur coal and low-sulfur coal additive in which low-sulfur coal contains less than or equal to 0.9 total sulfur in dry basis, weight ratio biomass:biomass additive is 100:3-8, weight ratio low-sulfur coal:low-sulfur coal additive is 100:5-10, weight ratio mixture (A):mixture (B) is 60-90:10-40, biomass additive is blast furnace slag, and low-sulfur coal additive is steel slag and sludge gas.    USE - A biomass-based fuel for industrial waste coupling catalyst.    ADVANTAGE - Fuel has reduced pollutant emission and improved ash fusibility, density, calorific value, and combustion or conversion rate of carbon, and additive has reduced cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass-based fuel which involves blending biomass additive, grinding into 200-400 meshes powder, uniformly mixing biomass and biomass additive to obtain mixture (A), blending low-sulfur coal additive, grinding into 200-400 meshes powder, mixing low-sulfur coal and low-sulfur coal additive to obtain mixture (B), uniformly mixing obtained mixture (A) and mixture (B), and molding into molding machine.
NOVELTY - A granular biomass fuel comprises 20-60 mass% biomass alcohol, 0-20 mass% water, 1-5 mass% anti-swelling preservative, 0-5 mass% tetrahydrofuran, 3-8 mass% solvent oil, 1-5 mass% starch, 1-3 mass% potassium removing agent, 1-5 mass% cyclopentane, 2-3 mass% acetone, 2-5 mass% diethyl ether, 0-3 mass% toluene, and 0-3 mass% xylene.    USE - A granular biomass fuel for combination and proportion of wastewater raw material.    ADVANTAGE - Fuel is environment-friendly and energy-saving.
NOVELTY - A biomass fuel is produced by adding biomass raw material, crushing, adding industrial wastewater and powder-shaped solid glucoamylase, stirring, forming ferment, stirring, adding 1/100-5/100 mass% maltogenic amylase, fermenting, and drying in which mass ratio industrial wastewater and biomass fuel is 10-25:100.    USE - Production of biomass fuel (claimed).    ADVANTAGE - Process has improved production efficiency, and product has improved quality.
NOVELTY - A granular biomass fuel is produced by spreading primary raw material comprising rice stalk, rice straw, rice hull, peanut shell, corncob, Camellia shell, and/or cottonseed hull, drying, exposing on light, cutting secondary raw material into 0.5-1 cm small piece, crushing, or powdering, solar drying having moisture content of 10-20%, crushing tertiary raw material having particle diameter of less than or equal to 5 mm, granulating into granulating machine, molding having diameter of 8-10 mm and density of 0.8-1.2 t/m3, collecting to transport, screening, and reconveying into granulating machine.    USE - Production of granular biomass fuel (claimed).    ADVANTAGE - Process is environment-friendly and simple and has high reliability, and product has improved usefulness.    DETAILED DESCRIPTION - A granular biomass fuel is produced by spreading primary raw material comprising rice stalk, rice straw, rice hull, peanut shell, corncob, Camellia shell, and/or cottonseed hull, drying, exposing on light, cutting secondary raw material into 0.5-1 cm small piece, crushing, or powdering, solar drying having moisture content of 10-20%, crushing tertiary raw material having particle diameter of less than or equal to 5 mm, granulating into granulating machine, molding having diameter of 8-10 mm and density of 0.8-1.2 t/m3, collecting to transport, screening, reconveying into granulating machine, granulating, measuring, packing into belt, and storing.
NOVELTY - Use of a livestock cultivation wastewater for preparing biomass water-coal slurry, is claimed. The biomass water-coal slurry is prepared by pulverizing coal powder and wastewater, and adjusting the pH value to 7-9 with sodium hydroxide. The mass ratio of the coal powder and wastewater is 0.5-1.5:100. The resulting concentration of the biomass water-coal slurry is not less than 60 mass%.    USE - The livestock cultivation wastewater is useful for preparing biomass water-coal slurry (claimed).    ADVANTAGE - The livestock cultivation wastewater is capable of simply preparing biomass water-coal slurry with high yield and good particle size distribution and viscosity using reduced amount of coal powder and water in pulping process in an economical and eco-friendly manner.
NOVELTY - Human artificial coal comprises 70-80 wt.% wood, 10-20 wt.% molybdenum-nickel alloy powder, and 5-15 wt.% activated carbon.    USE - Human artificial coal.    ADVANTAGE - The coal has high heat value, low water content, low ash content, easy burning, excellent property, simple preparation, low technical demands for device and personnel, low cost and wide application. It solves natural coal resource shortage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of human artificial coal comprising weighing raw materials; crushing block-shaped raw materials, grinding into powders; mixing and stirring powdered raw materials; placing into inner cavity of pressure machine; evacuating cavity at pressure of 100-500 Pa; low-temperature and high-pressure processing, heating to 150-250 degrees C and 0.3-3 MPa, holding for 0.5-3 hours; high-temperature and high-pressure processing, heating to 500-900 degrees C, applying pressure of 0.3-3 MPa, holding for 60-80 hours; and slowly reducing pressure to 1 atm, and slowly cooling to room temperature.
NOVELTY - Biomass fuel comprises 40-50 pts. wt. barley straw powder, 20-35 pts. wt. broad bean straw powder, 80-90 pts. wt. wheat straw powder, 20-25 pts. wt. lipid, 10-16 pts. wt. dried coral branches, 9-13 pts. wt. gingko branches, 11-16 pts. wt. oak branches, 1-3 pts. wt. combustion improver, 20-25 pts. wt. pig fat, 25-30 pts. wt. trench oil, 10-15 pts. wt. wheat bran, 5-8 pts. wt. potato, 15-20 pts. wt. grain slag, 10-16 pts. wt. cassava residue, 5-12 pts. wt. rice straw, and 5-8 pts. wt. corncob.    USE - Biomass fuel.    ADVANTAGE - The biomass fuel replaces conventional fuel oil with good industrial prospects.
NOVELTY - A clean environment-friendly vaporizing burner biomass fuel comprises 3-5 pts. wt. black walnut chips, 4-8 pts. wt. lemon wood chips, 6-19 pts. wt. sycamore wood chips, 9-19 pts. wt. davidia wood chips, 55-60 pts. wt. wheat powder, 30-40 pts. wt. peanut powder, 9-13 pts. wt. spidemoss herb, 10-16 pts. wt. pine bark, 8-13 pts. wt. fir branches, 35-45 pts. wt. cotton straw powder, 1 pt. wt. Chinese fir powder, 1 pt. wt. cypress powder, 15-20 pts. wt. coal gangue powder, 15-20 pts. wt. mulberry tree powder and 3-6 pts. wt. pine tree powder.    USE - Clean environment-friendly vaporizing burner biomass fuel.    ADVANTAGE - The biomass fuel has increased carbon content, thus prolonging combustion time and increasing heating value. It utilizes waste from coal production, thus protecting environment.
NOVELTY - Bio-fuel comprises 15-25 pts. wt. willow branches, 25-35 pts. wt. Sophora japonica branches, 11-18 pts. wt. large mustard straw powder, 10-16 pts. wt. sesame straw powder, 20-25 pts. wt. industrial ethanol, 40-55 pts. wt. biomass alcohol, 5-9 pts. wt. Pinus yunnanensis branches, 8-13 pts. wt. Pinus latteri branches, 15-25 pts. wt. dried coconut leaf twig, 15-25 pts. wt. garden burnet root branches, 15-25 pts. wt. Pinus latteri branches, 15-25 pts. wt. Chinese pine branches and, 15-25 pts. wt. pine branches.    USE - Used as a bio-fuel.    ADVANTAGE - The bio-fuel is environmental friendly (claimed); saves energy; has high calorific value; not only replaces renewable energy source completely, but also reduces discharge of carbon dioxide, sulfur dioxide and other harmful gases, and simultaneously utilizes biomass briquettes which solves the problem of large pile of straw in rural areas; and prevents the impact on landscape environment, and insecurity caused by fire.
NOVELTY - Biomass fuel comprises 15-20 pts. wt. industrial ethyl alcohol, 1-2 pts. wt. combustion improver, 5-10 pts. wt. broad bean straw powder, 45-55 pts. wt. wheat straw powder, 30-45 pts. wt. peanut straw powder, 10-15 pts. wt. mung bean powder, 35-45 pts. wt. cotton powder, 1 pts. wt. Chinese fir sawdust, 1 pts. wt. Chinese arborvitae sawdust, 15-20 pts. wt. coal powder, 15-20 pts. wt. mulberry sawdust, and 3-6 pts. wt. pine sawdust.    USE - Biomass fuel.    ADVANTAGE - The clean biomass fuel increases the carbon content of the fuel particles, while efficiently using coal waste, thus increasing the heat value and combustion time and reducing environmental pollution.
NOVELTY - A composite food waste crop straw biomass fuel comprises highland barley straw powder, broad bean straw powder, wheat straw powder, peanut powder, spidemoss herb, pine bar, beech tree, mangrove branch, oak tree branch, willow branch, anthracite coal, coal slurry, animal lipid, food garbage, camphor tree chips, oak tree chips, Buxus megistophylla powder, larch wood chips and pansy wooden chips.    USE - Composite food waste crop straw biomass fuel.    ADVANTAGE - The high-grade and environment-friendly biomass fuel is made from agricultural wastes which are deeply processed to convert into energy source. It does not easily loosen even with long-term storing, and does not add any chemical product. It uses pure natural plants.    DETAILED DESCRIPTION - A composite food waste crop straw biomass fuel comprises 20-35 pts. wt. highland barley straw powder, 30-45 pts. wt. broad bean straw powder, 55-60 pts. wt. wheat straw powder, 30-40 pts. wt. peanut powder, 9-13 pts. wt. spidemoss herb, 10-16 pts. wt. pine bark, 5-10 pts. wt. beech tree, 5-10 pts. wt. mangrove branch, 5-10 pts. wt. oak tree branch, 5-10 pts. wt. willow branch, 20-30 pts. wt. anthracite coal, 25-30 pts. wt. coal slurry, 15-25 pts. wt. animal lipid, 5-15 pts. wt. food garbage, 9-16 pts. wt. camphor tree chips, 8-13 pts. wt. oak tree chips, 10-15 pts. wt. Buxus megistophylla powder, 11-13 pts. wt. larch wood chips and 4-7 pts. wt. pansy wooden chips.
NOVELTY - Biomass granule fuel 25-30 pts. cotton straw powder, 35-55 pts. oilseed straw powder, 15-25 pts. green vine straw powder, 15-20 pts. large mustard straw powder, 25-30 pts. duck manure, 12-20 pts. goose droppings, 10-15 pts. pig manure, 9-16 pts. cypress wood, 1-3 pts. bungeana sawdust, 11-18 pts. Grevillea branches, and 14-30 pts. willow tree stem.    USE - Used as a biomass granule fuel.    ADVANTAGE - The fuel uses wide raw material sources, has prolonged combustion time and greatly enhanced heat value.
NOVELTY - Biomass fuel comprises 23-40 pts. wt. biomass alcohol, 30-46 pts. wt. oil seed straw powder, 19-26 pts. wt. vine green straw powder, 10-15 pts. wt. hemp straw powder, 20-30 pts. wt. sunflower straw powder, 35-45 pts. wt. castor straw powder, 16-25 pts. wt. rice hull powder, 30-45 pts. wt. peat, 40-65 pts. wt. coal powder, 55-60 pts. wt. mulberry branch, 6-13 pts. wt. pine oil, and 7-10 pts. wt. pine branch.    USE - The biomass fuel is useful for a boiler used in canteen, restaurant and hotel.    ADVANTAGE - The biomass fuel is safe to use, can not explode easily during storage and transportation, and replaces the use of a diesel oil or heavy oil with raw material such as by-product of factory leftovers and waste, thus reducing cost and saving resource.
NOVELTY - A biological fuel particle comprises 33-46 pts. wt. aqueous sticky rice straw powder, 40-55 pts. wt. corn straw powder, 5-10 pts. wt. birch branch, 20-30 pts. wt. corn straw powder, 10-25 pts. wt. soybean straw powder, 10-20 pts. wt. potato straw powder, 10-20 pts. wt. highland barley straw powder, 5-15 pts. wt. broad bean pole straw powder, 40-55 pts. wt. wheat straw powder, 5-9 pts. wt. baked pie, 5-10 pts. wt. chicken manure, 15-20 pts. wt. rice bran, 20-30 pts. wt. rice, 10-15 pts. wt. chicken manure, and 5-10 pts. wt. peat.    USE - Biological fuel particle (claimed).    ADVANTAGE - The fuel particle has high heat value and energy use rate, reduced ignition, good ventilation property, and increased combustion time, and avoids or reduces cooking oil and pig waste production and flow direction.
NOVELTY - A composite biomass fuel comprises furfural slag, Syzygium jambos branches, Davidia involucrata branches, Bombax ceiba branches, mulberry tree branches, dry pine tree branches, ebony tree branches, peach tree branches, oak tree branches, apricot tree branches, soybean straw powder, wheat straw, abamectin mixture, ammonium sulfate and monoammonium phosphate.    USE - Composite biomass fuel (claimed).    ADVANTAGE - The composite biomass fuel has excellent thermal stability and combustion efficiency, and is prepared by environmentally-friendly and economical process with reduced energy consumption.    DETAILED DESCRIPTION - A composite biomass fuel comprises 80-95 pts. wt. furfural slag, 4-8 pts. wt. Syzygium jambos branches, 9-16 pts. wt. Davidia involucrata branches, 8-13 pts. wt. Bombax ceiba branches, 11-17 pts. wt. mulberry tree branches, 15-20 pts. wt. dry pine tree branches, 1-3 pts. wt. ebony tree branches, 6-14 pts. wt. peach tree branches, 5-9 pts. wt. oak tree branches, 6-10 pts. wt. apricot tree branches, 55-60 pts. wt. soybean straw powder, 11-13 pts. wt. wheat straw, 0.001-0.003 pt. wt. abamectin mixture, 1-6 pts. wt. ammonium sulfate and 5-9 pts. wt. monoammonium phosphate.
NOVELTY - Biomass fuel comprises 80-95 pts. wt. furfural residue, 25-30 pts. wt. coal powder, 4-8 pts. wt. peach branch, 9-16 pts. wt. Davidia branch, 8-13 pts. wt. cotton branch, 11-17 pts. wt. mulberry, 15-20 pts. wt. pine branch, 1-3 pts. wt. sandalwood branch, 6-14 pts. wt. peach branch, 5-9 pts. wt. oak branch, 6-10 pts. wt. apricot branch, 11-21 pts. wt. coal slurry, 25-29 pts. wt. rice straw powder, 30-35 pts. wt. corn straw powder, 50-60 pts. wt. soybean straw powder, 14-20 pts. wt. rape cake, 14-23 pts. wt. rice bran, and 0.001-0.003 pts. wt. abamectin mixture.    USE - The biomass fuel is useful for microbial decomposition preparation (claimed).    ADVANTAGE - The biomass fuel: solve the direct combusting problem of furfural residue and low thermal efficiency of straw; increases the combustion efficiency; has low energy consumption property, low cost and pollution-free production process.
NOVELTY - Biomass fuel comprises 16-29 hemp pts. wt. straw powder, 15-20 pts. wt. mustard powder, 10-15 pts. wt. sesame powder, 14-16 pts. wt. sunflower pole powder, 5-9 pts. wt. biomass carbon, 1-2 pts. wt. chemical combustion improver, 3-5 pts. wt. coal, 10-15 pts. wt. poplar wood, 1 pts. wt. Chinese fir sawdust, 1 pts. wt. Chinese arborvitae sawdust, 15-20 pts. wt. coal gangue powder, 15-20 pts. wt. mulberry wood, and 3-6 pts. wt. pine.    USE - The biomass fuel is useful for vaporizing type burner (claimed).    ADVANTAGE - The high-efficient, eco-friendly and clean biomass fuel increases the carbon content of the fuel particles, thus increasing the combustion time of the burner.
NOVELTY - Artificial coal comprises 70-80 wt.% municipal solid waste, 10-20 wt.% nickel molybdenum alloy powder and 5-15 wt.% activated carbon.    USE - Used as artificial coal.    ADVANTAGE - The artificial coal: solves the shortage problem of natural coal resources; is close to natural coal in high thermal value, low moisture content and low ash content; is simple to prepare using less devices.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing artificial coal, comprising: (i) crushing all raw materials into powder; (ii) mixing the powder by stirring; (iii) adding the powder into the cavity of a pressing machine; (iv) vacuumizing with a vacuum degree of 100-500 Pa; (v) carrying out high temperature and pressure treatment at 150-250 degrees C with a pressure of 0.3-3 MPa for 0.5-3 hours; (vi) processing the material at 500-900 degrees C with a pressure of 0.3-3 MPa for 60-80 hours; and (vii) slowly reducing the pressure to 1 atmospheric pressure, and slowly cooling to room temperature.
NOVELTY - This new type utility claims one optimization of a heating and cooling, heating, heat, pneuma, five combined supplying system, comprising a operation room, the operating room comprising a solar energy device, a wind power generator, a combustion generation system, water cooling system and marsh gas ferment system, a solar energy device and wind power generator is set on the top of the straw burning generation system and storage device of a operation room is set a operation room, the underground water cold system is set a operation room, a marsh gas fermenting system is set a operation room, in the solar energy device comprising solar energy power generating plate and solar energy heat collecting pipe, marsh gas fermentation system comprising methane combustion generation device, a solar energy power generating plate, a wind power generator, a combustion energy-saving furnace with biomass straw generation system and methane combustion generation device and a storage device electric conduction connection. This system implementation for a renewable energy efficient a use, realize the diversification of energy use, which greatly reduces the dependence of for external energy, reduces the operation and maintenance of the cost.
NOVELTY - Preparing fatty acid enzyme composition comprises (a) mixing 40-50 wt.% grain byproduct, 40-50 wt.% sugar and 5-15 wt.% microorganism with water and fermenting to obtain liquid enzyme, and (b) mixing 25-35 wt.% liquid enzyme, 40-50 wt.% sugar, 45-55 wt.% fat and 5-15 wt.% microorganisms, and fermenting.    USE - The method is useful for preparing fatty acid enzyme composition (claimed).    ADVANTAGE - The composition has high energy value (claimed), which can be an alternative energy source to manage with global warming, thus reducing the usage of reduces the petroleum, refined oil, processed oil fuels; reduces the emission of carbon dioxide; decreases risks in oil reserves and risk of nuclear energy; and is environment-friendlily.
NOVELTY - Environmentally-friendly biofuel comprises 14-20 pts. green vine straw powder, 5-10 pts. Sophora japonica dry branch, 5-10 pts. beech tree dry branch, 5-10 pts. mangrove dry branch, 5-10 pts. oak tree dry branch, 5-10 pts. willow dry branch, 20-30 pts. anthracite, 25-30 pts. coal slurry, 55-60 pts. waste oil, 15-25 pts. animal fat, 5-15 pts. food waste, 8-13 pts. or 15-25 pts. Pinus latteri dry branch, 15-25 pts. olive dry branch, 15-25 pts. elm dry branch, 15-25 pts. Chinese pine dry branch and 15-25 pts. Korean pine dry branch.    USE - Used as biofuel.    ADVANTAGE - The biofuel is energy-saving with high heat productivity and reduces carbon dioxide, sulfur dioxide and other harmful gas discharge, and solves the problem of rural straw stack affecting the landscape environment.
NOVELTY - Green biomass fuel comprises 9-16 pts. wt. cypress wood, 1-3 pts. wt. bungeana sawdust, 10-15 pts. wt. hemp straw powder, 20-30 pts. wt. sunflower straw powder, 35-45 pts. wt. castor straw, 16-25 pts. wt. husk powder, 30-45 pts. wt. peat, 30-40 pts. wt. rice hull powder, 19-26 pts. wt. vine green rice stalk powder, 11-18 pts. wt. mustard straw powder, 10-16 pts. wt. flax straw powder, 20-25 pts. wt. industrial ethanol, 40-55 pts. wt. biomass alcohol, 5-9 pts. wt. South pine branches, 8-13 pts. wt. Pinus latteri branches and 7-10 pts. wt. Korean pine branches.    USE - The green biomass fuel is useful to replace diesel oil or heavy oil for collective canteens, restaurants, hotels, stoves and boilers.    ADVANTAGE - The green biomass fuel has high combustion efficiency and does not explode during storage and transport, hence safe. The raw materials for the green biomass fuel are left-overs from chemical plants, fertilizer plants, breweries, pharmaceutical factory, sugar wastes or their by-products, hence the resources are saved and cost-effective.    DETAILED DESCRIPTION - Green biomass fuel comprises 9-16 pts. wt. cypress wood, 1-3 pts. wt. bungeana sawdust, 10-15 pts. wt. hemp straw powder, 20-30 pts. wt. sunflower straw powder, 35-45 pts. wt. castor straw, 16-25 pts. wt. husk powder, 30-45 pts. wt. peat, 30-40 pts. wt. rice hull powder, 19-26 pts. wt. vine green rice stalk powder, 11-18 pts. wt. mustard straw powder, 10-16 pts. wt. flax straw powder, 20-25 pts. wt. industrial ethanol, 40-55 pts. wt. biomass alcohol, 5-9 pts. wt. South pine branches, 8-13 pts. wt. Pinus latteri branches, 6-13 pts. wt. Chinese pine branches and 7-10 pts. wt. Korean pine branches.
NOVELTY - Pyrolysis and liquefaction produced biomass fuel comprises 11-13 pts. wt. bagasse, 15-25 pts. wt. rice-rice straw powder, 65-70 pts. wt. soybean rice straw powder, 50-55 pts. wt. potato rice straw powder, 40-50 pts. wt. highland barley rice straw powder, 20-35 pts. wt. broad bean straw powder, 80-90 pts. wt. wheat straw powder, 20-25 pts. wt. pig fat, 10-16 pts. wt. coral branch, 9-13 pts. wt. Ginkgo branches, 10-15 pts. wt. wheat bran, 5-8 pts. wt. potato, 15-20 pts. wt. grain slag, 10-16 pts. wt. cassava residue, 5-12 pts. wt. rice straw, and 5-8 pts. wt. corn core.    USE - Used as pyrolysis and liquefaction produced biomass fuel.    ADVANTAGE - The fuel replaces conventional fuel oil, and has good industrialization prospect.
NOVELTY - A green one biomass fuel prescription comprises 30-46 pts. wt. oil seed straw stick powder, 19-26 pts. wt. vine green straw stick powder, 11-18 pts. wt. straw stick mustard powder, 10-16 pts. wt. sesame straw stick powder, 20-25 pts. wt. industrial ethyl alcohol, 40-55 pts. wt. biomass alcohol, 5-9 pts. wt. pine, 8-13 pts. wt. submicron pine, 6-13 pts. wt. pine oil, and 7-10 pts. wt. pine branch.    USE - A green one biomass fuel prescription for substitute diesel oil or heavy oil of collective canteen, restaurant, hotel, and boiler.    ADVANTAGE - Product reduces cost and saves resource.
NOVELTY - Environmentally friendly biofuel comprises 11-13 pts. wt. bagasse, 15-25 pts. wt. paddy straw powder, 20-30 pts. wt. corn straw powder, 10-25 pts. wt. soybean straw powder, 10-20 pts. wt. potato straw powder, 10-20 pts. wt. highland barley straw powder, 5-15 pts. wt. bean straw powder, 40-55 pts. wt. wheat straw powder, 1-2 pts. wt. cedar branches, 2-3 pts. wt. emulsifier, 4-6 pts. wt. methylhydroquinone, and 1-3 pts. wt. di-tert-butylhydroquinone.    USE - Used as environmentally friendly biofuel.    ADVANTAGE - The biofuel: utilizes the emulsifier for improving storage stability and liquidity of biomass pyrolysis oil; and has long-term storage stability and low pour point.
NOVELTY - A biomass fuel produced from liquefied agricultural waste comprises 15-20 pts. wt. industrial ethanol, 1-2 pts. wt. combustion improver, 5-10 pts. wt. bean straw powder, 45-55 pts. wt. wheat straw powder, 30-45 pts. wt. peanut straw powder, 10-15 pts. wt. mung bean straw powder, 5-9 pts. wt. rapeseed cake, 5-10 pts. wt. chicken manure, 15-20 pts. wt. rice bran, 10-15 pts. wt. wheat bran, 5-8 pts. wt. potato, 15-20 pts. wt. distillers grain residue, 10-16 pts. wt. cassava residue, 5-12 pts. wt. rice straw, and 5-8 pts. wt. corncob.    USE - A biomass fuel produced from liquefied agricultural waste (claimed).    ADVANTAGE - Biomass fuel produced from liquefied agricultural waste has good industrial prospects.
NOVELTY - A crop straw biomass fuel is prepared by using 55-70 pts. wt. straw powder, 17-23 pts. wt. soybean straw powder, 9-13 pts. wt. potato straw stick powder, 16-27 pts. wt. highland barley straw stick powder, 20-29 pts. wt. bean stick rice powder, 40-55 pts. wt. wheat rice powder, 16-29 pts. wt. peanut rice powder, 30-45 pts. wt. castor rice stick, 15-25 pts. wt. branch, 11-16 pts. wt. oak type branch, and 1-3 pts. wt. combustion improver.    USE - Preparation of crop straw biomass fuel for industrial boiler.    ADVANTAGE - Product is high grade fuel and reduces dust pollution and combustion cost.
NOVELTY - Biomass comprises barley straw powder, broad bean stalk powder, wheat straw powder, peanut straw powder, Juniperus chinensis branches, pine bark, fir branches, Moellendorf's spider moss herb, Chinese toon branches, oil seed rice straw powder, black walnut meal, lemon sawdust, Platanus orientalis wood meal, Davidia involucrata wooden meal, cotton wooden meal, kapok wooden meal and Bauhinia wooden meal.    USE - The biomass is useful in preparation of fuel (claimed).    ADVANTAGE - The biomass is: suitable in deep processing of agricultural waste into high-grade energy, and solid materials, and suitable for long-term storage, and environmental friendly; does not loosen easily, and contain any chemical products; and completely utilizes natural plant materials.    DETAILED DESCRIPTION - Biomass comprises 20-35 pts. wt. barley straw powder, 30-45 pts. wt. broad bean stalk powder, 55-60 pts. wt. wheat straw powder, 30-40 pts. wt. peanut straw powder, 9-13 pts. wt. Juniperus chinensis branches, 10-16 pts. wt. pine bark, 8-13 pts. wt. fir branches, 4-19 pts. wt. Moellendorf's spider moss herb, 5-10 pts. wt. Chinese toon branches, 19-26 pts. wt. oil seed rice straw powder, 3-5 pts. wt. black walnut meal, 4-8 pts. wt. lemon sawdust, 6-19 pts. wt. Platanus orientalis wood meal, 9-19 pts. wt. Davidia involucrata wooden meal, 9-16 pts. wt. cotton wooden meal, 3-8 pts. wt. kapok wooden meal and 4-7 pts. wt. Bauhinia wooden meal.
NOVELTY - Biomass fuel comprises 80-95 pts. wt. furfural slag, 25-32 pts. wt. coal slurry, 30-40 pts. wt. rice straw powder, 44-50 pts. wt. corn straw powder, 50-60 pts. wt. soybean straw powder, 14-23 pts. wt. rice bran, 11-13 pts. wt. wheat straw, 0.001-0.003 pts. wt. avermectin mixture, 1-6 pts. wt. ammonium sulfate and 5-9 pts. wt. monoammonium phosphate.    USE - Biomass fuel.    ADVANTAGE - The biomass fuel can be economically prepared with low thermal efficiency, increased combustion efficiency and low energy consumption and without pollution.
NOVELTY - Producing wood fuel, comprises (a) cutting the wood raw material having a length of 3 cm or less, (b) crushing the wood raw materials to form crude wood chip, (c) drying the crude wood chip until water content is 10-15% and then crushing, and (d) conveying the wood chips to a granulator and then granulating.    USE - The method is useful for producing wood fuel (claimed).    ADVANTAGE - The method is capable of simply preparing the wood fuel with reduced energy consumption, high automatic degree, and good stable property.
NOVELTY - A renewable crop straw biomass fuel contains 16-29 pts. wt. peanut straw powder, 30-45 pts. wt. castor straw, 55-70 pts. wt. corn straw powder, 65-70 pts. wt. soybean straw powder, 50-55 pts. wt. potato and rice straw powder, 40-50 pts. wt. highland barley rice straw powder, 20-35 pts. wt. broad bean rice straw powder, 80-90 pts. wt. wheat rice straw powder, 20-25 pts. wt. pig oil, 10-16 pts. wt. coral branch, 9-13 pts. wt. waste cooking oil, 11-16 pts. wt. industrial ethyl alcohol, 0.0001-0.0002 pt. wt. potassium germ powder, and 0.0001-0.0002 pt. wt. silicate powder.    USE - A renewable crop straw biomass fuel for industrial boiler.    ADVANTAGE - Fuel is clean and environment-friendly, reduces dust, combustion cost, and friction, enhances particle strength, and has high grade.    DETAILED DESCRIPTION - A renewable crop straw biomass fuel comprises 16-29 pts. wt. peanut straw powder, 30-45 pts. wt. castor straw, 55-70 pts. wt. corn straw powder, 65-70 pts. wt. soybean straw powder, 50-55 pts. wt. potato and rice straw powder, 40-50 pts. wt. highland barley rice straw powder, 20-35 pts. wt. broad bean rice straw powder, 80-90 pts. wt. wheat rice straw powder, 20-25 pts. wt. pig oil, 10-16 pts. wt. coral branch, 9-13 pts. wt. waste cooking oil, 11-16 pts. wt. industrial ethyl alcohol, 0.0001-0.0002 pt. wt. potassium germ powder, 0.0001-0.0002 pt. wt. silicate powder, 0.0001-0.0002 pt. wt. Bacillus cereus powder, and 1-3 pts. wt. combustion improver.
NOVELTY - Forest tree biofuel composition comprises 16-29 pts. wt. hemp straw powder, 15-20 pts. wt. mustard straw powder, 10-15 pts. wt. sesame straw powder, 14-16 pts. wt. sunflower straw powder, 5-9 pts. wt. biomass carbon, 1-2 pts. wt. chemical combustion improver, 3-5 pts. wt. coal, 10-15 pts. wt. poplar tree meal, 10-15 pts. wt. coconut tree meal, 10-15 pts. wt. garden burnet tree meal, 1-6 pts. wt. methyl alcohol and 9-16 pts. wt. ethyl alcohol.    USE - Used as forest tree biofuel composition.    ADVANTAGE - The composition discharges less amount of carbon monoxide, has low production cost, and utilizes biological sources which are widely distributed.
NOVELTY - A biofuel contains 13-25 pts. wt. oilseed straw powder, 14-20 pts. wt. green vine straw powder, 15-20 pts. wt. mustard straw powder, 10-15 pts. wt. sesame straw powder, 14-16 pts. wt. sunflower straw powder, 5-9 pts. wt. biomass carbon, 1-2 pts. wt. chemical combustion improver, 3-5 pts. wt. coal, 10-15 pts. wt. poplar wood chip, 10-15 pts. wt. olive wood chip, 10-15 pts. wt. elm wood chip, 9-16 pts. wt. camphor wood chip, 8-13 pts. wt. tussah wood chip, 10-15 pts. wt. Buxus megistophylla wood chip, and 12-16 pts. wt. Herba schizonepetae wood chip.    USE - A biofuel (claimed).    ADVANTAGE - Process is simple, product is safe and environment-friendly, and raw material is easy to get.    DETAILED DESCRIPTION - A biofuel comprises 13-25 pts. wt. oilseed straw powder, 14-20 pts. wt. green vine straw powder, 15-20 pts. wt. mustard straw powder, 10-15 pts. wt. sesame straw powder, 14-16 pts. wt. sunflower straw powder, 5-9 pts. wt. biomass carbon, 1-2 pts. wt. chemical combustion improver, 3-5 pts. wt. coal, 10-15 pts. wt. poplar wood chip, 10-15 pts. wt. olive wood chip, 10-15 pts. wt. elm wood chip, 9-16 pts. wt. camphor wood chip, 8-13 pts. wt. tussah wood chip, 10-15 pts. wt. B. megistophylla wood chip, 11-13 pts. wt. larch wood chip, 12-16 pts. wt. H. schizonepetae wood chip, 12-18 pts. wt. masson pine wood chip, and 11-15 pts. wt. Pinus kesiya wood chip.
NOVELTY - Bio-fuel comprises 5-10 pts. wt. birch branches, 5-10 pts. wt. Sophora japonica branches, 55-70 pts. wt. corn stalk powder, 17-23 pts. wt. soybean straw powder, 9-13 pts. wt. potato stalk powder, 16-27 pts. wt. highland barley straw powder, 20-29 pts. wt. broad bean stalk powder, 9-16 pts. wt. kapok wood meal, 3-8 pts. wt. kapok wood meal, 12-16 pts. wt. herba schizonepetae chip, 12-18 pts. wt. pine wood meal and 11-15 pts. wt. Simao pine wood meal.    USE - Used as a bio-fuel.    ADVANTAGE - The bio-fuel is environmental friendly; has easily available raw materials, and simple preparation process; and can replace traditional fuel.
NOVELTY - Biomass fuel comprises 25-30 pts. wt. cotton straw pole powder, 35-55 pts. wt. rice straw powder, 15-25 pts. wt. vine green rice straw powder, 15-20 pts. wt. mustard stick rice powder, 25-30 pts. wt. duck manure, 12-20 pts. wt. goose dung, 10-15 pts. wt. pig manure, 9-16 pts. wt. Juniperus cypress meal, 1-3 pts. wt. Pinus bungeana sawdust, 1 pts. wt. Cunninghamia lanceolata wood, 1 pts. wt. arborvitae wood, 15-20 pts. wt. coal powder, 15-20 pts. wt. mulberry, and 3-6 pts. wt. pine.    USE - The biomass fuel is useful for producing coal.    ADVANTAGE - The biomass fuel is eco-friendly, and has increased carbon content and heat value and prolonged combustion time.
NOVELTY - A crop straw biofuel comprises 17-23 pts. wt. soybean straw powder, 9-13 pts. wt. potato straw powder, 16-27 pts. wt. highland barley straw powder, 20-29 pts. wt. broad bean straw powder, 40-55 pts. wt. wheat straw powder, 16-29 pts. wt. peanut rice straw powder, 30-45 pts. wt. castor rice straw, 15-25 pts. wt. poplar branch, 15-25 pts. wt. dry olive branch, 15-25 pts. wt. elm branch, 15-25 pts. wt. Pinus latteri branch, 15-25 pts. wt. pine oil, and 15-25 pts. wt. pine branch.    USE - A crop straw biofuel (claimed).    ADVANTAGE - Biofuel is energy-saving and environment-friendly, replaces non-renewable energy, reduces carbon dioxide and sulfur dioxide, and has high heating value.
NOVELTY - Biological fuel composition comprises 16-29 pts. hemp straw powder, 33-46 pts. sunflower rice straw powder, 40-56 pts. rice husk powder, 15-30 pts. soybean rice straw, 10-16 pts. peat, 20-23 pts. Bauhinia branches, 11-17 pts. Albizia saman dry twigs, 5-9 pts. cortex albiziae branch, 1-3 pts. Patrinia scabiosaefolia branches, 5-9 pts. isopropyl alcohol, 5-8 pts. tert-butanol, 1-6 pts. methyl alcohol and 9-16 pts. ethyl alcohol.    USE - Used as a biological fuel.    ADVANTAGE - The fuel emits less carbon monoxide, has low production cost, and uses widely available biological sources.
NOVELTY - A cleaned biomass fuel comprises 10-16 pts. wt. ethyl alcohol, 25-30 pts. wt. coal powder, 4-8 pts. wt. Syzygium branch, 9-16 pts. wt. Davidia branch, 8-13 pts. wt. cotton branch, 11-17 pts. wt. mulberry, 15-20 pts. wt. pine branch, 1-3 pts. wt. dried sandalwood branch, 6-14 pts. wt. peach branch, 5-9 pts. wt. oak branch, 6-10 pts. wt. apricot branch, 55-60 pts. wt. soybean rice straw powder, 25-40 pts. wt. potato rice straw powder, 30-45 pts. wt. highland barley rice straw powder, 23-46 pts. wt. broad bean rice straw powder, and 45-50 pts. wt. wheat rice straw powder.    USE - A cleaned biomass fuel (claimed).    ADVANTAGE - Fuel is low cost and environment-friendly, prolongs combustion period, improves thermal efficiency, reduces emission of concentrated sulfur dioxide and carbon dioxide, and has light weight and high heating value.
NOVELTY - Biomass fuel comprises 55-70 pts. wt. straw powder, 65-70 pts. wt. soybean straw powder, 50-55 pts. wt. potato straw powder, 40-50 pts. wt. highland barley straw powder, 20-35 pts. wt. broad bean straw powder, 80-90 pts. wt. wheat straw powder, 20-25 pts. wt. pig lipid, 10-16 pts. wt. coral branches, 9-13 pts. wt. Gingko, 11-16 pts. wt. oak, and 1-3 pts. wt. combustion improving agent.    USE - The biomass fuel is useful for industrial boiler.    ADVANTAGE - The biomass fuel has reduced dust pollution, combustion cost and energy consumption.
NOVELTY - Biofuel composition comprises 80-60% of diesel oil and 20-40% of essential oil, where the essential oil is blended with diesel oil to decrease consumption of fuel, such as for 15 kg load decrease of fuel is up to 0.00-0.22 l/hour.    USE - The biofuel composition is useful as a source of energy for compression-ignition engine (claimed).    ADVANTAGE - The biofuel composition is capable of effectively controlling the carbon emission by 40-50%, boosting and increasing energy/calorie power of fuel for better performance, improving smooth running and purity of fuels, and reducing noise and maintenance. The composition is eco friendly, cost savings, labor savings, better heat and more purity of fuel, controls pollutions of furnace to improve the internal environment of production plant, and saves other equipments uses for fresh air and dusting level. The bio fuel composition: does not contain any ester products and does not form gel or clouding at -10 degrees C; does not involve any process like transesterification which brings more water into the biofuel; does not contain glycerol; does not cause significant decrease in fuel efficiency when compared to petroleum products, preferably produces comparable or improved fuel efficiency; and decreases wear and tear on engine and produces less noise.
NOVELTY - This new utility model claims of one of organic solid waste high temperature carbonization and heat recovery can use system, preheat includes heating device and cooling device, the heating device comprises preheat preheat heating cavity, heating pipe and waste preheat spiral conveyor, preheat heating pipe connected with waste feedstock tube and pipe connected with waste feedstock for hopper, preheat heating pipe connected with waste discharging pipe, cooling device comprises cooling cavity, cooling pipe, carbide feedstock tube, for carbide hopper, discharging carbonized and carbonized tube spiral conveyor, preheat the heating cavity top provided with cold air outlet and cold air outlet connected with fan is connected with cold air import, cooling cavity body top set with hot air outlet, the hot air outlet connected with hot air import. This new utility model and existing technology compared with the advantages as: finish hot can again use, reducing the dust pollute, water resource waste, prolongs the use life, at the same time reducing solid waste treatment process cost and process again, saving to can reducing arrange.
NOVELTY - This utility new type claims a new-type one anaerobic reactor, wherein, comprising: one the bottom of the anaerobic reactor, the anaerobic reactor set with one water distribution system for a water from lower to upper in turn one anaerobic reactor reaction area set with the anaerobic reactor inner, one said pneuma., one solid-liquid separating module, one pneuma biogas collecting system, set with external water circulation system, the circulation pump use the process the water is re-returns to the anaerobic reactor. This new-type anaerobic reactor the application range is wide, and it is very fit b industrial waste water treatment. A condition using a sludge or anaerobic flocculent sludge operation, degassing precipitation module is based on a design, this precipitate can be turbulence in a flow of the gas under the water and separating sludge and water circulation system the slurry fully mix, so as to ensure efficient. Relative low volume load and optimization of a degassing precipitation system, ensuring stable operation and anaerobic sludge is increased, without operation not visible, without need to maintain, a short time, control operation is simple, which can satisfy for odor, sludge yield and purification level is a more severe.
NOVELTY - This utility new type relates to one standard of a smoldering fuel, is placed in a box body inner smoldering, wherein, smoldering fuel layer is a standard paving a smoldering inner box body, fuel smoldering of the standard comprise biomass fuel layer and catalytic filter layer, wherein, the biomass fuel layer thickness is more than 30, the catalyst filter layer is biomass ash, the thickness is 5-6 cm. This utility new type is in fuel comprising catalytic filter layer, it can remove tar and a non-combustible substance in the smoke, the smoldering is more clean, process is easier to control.
NOVELTY - This utility new type claims a one full automatic straw granule fuel forming machine, comprising: a primary screen of the first raw material feeding device, a raw material fully stir mix a second feeding device, granulating device, a packing device of storage screen device, and a finished fuel product is a fuel, this forming machine from feeding, screen, stir, to screen a a product package, a completely automatic, it can process mass production, reduces the manpower and material resources.
NOVELTY - This new type utility claims one a biomass gasification furnace combustion chamber, it comprising parallel lower part of gasification room and burning room, gasification room and burning room is set with connected port, lower part is in furnace grate z pneuma, pneuma for furnace grate z of gasification room is under the first dust room, the first dust room set with air door or drawer-type cinder box, gasification room side and/or is set with sealed furnace door, lower part of burning room is burning grate, lower grate is second ash room, ash room set with second door or drawer type ash box, burning room upper part set with smoke outlet, wherein the boiler and furnace cover. It has simple structure, convenient use, complete combustion, heat efficiency is high.
NOVELTY - One small biomass gasification of cold heat connect power supply system, it comprising biomass gasification furnace, heat pipe type gas-liquid heat exchanger, hot water smoke direct, internal combustion engine, domestic hot water tank, spiral blade type add material device and temperature control system, said temperature control system comprises temperature sensor, single chip machine, module converter, the first number mould converter and the second number mould converter of biomass gasification furnace by pipeline orderly connected heat pipe type gas-liquid heat exchanger, gas purification device, blower and gas storage device. This new utility model system reasonable configuration, can full play to middle low temperature waste heat is on, implementation of step of using energy principle, increase of energy using rate of system.
NOVELTY - The split portable biomass gasification furnace has gas-solid feeding interaction device (11) having gas flow rate regulating button, direct current power source, gas flow rate sensor, centrifugal fan (12), feeding blade, and stepping motor. The feeding blade is connected to motor which is connected to sensor connected across power source via switch. The positive end and middle end of regulating button interface are connected to positive and negative terminals of power source. The centrifugal fan is connected to negative end and middle end of regulating button interface.    USE - Split portable biomass gasification furnace used outdoor for cooking, warning and shower by e.g. sports player.    ADVANTAGE - The whole gasification furnace is convenient to put in vehicle back-up tank. The gasification furnace has low investment cost, simple operation, stable structure, convenient mounting operation, and suitable wide range. The gasification furnace saves energy and is environment friendly. Avoids easy ignition under negative pressure, and also voids gas leakage. Reduces discharge of pollution substance by mounting a filter that removes gas impurity and ash to gas pipeline, and, at the same time increases capacity of combustible gas. Protects ecological environment when used outdoor. Saves fuel, and, at the same time, enables continuous biomass feeding.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the split portable biomass gasification furnace.    Biomass storage hopper (6)    Solid feeding connecting pipe (7)    Gas-solid feeding interaction device (11)    Centrifugal fan (12)    Ignition device (15)
NOVELTY - Tetraselmis species MBEyh04Gc strain preserved under a number KCTC 12432BP, is new.    USE - The Tetraselmis species MBEyh04Gc strain is useful for producing biodiesel (claimed).    ADVANTAGE - The Tetraselmis species MBEyh04Gc strain can be rapidly grown at low temperature.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) a composition for producing biodiesel comprising Tetraselmis species MBEyh04Gc strain as an active ingredient; and (2) method for producing biodiesel comprising inoculating Tetraselmis species MBEyh04Gc strain into a culture medium, cultivating strain under an optical irradiation, then collecting the cultivated strain, adding catalyst to the collected strain and converting fatty acid glycerol existing within the strain into fatty acid methyl ester.
NOVELTY - A Tetraselmis sp. MBEyh05Gc strain (KCTC 12433BP), is new.    USE - The Tetraselmis sp. MBEyh05Gc strain is useful in composition for producing biodiesel (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of manufacturing biodiesel, which involves inoculating the Tetraselmis strain into a culture medium, adding catalyst to the medium, culturing the strain under optical irradiation and converting fatty acid glycerol existing within the strain into the fatty acid ester.
NOVELTY - Dehydrating microalgae, comprises (a) performing one-dimensional centrifugation of the microalgae to obtain wet microalgae cells, (b) adding 1-3C lower alcohol to obtained wet microalgae cells, and stirring, and (c) performing two-dimensional centrifugation of alcohol treated microalgae, removing supernatant, and recovering dehydrated microalgae.    USE - The method is useful for dehydrating microalgae to produce biodiesel (all claimed), raw material of health functional food and feed of fish farm.    ADVANTAGE - The method dehydrates microalgae in simple and cost-efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing biodiesel, comprising (a), (b), (c) and (d) adding a catalyst to dehydrated microalgae, and converting glycerol fatty acid present in the microalgae to fatty acid esters.
NOVELTY - Method for enhancing soil microbial activity using organic fertilizer, involves (a) taking the rod-shaped fertilizer, forming ridges on a saline-alkali soil, and inserting the fertilizer into the soil to a length of 20 cm, (b) taking corn starch, adding the corn starch to water, heating at 70-75 degrees C for 1 hour, cooling to 45 degrees C, obtaining a paste, adding the paste to a spraying apparatus to spray under pressure on surface of the soil and forming a thin film, and (c) repeating the steps (a) and (b) once in every 20-25 days.    USE - The method is useful for enhancing soil microbial activity using organic fertilizer (claimed), and promoting growth of plant.    ADVANTAGE - The method is performed simply and conveniently, reduces salt content of soil, and enhances activity of microorganism and enzyme in soil.    DETAILED DESCRIPTION - Method for enhancing soil microbial activity using organic fertilizer, involves (a) taking the rod-shaped fertilizer, forming ridges on a saline-alkali soil, and inserting the fertilizer into the soil to a length of 20 cm, where length of exposed surface of the fertilizer is 1-2 cm, (b) taking corn starch, adding the corn starch to water, heating at 70-75 degrees C for 1 hour, cooling to 45 degrees C, obtaining a paste, adding the paste to a spraying apparatus to spray under pressure on surface of the soil and forming a thin film, and (c) repeating the steps (a) and (b) once in every 20-25 days. The fertilizer comprises mixture of acidic bentonite and sea clam shell powder in a mass ratio of 6:1, calcium propionate, accumulated spiral algae powder, dried dairy manure, wooden meal and food residue fermented product, phosphorus solubilizing bacteria and calcium phosphate fermenting bacteria. The mass ratio of wooden meal and food residue fermented product is 1:5.
NOVELTY - The device has a raw material inlet (1) that is connected with an air flow vortex crusher (2). An air blower (3) is connected with a filter (4) connected with a sedimentation pipe (5). The sedimentation pipe is arranged opposite to an oil receiver (10) in a tar depositing pool (7). A heating device (6) is located in the inner wall of tar depositing pool. A hoisting machine (8) is connected with the oil receiver and controlled by a drive device (9).    USE - Tar reduction device used in coking industry, for preparing biomass active carbon.    ADVANTAGE - The tar reduction device featured with simple structure, convenient mounting property, high tar removing efficiency, less use cost, and less investment cost is obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the tar reduction device used for preparing biomass active carbon.    Raw material inlet (1)    Air flow vortex crusher (2)    Air blower (3)    Filter (4)    Sedimentation pipe (5)    Heating device (6)    Tar depositing pool (7)    Hoisting machine (8)    Drive device (9)    Oil receiver (10)
NOVELTY - Agent comprises 10-20 pts. wt. nitrifying bacteria, 15-30 pts. wt. denitrifying bacteria, 10-50 pts. wt. Bacillus, 5-20 pts. wt. enzyme, 5-15 pts. wt. lactic acid bacterium, 10-20 pts. wt. yeast, and 20-40 pts. wt. photosynthetic bacteria. A single inoculum/g in medium comprises not less than 200 million active bacteria. The lactic acid bacterium is Streptococcus, Lactobacillus and/or Bifidobacterium. The yeast is Geotrichum or Candida.    USE - The agent is useful for treating livestock and poultry wastewater using microorganism (claimed).    ADVANTAGE - The agent is cost-effective.
NOVELTY - Method for treating disposed sewage sludge from konjac powder manufacturing industries, involves performing centrifugal dewatering of sewage sludge, drying sludge under sun at 80 degrees C, crushing dried sludge into powder with particle size less than 20 mesh, blending and pressing powder with humus in a weight ratio of 1:3, and mixing the mixture with soil.    USE - The method is useful for treating disposed sewage sludge from konjac powder manufacturing industries which is useful in soil for planting peony, rose and jasmine (claimed).    ADVANTAGE - The method prevents environmental pollution.
NOVELTY - Combusting household biomass involves feeding household biomass into a pyrolyzing reactor, where the pyrolysis of household biomass is performed at high temperature to obtain hot gas and carbon. The hot gas is stored in a waste heat recovery device.    USE - Method for combusting household biomass (claimed).    ADVANTAGE - The household biomass combusting method is suitable for farming.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a stove for combusting household biomass, which comprises a pyrolyzing reactor and combustion outlet that is connected to a gas cooker.
NOVELTY - A gas burning method involves taking dairy manure, drying and dehydrating dairy manure. The 60-90 wt.% dehydrated manure is added with 10-20 wt.% rice hull to obtain a mixed substance. The mixed substance is burned in a combustion furnace to obtain combustion gas. The produced combustion gas is cooled to remove dust, followed by removing impurities and tar to produce required gas.    USE - Method for burning gas of cow dung for use in power generation.
NOVELTY - The furnace has a furnace body provided with a high temperature resistant add material cover (2). A high temperature resistant seal ring is fixed with an upper part of a low temperature resistant add material cover (3). The low temperature resistant add material cover is fixed with a spiral pressure material pole (1). A pressure material disk (4) is fixed with a bottom part of the furnace body that is connected with a burner air inlet disk (6). A tar filter device is provided with a water-cooling tar filter (8) and a baffle plate type filter (18). A nozzle is connected with the air inlet disk.    USE - Biomass pneumatic furnace.    ADVANTAGE - The furnace has high combustion efficiency and prolonged service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass pneumatic furnace.    Spiral pressure material pole (1)    High temperature resistant add material cover (2)    Low temperature resistant add material cover (3)    Pressure material disk (4)    Burner air inlet disk (6)    Water-cooling tar filter (8)    Baffle plate type filter (18)
NOVELTY - A biomass coal-water slurry comprises feather hydrolyzate or feather hydrolysis sulfonated liquid, coal powder, and water in which dry mass ratio solid material in feather hydrolyzate or feather hydrolysis sulfonated liquid:coal powder is 0.15-1.5:100, biomass coal-water slurry has concentration of greater than or equal to 60 mass%, feather hydrolyzate is prepared by mixing 3-7 mass% sodium hydroxide, 20-35 mass% feather, and water and stirring and hydrolyzing at 60-90 degrees C for 2-10 hours, and feather hydrolysis sulfonated liquid is prepared by mixing 4-7 mass% sodium hydroxide with 5-12 mass% sodium sulfite.    USE - A biomass coal-water slurry (claimed).    ADVANTAGE - Biomass coal-water slurry is low-cost and reduces environment pollution.    DETAILED DESCRIPTION - A biomass coal-water slurry comprises feather hydrolyzate or feather hydrolysis sulfonated liquid, coal powder, and water in which dry mass ratio solid material in feather hydrolyzate or feather hydrolysis sulfonated liquid:coal powder is 0.15-1.5:100, biomass coal-water slurry has concentration of greater than or equal to 60 mass%, feather hydrolyzate is prepared by mixing 3-7 mass% sodium hydroxide, 20-35 mass% feather, and water and stirring and hydrolyzing at 60-90 degrees C for 2-10 hours, and feather hydrolysis sulfonated liquid is prepared by mixing 4-7 mass% sodium hydroxide, 5-12 mass% sodium sulfite, 17-25 mass% feather, and water, stirring, and hydrolyzing and sulfonating at 70-90 degrees C for 1.5-4 hours.
NOVELTY - Solid fuel is prepared by crushing biomass waste raw material to 2-30x 10-150x 10-30 mm, humidifying to moisture content of 15-50%, placing in steam explosion tank, sealing, introducing exogenous gas for 10-90 s to pressure of 0.5-2 MPa, introducing saturated steam for 0-60 s to pressure of 2-3 MPa, maintaining pressure for 2-20 minutes, opening dump valve to instantaneously release pressure, and extrusion molding in molding machine.    USE - Preparation of solid fuel (claimed).    ADVANTAGE - Preparation of solid fuel is simple, easy, and low-cost, has high efficiency, and saves energy.
NOVELTY - Preparation of fuel involves mixing palm oil with stearic acid to obtain primary mixture, adding glass fiber cotton, stirring the resultant product to obtain secondary mixture, providing the resultant product into mold, and cooling. The fuel comprises 40 wt.% palm oil, 40 wt.% stearic acid and 20 wt.% flame-resistant glass fiber cotton.    USE - Preparation of fuel used for ornamental lamp.    ADVANTAGE - The method economically provides fuel having excellent durability by safe process.
NOVELTY - A low-foaming water-based chain lubricant contains 1-4 mass parts fatty amine, 1-2 mass parts fatty amine polyoxyethylene ether, 0.1-1 mass part polyacrylamide, 0.1-5 mass parts fatty acid, 0.5-3 mass parts ether carboxylate, 0.1-5 mass parts bactericide, and 89-97.2 mass parts water.    USE - A low-foaming water-based chain lubricant (claimed).    ADVANTAGE - Process is environment-friendly and does not cause accumulation of foam, and product has no bubble, good bacteriostatic effect at relatively low concentration, hard water tolerance, and excellent lubricating performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of low-foaming water-based chain lubricant which involves adding fatty amine, fatty amine polyoxyethylene ether, and polyacrylamide into greater than or equal to 1/5 water, uniformly dispersing to obtain mixture, uniformly mixing fatty acid and ether carboxylate, adding into obtained mixture, stirring for 10-30 minutes to react completely, adding bactericide, uniformly stirring, adding remaining water, and uniformly stirring.
NOVELTY - Biodiesel preparation involves selecting methanol and lipid as raw materials and phosphotungstic acid ionic liquid as catalyst. The raw materials undergoes transesterification to obtain desired product.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method enables to prepare biodiesel in a simple and cost-effective manner.
NOVELTY - High clean vehicle M60-M85 methanol gasoline additive comprises 21-42 wt.% stabilizer, 12-32 wt.% combustion and antiknock agent, 11-28 wt.% energizer, 11-18 wt.% vapor pressure modulators, 4-19 wt.% antioxidants, 6-24 wt.% metal corrosion inhibitors and 5-18 wt.% rubber swelling inhibitor.    USE - High clean vehicle M60-M85 methanol gasoline additive.    ADVANTAGE - The product is environment-friendly.
NOVELTY - This utility new type belonging to the biomass energy regeneration technology field of environment engineering, relates to comprehensive use technology of biomass to prepare fuel and chemical raw material, especially one with a heat energy replacing function of biomass pyrolysis and gasification system, this system comprising pyrolyzing furnace, cooling device, pneuma liquid separating device, the oil liquid separating device, heat exchanger, a boiler, a water pump, water tank. This utility new type biomass pyrolysis of a gas for replacing liquefied petroleum gas, a rural areas provide a new clean high quality low cost of fuel gas, but also can be at the same time a high added value of the associated product wood carbon and pyroligneous, wood tar, wood and so on chemical raw material. Using the heat energy replacing technology, realize the heat can increase a use efficiency and reduces the heat energy loss. This utility new type for use rate of raw material is high, and without any three wastes.
NOVELTY - A fermentation fertilizer includes 75-80 pts. wt. urea, 2-3 pts. wt. xylitol, 10-12 pts. wt. locust bean powder, 2-4 pts. wt. bottle gourd tea, 1-3 pts. wt. garlic, 15-18 pts. wt. bentonite, 2-3 pts. wt. superphosphate, 4-5 pts. wt. potassium sulfate, 5-6 pts. wt. humic acid, 10-15 pts. wt. monoammonium phosphate, 1-2 pts. wt. potassium chloride, 0.4-5 pts. wt. sodium acetate, 1.4-1.7 pts. wt. magnesium sulfate, 8-9 pts. wt. soil nutrition agent, and 10-15 pts. wt. azotobacter fertilizer.    USE - Fermentation fertilizer.    ADVANTAGE - The fertilizer has increased utilization ratio and reduced dosage, improves quality of plant, and increases yield.    DETAILED DESCRIPTION - Fermentation fertilizer comprises 75-80 pts. wt. urea, 2-3 pts. wt. xylitol, 10-12 pts. wt. locust bean powder, 2-4 pts. wt. bottle gourd tea, 1-3 pts. wt. garlic, 15-18 pts. wt. bentonite, 2-3 pts. wt. superphosphate, 4-5 pts. wt. potassium sulfate, 5-6 pts. wt. humic acid, 10-15 pts. wt. monoammonium phosphate, 1-2 pts. wt. potassium chloride, 0.4-5 pts. wt. sodium acetate, 1.4-1.7 pts. wt. magnesium sulfate, 8-9 pts. wt. soil nutrition agent, 2-3 pts. wt. potassium dihydrogen phosphate,1.1-1.3 pts. wt. sodium, 0.6-0.7 pts. wt. ferrous sulfate, and 10-15 pts. wt. azotobacter fertilizer. An INDEPENDENT CLAIM is included for preparing the fertilizer comprising taking raw materials, adding purified water, adding xylitol, locust bean powder, bottle gourd tea root and garlic head, seal fermenting for 20-30 days at 60-65 degrees C, turning for 2-3 times, drying, adding urea and potassium fertilizer, stirring, adding bentonite, drying for 10-20 minutes, heating to 100-120 degrees C, adding calcium superphosphate, potassium sulfate, monoammonium phosphate, potassium chloride, sodium acetate, and magnesium sulfate, stirring, mix granulating, and drying to obtain the product.
NOVELTY - This utility new type claims a petrochemical industrial waste gas treatment system, comprising a fire arrestor, a bag-type dust remover, high temperature plasma device, the inside set with flame retardant, flame arrester set with side wall of valve, fire arrestor through opening flange and a pipeline, fire arrestor one side set with bag-type dust remover, a bag-type dust remover tank body set with several inner filter bag, filter bag is set with blowing nozzle, the blowing pipeline connected by the lower bag-type dust remover tank body set with discharge wherein, discharging discharging; wherein one side set with bag-type dust remover high temperature plasma device, a high temperature plasma box body is set with a bracket, the bracket is set with a multiple electrode, the upper part set with opening is convenient to a high frequency high voltage component and control circuit, high-temperature plasma device one side set with a draught fan, the draught fan and a gas discharging process, the utility model is new type structure is simple, technique process is reasonable, design characteristic is bright.
NOVELTY - Outside this utility new type claims a one from convection heat from hydrogen-oxygen generator, comprising shell, reactor, a multi-and a radiating heat pipe, a reactor set in the shell, and a reactor is connected the electrode extends out of the shell, a multi-radiating a heat pipe are connected and a housing, and uniform distribute in outside surface of the shell, the utility model is new type of convection from heat from hydrogen-oxygen generator, structure simple, volume is small, and a hydrogen in a hydrogen-oxygen gas mixture can form convection, heat radiating effect is good.
NOVELTY - The device has electrodes e.g. anode (4) and cathode (5), made of ferritic and magnetic stainless steel 430 with a galvanic potential of 0.5, or non-magnetic austenitic stainless steel 316 L or 304 L with a galvanic potential of 0.4. The electrodes are plunged in an insulating material vat (1) that is filled with a dielectric liquid, where the liquid comprises water and a specific additive. An electronic circuit delivers a square signal with microwave frequency that is lesser than 30 gigahertz. Plates (3) follow a specific polarization of an electrical circuit established during electrolysis.    USE - Device for production of a gas mixture of hydrogen and oxygen in an electrolysis cell for feeding a thermal engine and fossil energy consumer e.g. boiler and burner, in a car and a lorry (all claimed).    ADVANTAGE - The device optimally outputs a gas mixture of hydrogen and oxygen under reduced consumption of electric current and fuel and limited emission of unburnt residues and pollutants such as carbon monoxide and nitrogen oxides. The device is designed such that encrassage of combustion chambers, EGR valves-type equipment and an exhaust line is decreased.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a device for production of a gas mixture.    Insulating material vat (1)    Lid (2)    Plates (3)    Anode (4)    Cathode (5)
NOVELTY - This utility new type claims a ceramic one aeration bar, comprising: air branch pipe, wherein a position of the air branch pipe horizontal a, several air holes are arranged in straight line at the bottom of air branch pipe, air branch pipe at the bottom and a pneuma hole is corresponding to is set with a saddle, a saddle and this air branch pipe and set with check valve, and pneuma hole are connected, and connected with a saddle and saddle number corresponding to a rod in air aeration pipe, the aeration rod material is Al2O3. This utility new type using aeration rod using underneath type mounting, a condensing water can be in a air branch pipe, reduces the air resistance on the saddle in a check valve can effective prevent the sewage backflow, reducing the blocking probability of aeration rod, to Al2O3 as aeration rod material, which overcomes the defect of source aeration rod material, increase the use life of device. This utility new type has simple structure, without sewage backflow, a condensing water accumulate and so on, but also use motorized is small, charging efficiency is high, use life is long.
NOVELTY - This new type utility claims one use a rotary cement kiln waste incineration process of pre-processing system, in turn comprising a weighing platform, a bag breaking machine, primary, level one, level two screen machine and a processing system, cutting machine, cutting crusher, a crusher and magnetic separator; the a processing system comprising a system A and a system B; the processing system A and first-stage screening machine comprising a device and a device and connect the processing system B comprising a machine, a level and a screening machine and a drier and a crusher is. This utility new type use rotary cement kiln for incineration of garbage pre-processing process, the garbage a maximum use and burning of garbage is low water content, a high heat value combustible, resource recovery rate is high, energy-saving, clean and environment-friendly.
NOVELTY - This utility new type claims a one waste water processing system, comprising regulating pool, sludge, biochemical reaction pool, a sludge concentrate pool, outside discharging pool, a regulating pool, sludge, biochemical reaction pool, a discharging pool outside connecting in turn, a floatation and sedimentation with sludge discharging pipeline and the sludge concentrate pool is connected, a drain pipeline of the secondary sedimentation tank is set with a sludge reflux pipe, and a pipeline connected between the pool and the biochemical reaction pool connection, front end of the biochemical reaction pool set with strain culture tank, and biochemical reaction pool is connected, the utility model is new type of waste water processing system, set with a strain culture tank can be effective in provide a high-effect strain is biochemical reaction pool, instant culture, instant use, activity of strain, biochemical efficiency is high, a sink water outlet, a waste water degradation effect is good.
NOVELTY - This new utility model claims one kind of domestic garbage degradation device, comprising box and inner box set with degradable groove, heating heat preservation layer, set in device, temperature sensor, temperature sensor, deodorizing device, crushing device, discharge pump and stirring device, the stirring device comprises motor and electric machine through chain and connected with the stirring shaft, stirring shaft of crossed fixed with stirring rod, box frontage also provided with control room and automatic garbage conveying device, automatic garbage transfer device by motor for automatic transfer to kitchen garbage crushing device, the garbage crushing after enter into degrading groove degradation, deodorizing device and discharge pump used for purification and pump the waste gas and outlet device. When in use as long as using kitchen garbage already get in degrading groove and adding proper amount of degradation strain, can automatically control temperature and degradation can be hold in a certain of range slot inside, and automatically stirring, degrading, deodorizing and discharge, and more effective and environmental protection and method for organic waste transformation as organic fertilizer.
NOVELTY - This utility new type claims a corn straw in one whole stack collecting rotten plant structure, using the high temperature fiber decomposing a spore as corn straw rotten fungus, this method is selecting flat area in corn planting, after collecting the corn is corn straw according to entire alternately horizontal and vertical way of stacking, stacking corn straw is total height is 150 cm to 180 cm, the thickness of stacking in a stacking process is 25 cm to 35 cm time the pressing compact and uniform spreading the strain and urea in c, a fungus is corn straw weight is 1% to 3% and a urea is corn straw weight is 1.5% to 3%, each stack corn straw stacking weight is not less than 1000kg; then agricultural film use a cover, rear cover rock with the pressure compaction in the top, at the same time a hole of agricultural film is pressed in rock, water through adding water, composting time for 90 to 120 days. After using the method, a promoting mineralization of organic matter and humus, promote corn straw rotten, improve the compost quality.
NOVELTY - The aeration pipe is a multifunctional type aerobic compost reactor, comprising a end cover of a main body, , multifunctional aerating pipe, bracket and motor fixed in upper of bracket, said bracket comprising a support pedestal are symmetrically set with inserting part main body is set with a small hole in triangular support pole of support pedestal two side, and used for supporting a bracket of a the body of self-discharging device comprising a steering wheel, a gear, an aeration pipe used for comprising a main body end cover is inserted into the circular hole of outer pipe, used for inserting inner tube cavity of inner tube outside, outside pipe, inner pipe according to need. b is a is a different type of inner tube, the outermost end used for and set with a corresponding connecting device of rotary joint, inner pipe and the outside pipe there is a gap. This utility new type is time beneficial effect is: a the compost material rapid, cabin, a timing for oxygen, quantitative water supplement, sampling a real-time temperature measuring function, increase the efficiency and accuracy of scientific research test.
NOVELTY - This utility new type provide a one for sludge treatment of tower-type gravity reverse turning bed sludge aerobic compost device, comprising frame, inner the upper frame set with two rows fermentation tank and each row fermentation tank set with multiple layer fermentation chamber, the fermentation chamber bottom by several spliced into reverse turning bed, reverse turning bed one end through a bearing base support in a frame, and the other end through a base supporting a frame after a and a turning control device, two side frame set with a air blower and draught fan, a lower distributing plate of the material a the inner to each row fermentation tank top fermenting chamber is, material of inner top fermenting chamber through the raking device is set on a frame of the uniform distribute to the upper plate, and a material of a plate through plate control device a layer of inner fermenting chamber to ferment. This utility new type device automatic degree high, full automatic finish the whole cloth and process of fermenting, low energy consumption, small floor area, short construction period short, working environment is greatly improved, and strong practicability, which is good for large-range popularization and application.
NOVELTY - This utility model claims a large industrial marsh gas secondary fermentation device. It comprises in turn connected a yellow/green storage and oxygen supplying system for garbage fermentation device, in pre-processing temperature hydrolyzing jar, first-stage temperature in Anaerobic fermenting gas generating jar and a normal temperature level Anaerobic fermenting gas generating jar, wherein, in temperature hydrolyzing pre-processing tank top equipped with a stir, first-stage temperature in Anaerobic fermenting gas generating jar is equipped side stir device, a water heating device and double-pneuma cabinet, a normal temperature level Anaerobic fermenting gas generating jar is equipped double pneuma. This utility model is set a level fermentation jar, heat preservation is not only hot water with setting temperature and stir device, which not only can fully use of marsh gas fermenting raw material, but also can fully use residual heat in a first-stage fermentation, and to make the volume production rate of biogas fermentation jar holding a high comparison is at the same time the yield of marsh gas raw material by a common 65% increase to 85%. This utility model whole set technology is simple and reliable, it is easy to realize large industrial production, agricultural straw is a supply of one of a simple and easy method.
NOVELTY - This utility model relates to a manufacturing field, especially claims a household garbage recovery and using device, the structure comprises: decomposing device, connecting device and storage device, comprising a garbage entrance, entrance valve, jar, temperature controller, pressure controller I,wherein a valve, a device comprises a tube and a tube valve, storage device comprises storage jar, pressure controller II, an air outlet, an air outlet valve. After domestic garbage by garbage entrance entering into the decomposition jar, a temperature regulating temperature to produce the marsh gas and organic matter, through a pipe enter into marsh gas in storage jar, and then conveying to as living life energy use, organic garbage through a transportation to farmland in wherein as organic fertilizer by use of air storage jar. This advantages of utility model is: a household garbage for volume reduction, decrement, and increasing waste as resource circulation use or the use of value, improve the ecological environment and investment environment.
NOVELTY - A recombinant beta -glucosidase protein variant, is new. The beta -glucosidase protein variant comprises first segment having at least 26% sequence identity to GH3 domain consensus sequence having a 226 amino acid sequence (SEQ ID NO: 53) all fully defined in the specification and second segment having at least 19% sequence identity to GH3-C domain consensus sequence having a 211 amino acid sequence (SEQ ID NO: 54) all fully defined in the specification.    USE - The recombinant beta -glucosidase protein variant is useful for producing soluble sugars from cellulosic biomass.    ADVANTAGE - The recombinant beta -glucosidase protein variant has enhanced thermoactivity compared to naturally occurring proteins.    DETAILED DESCRIPTION - A recombinant beta -glucosidase protein variant, is new. The beta -glucosidase protein variant comprises first segment having at least 26% sequence identity to GH3 domain consensus sequence having a 226 amino acid sequence (SEQ ID NO: 53) all fully defined in the specification and second segment having at least 19% sequence identity to GH3-C domain consensus sequence having a 211 amino acid sequence (SEQ ID NO: 54) all fully defined in the specification, where the beta -glucosidase protein variant is catalytically active and comprises one or more residues chosen from (a) sequence having alanine residue at position 104 of SEQ ID NO:1 (sequence not defined in the specification), (b) sequence having leucine residue at position 157 of SEQ ID NO: 1, (c) sequence having isoleucine residue at position 210 of SEQ ID NO: 1, (d) sequence having alanine residue at position 485 of SEQ ID NO: 1, (e) sequence having alanine residue at position 572 of SEQ ID NO: 1, and (f) sequence having tyrosine residue at position 649 of SEQ ID NO: 1.
NOVELTY - The method involves providing acetoacetate and methanol into an esterification kettle. The methyl acetoacetate is over flown into a heat preservation kettle from a heat transfer groove. The crude acetoacetate and methanol is transferred into a rectifying tower from the heat transfer groove by a pump. The vacuum degree of the rectifying tower is increased to obtain the finished product under a certain return status. The top end of rectifying tower is rectified for discharging the residue.    USE - Method for continuously producing methyl acetoacetate used in pesticide industry and pharmaceutical industry.    ADVANTAGE - The work efficiency is improved so that the the productivity of methyl acetoacetate is increased. Hence the steam energy consumption is reduced, and device investment is saved.
NOVELTY - Special organic fertilizer comprises vegetable oil cake, cow dung, quail manure, calcium magnesium phosphate and biological culture. The special organic fertilizer is prepared by mixing vegetable oil cake, cow dung and quail manure, adding biological culture to the mixture, stirring mixture, maintaining moisture content of the mixture at 45-48%, fermenting mixture, turning mixture, maintaining moisture content of the mixture, adding crushed calcium magnesium phosphate to the mixture, screening mixture, and finally preparing into powder or granulating mixture.    USE - The special organic fertilizer is useful for tobacco (claimed).    ADVANTAGE - The special organic fertilizer increases organic matter content in soil.    DETAILED DESCRIPTION - Special organic fertilizer comprises 25-40 wt.% vegetable oil cake, 30-50 wt.% cow dung, 10-20 wt.% quail manure, 10-25 wt.% calcium magnesium phosphate and 1-5 wt.% biological culture. The special organic fertilizer is prepared by mixing vegetable oil cake, cow dung and quail manure, adding biological culture to the mixture, stirring mixture, maintaining moisture content of the mixture at 45-48%, fermenting mixture under aerobic conditions for 20 days, turning mixture, maintaining moisture content of the mixture to 25%, adding crushed calcium magnesium phosphate to the mixture, screening mixture, and finally preparing into powder or granulating mixture.
NOVELTY - This utility new type relates to a one engineering wound plant ecological restoration system, category repairing wound surface engineering technology field. The characteristic is: a soil layer, nutrient medium. The soil layer comprising two layer of the bottom layer soil by arbor, shrub, is according to 4: 2: peat soil of proportion 1 of, soil layer thickness is 20 to 30cm; soil layer is cover low volume weight, high porosity, without degradation of clay soil or adding high quality soil is soil modifying agent, soil layer thickness is 20 to 35 cm. The nutrition base of a following component mixture of (weight percentage): fungus dreg 60 to 70% of peat, 10 to 20% degrees centigrade, crushing-shaped crop straw, 10 to 20% of farm fertilizer, 5 to 10% of additive composition 5 to 10%, wherein peat and dreg in water content between 10 to 15%, a is less than 2 cm, water content of farmyard manure in 10 to 15%. The nutrition base is set in the bottom layer of soil and the table of earth intermediate layer, thickness is 15 to 20 cm. After this utility new type, contributing the rainfall with anti-corrosion, firm and vapour-permeable and the natural soil is close is a nutrient, inner short engineering wound can recover soil nutrient, recovering engineering a wound.
NOVELTY - This utility new type belongs to the field of chemical device technology field, especially relates to a one fertilizer production dust-removing device, comprising granulation tower and settling chamber, the top part of the granulating tower set with tail pneuma, tail pneuma discharge port through the pneuma the tail tube and the top of the depositing room is connected, the tail pneuma outlet pipe extends into the settling chamber, lower part of the sedimentation room set with dust inlet, the sedimentation room side upper part is set with gas mixture outlet, a sedimentation room is outside side wall and a gas mixture outlet is corresponding to is set with a buffering jar, a gas mixture outlet connected said buffer jar is in upper part, the top part of the buffering jar set with close cover, the bottom of the buffering jar set with the water pipe, the lower side the buffer jar is set with gas outlet pipe part. This fertilizer production dust-removing device, the design is reasonable, operation is convenient to use the waste resource, saves the cost, but also increase the dust removing effect and reduces the environment pollution.
NOVELTY - The device has a sequencing batch sewage processing pool (4) fixed with a sludge concentration meter (14). The sequencing batch sewage processing pool is connected with a DA/AD data converter (20) through a cable. The DA/AD data converter is connected with a PLC control cabinet (21) through the cable. The PLC control cabinet is connected with a remote control computer (22) through an Ethernet. A bottom part and a side wall of the sequencing batch sewage processing pool are fixed with a diving stirrer (12).    USE - Real time control sequencing batch sewage treatment device.    ADVANTAGE - The device enables effectively determines characteristic point instrument detection data in real time, effectively prevents aeration in real time, and reduces aeration time so as to save sludge expansion and electric energy waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic block diagram of a real time control sequencing batch sewage treatment device.    Sequencing batch sewage processing pool (4)    Diving stirrer (12)    Sludge concentration meter (14)    DA/AD data converter (20)    PLC control cabinet (21)    Remote control computer (22)
NOVELTY - Method for producing fat/oil component, involves culturing salt-tolerant alga in culture medium, where salt concentration of the culture medium is increased in stepwise manner.    USE - The method is useful for producing fat/oil component which is used for preparing high-class unsaturated fatty acid, preferably oleic acid or linolenic acid (all claimed), and as fuel and chemical raw material.    ADVANTAGE - The method enables production of the fat/oil component with high productive efficiency up to 183.9 mg/l/day, as concentration of the salt in the culture medium is increased in a stepwise manner and not randomly that in turn improves proliferation efficiency of the Chlamydomonas in the culture medium in controlled manner, as compared to existing methods.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing high-class unsaturated fatty acid, which involves hydrolyzing the fat/oil component produced by the above-mentioned method (M1).
NOVELTY - A poultry droppings turning rake roller comprises turn rake teeth set (1), outer retainer ring (2), limiting wheel (3), retaining ring (4), left and right side plates (5), nylon lining, inner retainer ring, transverse rods, roller, fixed plate, turn rake teeth, toothholder, clamp tooth plate and long head.    USE - Poultry droppings turning rake roller.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of poultry droppings turning rake roller.    Turn rake teeth set (1)    Outer retainer ring (2)    Limiting wheel (3)    Retaining ring (4)    Left and right side plates (5)
NOVELTY - Leaves processing system comprises a crushing device (1), a sieving device (2), a collecting pool (3), a cleaning pool (4), a sterilizing pool, and a packing device, and further comprises a fermenting pool (5).    USE - Used as leaves processing system.    ADVANTAGE - The system has simple structure, is easy to use, safe and environmentally friendly, has good social and economic benefit, and has high popularization value.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the leaves processing system.    Crushing device (1)    Sieving device (2)    Collecting pool (3)    Cleaning pool (4)    Fermenting pool (5)
NOVELTY - A nitrogen reforming catalyst comprises a nitrogen-modified activated carbon as catalyst carrier, 0.01-10 mass% metal salt compound, and 0.01-10 mass% nitrogen-containing compound.    USE - A nitrogen reforming catalyst used in catalytic pyrolysis of 1,2-dichloroethane in preparing vinyl chloride (claimed).    ADVANTAGE - The catalyst reduces pyrolysis temperature, maintains high conversion rate and selectivity of vinyl chloride, and is energy-saving and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the nitrogen reforming catalyst, comprising:    (A) washing activated carbon using 0.1-5 mol/L acid solution for 5-10 hours, and drying at 60-120 degrees C for 6-24 hours;    (B) dissolving 0.01-20 mass% metal salt compound and 0.01-20 mass% nitrogen-containing compound in deionized water to obtain a dipping liquid; and    (C) impregnating the dipping liquid for 0.1-24 hours, and activating at 200-800 degrees C for 3-12 hours under nitrogen protection.
NOVELTY - A household garbage fermentation device comprises a seepage pit, a breathable filler layer, and a ventilating fermenter (7). The bottom of the seepage pit comprises a compacted clay layer (1) having a waterproof layer (2). The pit is lined with the permeable filler layer set with drainage duct (4). The filler layer comprises a gravel layer (3), and an upper part sand layer (6). The waterproof layer is a high density polyethylene film having a geotextile upper part (5).    USE - A household garbage fermentation device.    ADVANTAGE - The device requires simple operation, has improved ventilation, and is inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the household garbage fermentation device.    Compacted clay layer (1)    Waterproof layer (2)    Gravel layer (3)    Drainage duct (4)    Geotextile upper part (5)    Upper part sand layer (6)    Ventilating fermenter (7)
NOVELTY - Composition comprises 1 pts. wt. composite Pseudomonas microorganism organic fertilizer, 1-2 pts. wt. straw particles and 1-2 pts. wt. soil particles.    USE - The composition is useful for preventing and treating black shank disease in tobacco plant caused by fungus (claimed) and preventing bacterial infection.    ADVANTAGE - The composition improves the root soil structure of tobacco plant and effectively promotes the growth of tobacco plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the composition, comprising uniformly mixing composite Pseudomonas microorganism organic fertilizer, straw granules and soil particles at room temperature for 5-7 days, stacking at temperature of 40 degrees C and drying at temperature of 40 degrees C until water content is less than 15%.
NOVELTY - Fertilizer comprises 1-3 pts. wt. zinc sulfate, 20-35 pts. wt. urea, 40-50 pts. wt. superphosphate, 6-8 pts. wt. calcium chloride, 2-8 pts. wt. potassium chloride, 5-9 pts. wt. potassium sulfate and 60-80 pts. wt. poultry manure.    USE - The fertilizer is useful for cultivating Houttuynia cordata (claimed).    ADVANTAGE - The fertilizer has high nutrition content, increases soil fertility, and can be prepared in an eco-friendly manner.    DETAILED DESCRIPTION - AN INDEPENDENT CLAIM is included for preparing the fertilizer comprising fermenting poultry manure for 3-6 days, adding zinc sulfate, urea, superphosphate, calcium chloride, potassium chloride, and potassium sulfate to the fermented product and then mixing, and extruding the mixture and then granulating.
NOVELTY - Lettuce fertilizer comprises 100-120 pts. chicken manure, 70-90 pts. peat, 30-50 pts. Houttuynia cordata, 20-30 pts. rice husk powder, 8-10 pts. strain powder, 30-40 pts. peat soil, 20-30 pts. rock phosphate, 10-20 pts. potassium mineral powder, 8-10 pts. nitrogen fertilizer, 3-5 pts. phosphate fertilizer, 7-9 pts. potash fertilizer, and 80-100 pts. water.    USE - Used as a lettuce fertilizer.    ADVANTAGE - The fertilizer satisfies the nutrient requirement of lettuce, creates a good environment for the growth of crops, improves soil properties and produces green organic agricultural products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the lettuce fertilizer, comprising (i) crushing the mentioned components into powder in a crusher, and fermenting in a closed tank; and (ii) preheating the screw mixer to 75 degrees C, maintaining constant temperature, adding the raw material into single screw kneader, turning, maintaining pressure of the die to 1.3-1.5 MPa, and forming into fertilizer granules via screw die jet.
NOVELTY - Sustained-release fertilizer comprises 3-8 pts. wt. monoammonium phosphate, 6-10 pts. wt. ferrous sulfate, 9-15 pts. wt. organic fertilizer, 2-8 pts. wt. calcium superphosphate, 3-9 pts. wt. zeolite, 8-14 pts. wt. peat, 4-6 pts. wt. ammonium molybdate, 3-5 pts. wt. calcium nitrate, 3-6 pts. wt. clay, 5-10 pts. wt. alfalfa, 5-8 pts. wt. Lactobacillus, 2-5 pts. wt. EDTA-chelated zinc and 2-8 pts. wt. sodium selenite.    USE - Used as sustained-release fertilizer.    ADVANTAGE - The fertilizer provides long-term nutritional substance required by crops.
NOVELTY - An n-butane isomerization is performed by loading platinum or palladium catalyst in n-butane at 80-120 degrees C.    USE - Method for n-butane isomerization for producing isobutane (claimed).    ADVANTAGE - The method has high conversion rate.    DETAILED DESCRIPTION - n-Butane isomerization comprises loading H3PW12O40, Cs2.5H0.5PW12O40, or platinum or palladium catalyst in n-butane at 80-120 degrees C.
NOVELTY - Fingolimod hydrochloride is performed by reducing 3-nitro-1-(4-octylphenyl)propan-1-one, performing aldol condensation reaction with formaldehyde, reducing, and performing salt-forming reaction with hydrochloric acid.    USE - Synthesis of fingolimod hydrochloride (claimed).    ADVANTAGE - Synthesis of fingolimod hydrochloride is short, simple, and environment-friendly.    DETAILED DESCRIPTION - Fingolimod hydrochloride of formula (1) is synthesized by reducing 3-nitro-1-(4-octylphenyl)propan-1-one compound of formula (2) to obtain compound of formula (3), performing aldol condensation reaction with formaldehyde to form compound of formula (4), reducing, and performing salt-forming reaction with hydrochloric acid.
NOVELTY - Norfloxacin is prepared by substitution-reacting 1-ethyl-6-fluoro-7-chloro-4-oxo-1,4-dihydro-quinoline-3-carboxylic acid and piperazine in solvent and post-treating.    USE - Preparation of norfloxacin (claimed).    ADVANTAGE - The preparation has high yield, low by-product, short and convenient operation, and low cost, avoids producing ammonia-nitrogen wastewater, and reduces pollution and inorganic salt formation.    DETAILED DESCRIPTION - Norfloxacin is prepared by substitution-reacting 1-ethyl-6-fluoro-7-chloro-4-oxo-1,4-dihydro-quinoline-3-carboxylic acid of formula (I) and piperazine in solvent and post-treating.    M+=Na, K, Li, Rb, or Cs.    INDEPENDENT CLAIMS are included for:    (1) preparation of ciprofloxacin which involves substitution-reacting 1-cyclopropyl-6-fluoro-7-chloro-4-oxo-1,4-dihydro-quinoline-3-carboxylic acid of formula (II) and piperazine in solvent and post-treating; and    (2) preparation of enrofloxacin which involves substitution-reacting 1-cyclopropyl-6-fluoro-7-chloro-4-oxo-1,4-dihydro-quinoline-3-carboxylic acid and N-ethyl piperazine and post-treating in which reaction is represented in formula (III).    .
NOVELTY - This new utility model provide a kind of urban solid waste and located one recycling and using system, comprising kitchen agriculture and forestry waste yard, yard municipal sludge and household garbage storage yard, building garbage storage yard, and separation prevention device, active made fertile device, Anaerobic fermentation device, gasification device, domestic garbage sorting device, clean plastic granulating device, sintering building material device, pressing material device, building garbage crushing device and sieving dust removing and odour removing device. Using " active preparing fertile, Anaerobic fermentation, pyrolysis gasification, plastic granulating, sintering building material, building material and crushing and sieving the each combination of comprehensive treatment method, using each individual component of urban and rural garbage and to have things and basic realize " zero filling, ensuring waste harmlessness, reduction and recycling process, reducing active second time pollute, relieving the environment pollute city caused by the garbage.
NOVELTY - This utility new type belongs to the biological technology and a technology field, relates to using a microorganism conversion method of a compost seepage filtered liquid a functional conversion system. This utility new type by regulating pool, first-stage fermentation pool, microorganism culture device, a microorganism, nutrition liquid supplied to jar, a level fermentation pool, deposition pool, fermentation liquid storage jar, fermentation liquid spray deodorizing device, stirrer, oxygen device, mineral filler and so on compose. This utility new type garbage percolate is effectively reduce actual produce, reduce percolate processing load reduces the energy consumption, and it can effective restrain and eliminate the garbage treatment process in the produce of malodorous gas, a municipal of the compost field provide one set low cost, high efficiency, the garbage leachate recycling circulation using a benzotriazole leachate and solves the problem of malodour.
NOVELTY - This utility new type belongs to a microorganism technology and organic waste pneuma and organic waste water recycling field, relates to a one to a rotten plant by using a microorganism organic waste compost is a liquid. Mineral layer fill a microorganism in a corrosion plant for microorganism culture device, inner cylinder in fill corrosion by plant microorganism source, mineral filler inner set with a first-stage fermentation pool and a fermentation pool level. Microorganism culture device through enriched culture corrosion plant for microorganism, a fermentation pool a rotten plant nutrient solution is rich in microorganism, capable of promoting organic sewage liquid compost smoothly carry out a microorganism community structure in inner fermentation pool. This utility new type is drain enterprise provide the one low cost, a sewage recycling device of high added value, it can realize to organic resourceful and recycling product application is core of ecological cycle a structure.
NOVELTY - This new utility model relates to one of multi-turn fermentation cabin, comprising barrel, one end of tube as feedstock end, the other end is a discharging end, the tube is closed cylindrical tube installed on bracket of barrel, barrel when install feedstock high end, a discharge end low, when installed along tube axis inclination angle is 1 to 10 degrees, and the outside is set with tube with tube rotation using the drive device, internal tube are mounted with disturbance action of baffle plate, inner tube installed with gas distribution device. This new utility model structure is simple, with fermentation period short, full complete fermentation, not producing odour, small floor area small, suitable operation, maintenance operation is simple, fermentation cabin is closed system, operating environment condition is good, and the traditional ferment compost method, gets rid of floor area large, fermentation period long, incomplete fermentation, bad environment equal defect.
NOVELTY - A polylactic acid-type resin has weight average molecular weight of 5400-232000.    USE - Polylactic acid-type resin is used as raw material for anaerobic digestion process for generating biogas. Can also be used as labeling and packaging material and agricultural material.    ADVANTAGE - The polylactic acid-type resin has excellent biodegradability, and enables efficient production of biogas with excellent energy recovery, and maintains the hydrolysis rate during production of biogas. The production of biogas is controlled by controlling crystallinity degree and weight average molecular weight of the polylactic acid-type resin.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of polylactic acid-type resin, which involves reducing molecular weight of the polylactic acid-type resin of raw material, dissolving obtained polylactic acid-type resin at temperature beyond the melting point, annealing dissolved polylactic acid-type resin at temperature less than melting point, and adjusting the obtained product to specific crystallinity degree.
NOVELTY - Performing small scale pyrolysis in a distributed way and creating value through at least one pyrolysis by-product produced from it, comprises: (a) producing at least one pyrolysis by-product by small scale pyrolysis of at least one waste at a production site to be used by at least one by-product processor.    USE - The method is useful for performing small scale pyrolysis in a distributed way and creating value through at least one pyrolysis by-product produced from it (claimed), where the by-product is a liquid, gas or solid and is used to produce renewable fuels.    ADVANTAGE - The method: reduces the cost of waste management, pollution due to transportation and risks associated with the scale-up of conventional technologies; produces energetic by-products that may be sold and used or even reused on site; efficiently transforms biomass and waste into pyrolytic oils (bio-oils), gas (bio-gas) and carbon black; reduces the time required to heat the biomass; exhibits improved control of reaction time, thus maximizing the production of oils over gases and allowing for improved control of oil composition; and avoids the need for a complex drying system and further improves the quality of the bio-oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for performing small scale pyrolysis in a distributed way and creating value through at least one pyrolysis by-product produced from it, comprising: a pyrolysis apparatus for small scale pyrolysis of at least one waste at a production site; and a transport apparatus for transportation of the pyrolysis by-product to at least one by-product processor.
NOVELTY - The method involves feeding the hydride e.g. sodium borohydride and the accelerator e.g. malic acid each being a component in a liquid mixture (4,5)to a reaction site (11-13) and commingled to start and carry on the reaction. The hydride and the accelerator in the respective liquid mixtures to be commingled are fed, through the whole duration of the reaction, under a constant mutual ratio. The hydride and the accelerator in the respective liquid mixtures are maintained with a constant concentration and are varied direct proportional to each other.    USE - Method for generating hydrogen by reacting chemical hydride in presence of accelerator in hydrogen generator apparatus (claimed).    ADVANTAGE - The hydride and the accelerator in the respective liquid mixtures to be commingled are fed, through the whole duration of the reaction, under a constant mutual ratio. Thus, the solid chemical hydride is mixed with water on demand in order to reach a high nominal concentration for minimizing the self-decomposition of the chemical hydride. Hence, the intensity of the commingling process is enhanced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for generating hydrogen by reacting chemical hydride in presence of accelerator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generator apparatus.    Hydrogen generator apparatus (1)    Fuel tank (2)    Accelerator tank (3)    Liquid mixture (4,5)    Reaction site (11-13)
NOVELTY - This utility new type claims a one micro-polluted water removing nitrogen and phosphorus removal of a device, comprising: a reactor (1), machinery lifting device (2), a water inlet pipe (3), discharging hopper (5), methanol channel (6), a sludge valve (7), a back washing flow channel (8), a back washing flow channel control valve (9), a lifting area (10), reaction area layer (11), mixing area (12), a water outlet (14), a sleeve (16) and electrical machine (17), a reactor (1), the upper part is cylinder shape, the bottom is funnel-shaped, mud discharge bucket (5) set in reactor (1) is most bottom of reactor (1) in reactor (1) centre axis a. there is machinery lifting device (2). The utility model effective solves the problem that the micro-polluted water of nitrogen phosphorus standard, for removing a nitrogen phosphorus through prevention by a nitrogen phosphorus caused by overproof of water body eutrophication fit depth of river, lake and landscape water removing nitrogen and phosphorus removal process.
NOVELTY - This utility new type claims a livestock manure continuous producing one solid fertilizer and liquid fertilizer of device, set with a livestock and poultry excrement solid-liquid separating unit, solid fermentation and drying unit and liquid fermentation unit, solid-liquid separating unit connecting a solid fermentation and drying unit and unit liquid fermentation, liquid fermentation unit b. solid-liquid separating unit, solid fermentation and lower part of drying unit or are staggered set, the whole device structure is reasonable, into automatic degree high, a short period, saves resource, a low cost, stable property, simple operation, little investment, without second pollution, can the solid and liquid manure is separate, and at the same time a production organic solid fertilizer and liquid fertilizer, solves the problem that the large-scale cultivation and produce a livestock and poultry excrement pollution problem and is for a crop for organic fertilizer requirement, a recycling process, promoting circulation economic development of livestock and poultry industry and agriculture and forestry, it has a good economic benefit, social benefit and ecological benefit.
NOVELTY - Non-naturally occurring microorganism that is capable of growing on a gaseous substrate as a carbon and/or energy source, is new, where the microorganism comprises at least one exogenous nucleic acid encoding a limonene synthase enzyme, and the microorganism biosynthesizes squalene.    USE - The microorganism is useful for producing limonene and squalene, where limonene is useful e.g. in a jet fuel, for producing terephthalic acid (all claimed), as a solvent replacement, as a release agent for asphalt, as a circuit board cleaner, as a grease trap maintainer, as a spot and stain remover, as a hand cleaner, as a cleaner for printing inks, as an aerosol ingredient, as a penetrating oil, as an adhesive removal, as a marine vessel cleaning product, as a solvent carrier, in asphalt grading, as a pesticide, as an odorant, in Flavor and fragrance industry, in food manufacturing for flavoring, in beauty products as a scent in perfume and lotions, as an antioxidant, as a disinfector, as a biofuel, and as a laundry additive.    ADVANTAGE - The microorganism provides low cost limonene products.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) producing limonene, comprising culturing the non-naturally occurring microorganism in a bioreactor that comprises the gaseous substrate and a culture medium that comprises other nutrients for growth and bioproduct production, under conditions that are suitable for growth of the microorganism and production of limonene, where the microorganism produces limonene; and    (2) producing squalene, comprising culturing the non-naturally occurring microorganism in a bioreactor that comprises the gaseous substrate and a culture medium that comprises other nutrients for growth and bioproduct production, under conditions that are suitable for growth of the microorganism and production of squalene, where the microorganism produces squalene.
NOVELTY - This utility new type claims an experiment device for mixing and stirring in gas fermenting process, wherein thea anaerobic fermentation flask of the device is of flat glass wherein three bottle structure; the anaerobic fermentation flask is set up with three of same, two side of bottle wherein different is set with inclined angle, a bottle opening is set with a seal bottle plug, bottle plug set with seal temperature monitor, an air pipe I and machinery stir device activity, activity machinery stir device is a micro electric machine speed reducer fixed at the bottle cover upper seal, and seal bottle plug is connected, the upper speed reducer is a seal cover set with fixed clamp, a speed reducer and a micro motor, stir blade through stir shaft and speed reducer, stir shaft end by a fixing clamp fixing activity. This utility new type is convenient to use activity machinery a stir device for a high concentration fermentation flask material in a different angle, depth of stir monitoring experiment, to search a different machinery stir depth, angle a of the best biogas, a biogas production actual provide technology support.
NOVELTY - This utility new type provide the one constant temperature and a fermenting groove, comprising a plurality of a fermenting groove, in the fermentation groove set with temperature sensor, further comprising an exhaust pipeline, the exhaust pipeline in set with a fan, the air inlet of the exhaust pipeline set with a biological filter bed in the upper part of the fermenting groove, an air outlet of the air draft pipeline, in the biological filter bed is set with biology. This utility new type aiming at a defect in existing technology process improves, it has following advantages: air blower. space, introducing external air amount is a control, and a heat energy after processing for taking a and reduce the energy consumption. Closeness space, negative pressure air conditioner design, reduces the smell, smell by a two channel processing only. The fermenting groove inner operation parameter retrieval monitoring system, recording data, and a air blower wind amount, and a humidifying, establishing best fermentation environment. A according to a monitoring condition control exhaust fan air amount, real time reflect the fermentation condition, and establishing safe working environment.
NOVELTY - This utility model claims a four-level circulation reflux marsh gas pool, comprising gas storage room, a gas room set with an air outlet, the upper end of the gas storage room is a four, four of the gas storage room are set, four of the gas storage room is between the middle are set with connected wherein located on one side of the gas storage room one side is set with a feeding port, b positoin the other side of the gas storage room one side is set with a liquid outlet, the liquid outlet wherein is set with a gas storage room and a reflux pump connect entrance, exit of the reflux pump and set with a feed wherein the gas storage room is connected. And the existing technology, this utility new type four level circulation reflux marsh gas pool, original overturning device for hydraulic biogas pool for carrying out. A continuous feeding, solid-liquid separating, stable, anti-explosion, after cleaning does not need one time feeding such as a complete, especially suitable for b of pig farm excrement removing.
NOVELTY - Preparation of solid base catalyst involves mixing zinc oxide, calcium hydroxide and potassium fluoride dihydrate in a molar ratio of 2:1:(1-1.5), obtaining mixture, adding deionized water, drying at 70-90 degrees C for 5-7 hours, and calcining at 250-500 degrees C for 5-7 hours. The molar ratio of mixture and deionized water is (2.5-3.5):16.    USE - Preparation of solid base catalyst used for preparing biodiesel.    ADVANTAGE - The method enables simple preparation of solid base catalyst having excellent activity.
NOVELTY - Preparation of solid base catalyst involves obtaining a mixture by mixing zinc oxide, calcium hydroxide and potassium fluoride dihydrate in molar ratio of 2:1:0.5-2, adding deionized water, grinding the resultant product, drying at 70-90 degrees C for 5-7 hours, and baking at 350-450 degrees C for 5-7 hours. The molar ratio of deionized water and mixture is 2.5-3.5:16.    USE - Preparation of solid base catalyst used for preparing biodiesel.    ADVANTAGE - The method enables simple preparation of solid base catalyst having excellent activity.
NOVELTY - Preparing bio-organic fertilizer comprises: (a) preparing raw materials comprising 23 wt.% of nitrate mud, 22 wt.% of animal manure, 20 wt.% of clay, 15 wt.% of rapeseed cake, 10 wt.% of phosphorus powder, 10 wt.% of ash, and liquid methane; (b) drying nitrate mud, clay, phosphorus powder, rapeseed cake, ash and animal manure to a moisture content of less than 12%, crushing the materials, mixing the other ingredients, stirring the mixture, adjusting the water content of the mixture to 55-65%; (c) fermenting the mixture; (d) drying; and (e) packaging the organic fertilizer.    USE - The method is useful for preparing bio-organic fertilizer (claimed).    ADVANTAGE - The method is capable of economically preparing the fertilizer, which improves soil structure, promotes soil microorganism activity, enhances fertilizer-keeping property, increases crop yield, and increases product quality.    DETAILED DESCRIPTION - Preparing bio-organic fertilizer comprises: (a) preparing raw materials comprising 23 wt.% of nitrate mud, 22 wt.% of animal manure, 20 wt.% of clay, 15 wt.% of rapeseed cake, 10 wt.% of phosphorus powder, 10 wt.% of ash, and liquid methane; (b) drying nitrate mud, clay, phosphorus powder, rapeseed cake, ash and animal manure to a moisture content of less than 12%, crushing the materials, mixing the other ingredients, stirring the mixture, adjusting the water content of the mixture to 55-65%; (c) carrying out anaerobic fermentation for the mixture for 6-8 days, carrying out heap fermentation when the internal temperature of the mixture reaches 60 degrees C, covering the mixture with a plastic sheeting, again fermenting the mixture for 6-8 days until the mixture turns to brown or dark brown color; (d) drying the fermented mixture at 70 degrees C to a moisture content of less than 8-12%, and (e) packaging the organic fertilizer.
NOVELTY - The system has a filter screen connected with a polygonal frame. A sludge mixture paving horizontal porous plate is arranged on the frame. An oxygen supply system is provided with an oxygen storage tank (7) which is connected with an oxygen supply pipeline (8). A composting chamber (4) is mounted at the oxygen storage tank. An electromagnetic control valve is arranged at the oxygen supply pipeline. The oxygen is passed into the composting chamber through the oxygen supply pipeline. The exhaust gas produced in the composting chamber is discharged through a waste gas discharging outlet (6).    USE - Multi-layer digestion sludge aerobic composting bed system.    ADVANTAGE - The manufacturing cost and operating cost of the multi-layer digestion sludge aerobic composting bed system are reduced. The aerobic composting time is reduced. The sludge stabilization rate of the aerobic composting bed system is improved. The sludge aerobic composting efficiency is increased. The energy loss during the sludge composting process is reduced. The occurrence of environmental pollution by the sludge aerobic composting bed system is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multi-layer digestion sludge aerobic composting bed system.    Composting chamber (4)    Waste gas discharging outlet (6)    Oxygen storage tank (7)    Oxygen supply pipeline (8)    Oxygen content sensor (14)
NOVELTY - Multi-effect fertilizer is prepared using 200-250 pts. wt. rapeseed cake, 30-40 pts. wt. pig manure, 30-40 pts. wt. chicken manure, 30-40 pts. wt. corn straw, 30-40 pts. wt. rice straw, 10-20 pts. wt. calcium superphosphate, 10-20 pts. wt. urea, 10-15 pts. wt. monopotassium phosphate, 8-10 pts. wt. diammonium phosphate, 8-10 pts. wt. ferrous sulfate, 3-5 pts. wt. zinc sulfate, 3-5 pts. wt. boric acid, 10-20 pts. wt. rhizobia powder, 8-15 pts. wt. effective microorganism (EM) agent, 3-4 pts. wt. sugar, and suitable amount of water.    USE - As multi-effect fertilizer.    ADVANTAGE - The multi-effect fertilizer is nontoxic, and ensures to increase crop yield, prevent crop disease and improve soil fertility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the multi-effect fertilizer, which involves (a) soaking corn straw, and rice straw in water for 24-48 hours, mixing the soaked mixture with rapeseed cake, crushing the resulting mixture, and adding chicken manure to the crushed mixture, (b) mixing EM agent with sugar and culturing the resulting mixture for 24 hours to obtain bacterial liquid, (c) mixing the bacterial liquid with mixture obtained in the step (a) and remaining raw materials except rhizobia powder and fermenting the resulting mixture for 20-25 days at 55 degrees C or more by turning the fermentation mixture once after every 3-5 days, where the fermentation mixture has moisture content of 60%, (d) drying the fermentation product at 150 degrees C or more for 2-4 hours, and (e) adding rhizobia powder to the dried fermentation product and granulating the resulting mixture to obtain product.
NOVELTY - Fertilizer comprises mixed organic fertilizer, mixed inorganic fertilizer and effective microorganism active nutrient solution. Mixed organic fertilizer is prepared by mixing chicken manure, cow dung and rice straw with water and then carrying out fermentation. Mixed inorganic fertilizer comprises nitrogen fertilizer, phosphorus fertilizer, potassium fertilizer and calcium.    USE - Fertilizer used for flue-cured tobacco (claimed).    ADVANTAGE - The fertilizer improves quality, height and stem diameter of tobacco, increases yield of tobacco, promotes plant growth and development, and has balanced nutrition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) mixing chicken manure, cow dung and rice straw with water, and adding rice straw in a fermenting container to carry out fermentation at 65-68 degrees C for 7-8 days and then at 50-53 degrees C for 15-16 days to obtain a fermented product;    (B) stacking the fermented product at normal temperature for 18-20 days, sterilizing it to obtain mixed organic fertilizer;    (C) mixing nitrogen fertilizer, phosphorus fertilizer, potassium fertilizer and calcium to obtain mixed inorganic fertilizer; and    (D) mixing mixed organic fertilizer and mixed inorganic fertilizer to obtain a mixture, and then spraying effective microorganism active nutrient solution on the mixture by using a machine to obtain final product.
NOVELTY - 2-Amino-5-phenyl-1,3,4-oxadiazole-based compound (I), is new.    USE - 2-Amino-5-phenyl-1,3,4-oxadiazole-based compound (I) used for preparing medicine for reducing blood pressure.    ADVANTAGE - The compound is prepared using readily available raw materials. The method is simple, has moderate conditions, is environment-friendly, and has a yield of 94%.    DETAILED DESCRIPTION - 2-Amino-5-phenyl-1,3,4-oxadiazole-based compound of formula (I), is new.    R=methyl, phenyl, vinyl, naphthyl, fluorophenyl, methoxyphenyl, thienyl, or dimethylaminophenyl.    An INDEPENDENT CLAIM is included for preparing (I).
NOVELTY - Synthesis of apixaban (I) comprises hydrolysis reacting 1-(4-methoxyphenyl)-7-oxo-6-(4-(2-oxo-1-piperidinyl)phenyl)-4,5,6,7-tetrahydro-1H-pyrazolo(3,4-c)pyridine-3-carbonitrile (II) and hydrogen peroxide under alkaline condition.    USE - Synthesis of apixaban (I) (claimed).    ADVANTAGE - The method controls product quality by avoiding side reactions, has mild reaction condition, low equipment demand, low auxiliary agent dosage, low total cost, and high yield in each reaction step, is environment-friendly and suitable for industrial production, and avoids the use of ammonia sources.    DETAILED DESCRIPTION - Synthesis of apixaban of formula (I) comprises hydrolysis reacting 1-(4-methoxyphenyl)-7-oxo-6-(4-(2-oxo-1-piperidinyl)phenyl)-4,5,6,7-tetrahydro-1H-pyrazolo(3,4-c)pyridine-3-carbonitrile of formula (II) and hydrogen peroxide under alkaline condition. INDEPENDENT CLAIMS are included for:    (1) preparation of apixaban intermediate i.e. compound (II) comprising subjecting carbonitrile compound of formula (9) and nitrophenyl compound of formula (10) in the presence of acid-binding agent to 1,3-dipolar cycloaddition cyclization to obtain methoxyphenyl compound of formula (11), subjecting compound (11) to reduction reaction to obtain aniline compound of formula (12), subjecting compound (12) and 5-halogenated chloride compound of formula X-CH2-CH2-CH2-CH2-C(=O)-Cl (A) to amidation reaction in the presence of acid-binding agent to prepare piperidinone compound of formula (13), and subjecting compound (13) to ring closing N-alkylation reaction in the presence of acid-binding agent to prepare (II);    (2) apixaban intermediate i.e. compound (11);    (3) apixaban intermediate i.e. compound (12); and    (4) apixaban intermediate i.e. compound (13).    X=Cl, Br, or I.
NOVELTY - A N-phosphonomethyliminodiacetic acid (PMIDA)-prepared glyphosate is produced by oxidizing hydrogen peroxide, air or oxygen-rich gas as oxidizing agent, activated carbon as catalyst, and PMIDA in water, cooling reaction system, adding alkali to obtain glyphosate salt and activated carbon mixture, solid-liquid separating mixture to obtain solid activated carbon and glyphosate salt solution as filtered liquid, feeding glyphosate salt solution in bipolar film electro-dialysis device, treating, controlling pH to 2-3 in salt room to obtain glyphosate solution and alkali solution in alkali chamber.    USE - Production of N-phosphonomethyliminodiacetic acid-prepared glyphosate (claimed).    ADVANTAGE - The production increases glyphosate solubility, avoids formaldehyde by-product in mother liquid and repeated heating and cooling, does not need to add acid to neutralize, eliminates sulfate or hydrochloride coagulant salt by-product, reduces waste pollution and salt-containing wastewater, and has good product quality and high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for PMIDA-prepared glyphosate production device comprising oxidation reaction device, solid-liquid separating device, bipolar film electro-dialysis device, and crystallizing device in which oxidation device material outlet is connected to solid-liquid separating device material inlet, solid-liquid separating device filtered liquid outlet is connected to bipolar film electro-dialysis device salt room, solid-liquid separating device solid outlet is connected oxidation reaction device, bipolar film electro-dialysis device alkali room is connected to oxidation reaction device, and bipolar film electro-dialysis device salt room is connected to crystallizing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of PMIDA-prepared glyphosate production and device. (Drawing includes non-English language text).
NOVELTY - 3-substituted-6-metallocene-methyl-1,2,4-triazolo(3.4-b)-1,3,4-thiadiazole is new.    USE - 3-substituted-6-metallocene-methyl-1,2,4-triazolo(3.4-b)-1,3,4-thiadiazole for pesticide, anti-microbial filed, pharmaceutical field, and insecticide.    ADVANTAGE - The compound has good biological activity, short synthesis time, safe reaction, and high yield, is environment-friendly and economical.    DETAILED DESCRIPTION - 3-substituted-6-metallocene-methyl-1,2,4-triazolo(3.4-b)-1,3,4-thiadiazole of formula (I) is new.    X=formula (i); and    R=H, aryl, or 1-10C alkyl.    An INDEPENDENT CLAIM is included for preparation of 3-substituted-6-metallocene-methyl-1,2,4-triazolo(3.4-b)-1,3,4-thiadiazole.
NOVELTY - 4-(3,4-dihydroxybenzoyloxymethyl)phenyl-O- beta -D-glucopyranoside is synthesized by reacting 2,3,4,6-tetra-O-acetyl- alpha -D-glucopyranosyl bromide and p-hydroxybenzyl alcohol in anhydrous dipolar aprotic solvent, catalyzing using anhydrous potassium carbonate and cesium chloride accelerator to obtain 4-(hydroxymethyl)phenyl-2,3,4,6-tetra-O-acetyl- beta -D-glucopyranoside, and reacting with 3,4-diacetoxy-benzoyl chloride in anhydrous chlorinated hydrocarbon organic solvent and acid-binding agent to obtain 4-(3,4-diacetoxybenzoyloxymethyl)-phenyl-2,3,4,6-tetra-O-acetyl beta -D-glucopyranoside.    USE - Synthesis of 4-(3,4-dihydroxybenzoyloxymethyl)phenyl-O-beta-D-glucopyranoside (claimed).    ADVANTAGE - Process is low cost, convenient, short, and environment-friendly, and does not require use of column chromatography.
NOVELTY - Polyhydroxy sterol monomer compounds, which are dendronesterol A and (20S,22E,24R)-ergosta-7,22-dien-3 beta ,5 alpha ,6 beta -triol, are prepared by homogenizing fresh sea squirt using tissue triturator, ultrasonically extracting 4 times using 95% ethanol for 30 minutes each, combining extracts, vacuum-concentrating using rotary evaporator at 35 degrees C, measuring relative density which is 1.1-1.4 to obtain extract, dispersing extract and water in which mass ratio of extract and water is 1:1, vacuum-concentrating using ethyl acetate at 35 degrees C, and measuring relative density which is 1.1-1.4.    USE - Preparation of polyhydroxy sterol monomer compound for anti-Artemia medicine (claimed).    ADVANTAGE - Process is simple, low cost, and environment-friendly, has high efficiency, and produces product with increased insecticidal rate.    DETAILED DESCRIPTION - Polyhydroxy sterol monomer compounds, which are dendronesterol A of formula (1) and (20S,22E,24R)-ergosta-7,22-dien-3 beta ,5 alpha ,6 beta -triol of formula (2), are prepared by homogenizing fresh sea squirt using tissue triturator, ultrasonically extracting 4 times using 95% ethanol for 30 minutes each, combining extracts, vacuum-concentrating using rotary evaporator at 35 degrees C, measuring relative density which is 1.1-1.4 to obtain extract, dispersing extract and water in which mass ratio of extract and water is 1:1, vacuum-concentrating using ethyl acetate at 35 degrees C, measuring relative density which is 1.1-1.4 to obtain ethyl acetate phase extract, dissolving in methanol, performing Sephadax LH-20 gel column chromatography and RP-18 reverse phase silica gel column chromatography, carrying out gradient elution using methanol/water with concentration of 30%, 40%, 50%, 60%, 70%, 80%, 90%, and 100%, performing highly efficient liquid phase chromatography, and eluting with 80% aqueous methanol.
NOVELTY - A biomass energy conversion method is performed by selecting agricultural source, poultry excrement, organic wastewater and organic solid waste in which agricultural source is soybean, rapeseed, sesame, peanut, sunflower, cottonseed, and hemp, and organic wastewater comprises sugar wastewater, animal lipid, and catering waste oil, crushing raw materials to obtain not greater than 2 mm granules, heating to vaporize, condensing, collecting condensate, adding alcohol and catalyst i.e. basic catalyst, acidic catalyst, and enzyme catalyst, uniformly mixing, transesterifying, and filtering to obtain diesel oil.    USE - A biomass energy conversion method (claimed).    ADVANTAGE - The method can be performed using wide range of raw materials, is environment-friendly, safe, reduces cost of energy consumption, and has high stability.    DETAILED DESCRIPTION - A biomass energy conversion method is performed by selecting agricultural source, poultry excrement, organic wastewater and organic solid waste in which agricultural source is soybean, rapeseed, sesame, peanut, sunflower, cottonseed, hemp, Linum usitatissimum, castor oil, Semen perillae acutae, pistachio, and palm oil, and organic wastewater comprises sugar wastewater, animal lipid, and catering waste oil, crushing raw materials to obtain not greater than 2 mm granules, heating to vaporize, condensing, collecting condensate, adding alcohol and catalyst i.e. basic catalyst, acidic catalyst, and enzyme catalyst, uniformly mixing, transesterifying, and filtering to obtain biomass diesel oil.
NOVELTY - The method involves detecting carbon dioxide and methane contents in greenhouse gas sample at preset working conditions by flame ionization detector and electron capture detector at operating temperature of 250 degrees C. The nitrous oxide is detected in nitrogen carrier gas detector at operating temperature of 300 degrees C. The ruminant greenhouse gas emissions rate is calculated based on rate of change of concentration of greenhouse gases in respiratory metabolism tank for calculating (105) ruminant test rate and total daily emissions of greenhouse gas emission.    USE - Method for measuring greenhouse gas emission from ruminant livestock.    ADVANTAGE - The ruminant greenhouse gas emissions rate is calculated for calculating ruminant test rate and total daily emissions of greenhouse gas emission, such that the economic and environment-friendly greenhouse gas emission measurement is realized. The simple and easy operations are realized. The accurate measure of ruminant livestock greenhouse gas discharge rate is attained.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the greenhouse gas emission measuring process. (Drawing includes non-English language text)    Step for manufacturing sealed respiratory metabolism tank (101)    Step for selecting ruminant livestock (102)    Step for collecting greenhouse gas sample (103)    Step for detecting carbon dioxide and methane contents (104)    Step for calculating ruminant test rate and total daily emissions of greenhouse gas emission (105)
NOVELTY - This utility new type claims a piggery one excrement cleaning mechanism, comprising bottom plate and by composed of pigsty, the ring is inclined set with excrement with a guide groove, the guide groove is manure outlet end mounting a solid-liquid separating machine, solid-liquid separating machine is liquid outlet end connecting with a sewage treatment pool, outlet end of solid solid-liquid separating machine connecting with a marsh gas fermentation pool, a bottom plate by a multi-rotating a compose a activity plate is mounted bottom, the and the excrement groove separating, one end each plate of activity are connecting with driving the rotation of motor, and set with a water source is a water spraying pipe in each side wall of the excrement groove, a water spraying pipe with a further set with multi-jet device with a high pressure spray head of electromagnetic valve, ring of rear front side wall, a solid-liquid separating machine and a multi-motor, high pressure nozzle and jet device at the same time electrically connect with one controller, the operation is convenient, energy-saving and environment-friendly, has a flushing time would not the pig is sprayed water, and a long-term holding piggery inner environment of drying and so on.
NOVELTY - This utility new type relates to a biological diesel oil one rectifying device, belonging to rectifying device technology field. This utility new type including the outlet I of gas mix pipe, distillation column I, a distillation column II, column III, column IV and pressure distillation column, gas mixed pipe a snake-shaped tube I, outlet II a snake-shaped pipe III, III outlet connecting pipe I and pipe II connection pipe III, IV connecting pipe , IV connecting pipe , upper outlet of separator I a snake-shaped pipe II, below a liquid outlet pipe I and separator II under a liquid outlet pipe II, III a separator exit a snake-shaped pipe IV, below lower outlet connecting pipe I, a separator liquid outlet IV a liquid outlet pipe II, an air outlet pipe and pipe IX up the top part of air outlet pipe and pressure distillation of distillation column 4 is a distillation column and connected to the pipe VII, a separator V outlet connecting inlet I, below a liquid outlet pipe III. This utility new type operation is convenient, the energy consumption is low, product quality is stable.
NOVELTY - The utility model relates to a a rear leg special-shaped cushion pillow , comprising cushion body positive sidee and pad body, the anode side gasket body shape and size mat body is same, a trapezoid block, the top part is arc-shaped saddle, the anode side gasket body is one wherein a vertical side wall and a pad body is one wherein a vertical side wall activity connection, in the top wall part of the anode side of pad body is fixed and set with a bi-directional supplement positive modulating material, the pad body of the top wall is in part embedded and fixed set with bi-directional supplement and regulate and control, in the anode side gasket body pad body and one side of the inclined side wall is in a part embedded and fixed set with a positive side magnetic piece and cathode side magnetic piece, the N pole direction of said anode side magnetic piece towards the outside of the anode side gasket body, the magnetic piece is S pole direction towards the outside of the pad body. The beneficial effect is simple structure, a low cost, without energy consumption, it can effective relieve the waist and leg pain caused by the imbalance is.
NOVELTY - This new utility model relates to a kind of biological diesel oil refining device one, category biological energy technology area. This new utility model comprises rough biological diesel oil storage tank, a distillation kettle, gas circulation pump and heat exchanger, import and exit and distillation kettle bottom upper part of the rough biological diesel oil storage tank connected with the import left side outlet and the heat exchanger and distillation kettle top part connected with the middle part of distillation kettle set with the import of inert gas, exit of import and gas circulation pump and inert gas connection, top right side exit and import and the gas circulation pump connected with heat exchanger, the heat exchanger bottom right side provided with refined product outlet. This utility model with new inert gas distillation refining biological diesel oil, the biologic diesel oil with high purity, realize low temperature refining biological diesel oil, utilization rate increase device, reduce the energy consumption, at the same time prevent the distillation process of generating oxidation products.
NOVELTY - One a municipal domestic sewage harmless processing device, referring to a domestic sewage processing device one, a plurality a defecation device through feces. pipeline (3) a septic tank, the septic tank upper part set with taking excrement pump, septic tank the lower part through liquid pipeline (13) connecting liquid dehydration device (6), liquid dehydration device upper part set with material wherein (15), dehydration device through liquid pipeline (10) in connection or municipal and pipeline (12), liquid dehydration device through pipeline or a municipal drainage main pipeline (11), the utility model is new type use waste pipeline. the dejecta of squatting pan, pedestal pan collecting to septic tank, a feces organic fertilizer is a b agricultural production, which effectively reduces the waste pollution for a channel.
NOVELTY - A chicken feed additive contains Macleaya cordata extract, phytase, probiotics, composite trace element, and multivitamin.    USE - A chicken feed additive for chicken feed (claimed).    ADVANTAGE - Process is environment-friendly and increases egg production rate, and product is healthy, satisfies nutritional need, protects intestinal tract, improves liver function, immunity, and digestibility, maintains stability, reduces ammonia concentration, and has natural antibacterial effect and anti-inflammatory effect, high quality, and less toxic and side effect.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) preparation of chicken feed additive which involves performing 1st-stage pre-mixing in composite trace element and multivitamin using mixer, performing 2nd-stage pre-mixing in multivitamin, methionine, lysine, sodium bicarbonate, and zeolite powder using mixer, performing 3rd-stage pre-mixing in 2nd-stage pre-mixed semi-finished product, medical stone, composite trace element, stone powder, calcium hydrophosphate, and sodium chloride, performing greater than or equal to 3 stages pre-mixing in probiotics, phytase, M. cordata extract, and zeolite powder, and distributing; (2) chicken feed comprising 55-65 pts. wt. corn, 20-28 pts. wt. soybean meal, 0-3 pts. wt. wheat bran, 5-10 pts. wt. stone powder, and 4-6 pts. wt. feed additive; and (3) application of chicken feed which involves feeding chicken feed into 18 weeks old egg-laying hen.
NOVELTY - The device has a coalescent filter (1) that is connected with an outlet pipe at the bottom. The upper portion of filler towers (2,3) is connected to outlet end of plug valves. The entrance end of plug valves is connected with a high pressure gas discharging tube (11). The plug valves are connected to a regeneration gas cooler (4). The middle portion of a regeneration gas heater (5) is connected to steam inlet pipe (9). The outlet end of gas heater is connected to a condensed water pipe (10). A de-film separating outlet pipe (17) is connected to plug valves.    USE - Temperature change absorbing device for protective membrane separation equipment used in methanol synthesis.    ADVANTAGE - The operating efficiency of the protective membrane separation equipment is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for temperature change absorbing method for protective membrane separation equipment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the temperature change absorbing device.    Coalescent filter (1)    Filler towers (2,3)    Regeneration gas cooler (4)    Regeneration gas heater (5)    Steam inlet pipe (9)    Condensed water pipe (10)    High pressure gas discharging tube (11)    Separating outlet pipe (17)
NOVELTY - The super-gravity device has a non-impact flow structure and super-gravity structure. The non-impact flow structure includes sub-feeding pipe, secondary feeding pipe and main feeding tube. The front end of main feeding pipe is set with nozzle. The super-gravity structure includes housing which is set with liquid outlet, a rotor, a motor, filler and a rotating shaft. The edge of rotor is connected with filler. The rotating shaft is connected with motor to drive rotor.    USE - Super-gravity device for continuous production of methanol emulsified diesel oil.    ADVANTAGE - The two phase flow impact effect is increased and the continuous preparation of large flow amount of diesel oil is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the super-gravity device for continuous production of methanol emulsified diesel oil.    Rotary filler bed emulsifying device (1)    Water conveyer pump (2)    Emulsifier (3)    Oil pump (4)    Methyl alcohol storage tank (5)    Product storage tank (6)
NOVELTY - A honeycomb-shaped methanation catalyst comprises carrier, nickel as active component and additive. The carrier is cordierite honeycomb-shaped ceramic-coated alumina film. The additive contains additive (A) and additive (B). The additive (A) contains calcium oxide and/or magnesium oxide. The additive (B) contains lanthanum(III) oxide.    USE - Honeycomb-shaped methanation catalyst (claimed).    ADVANTAGE - The honeycomb-shaped methanation catalyst has excellent dispersibility with respect to nickel oxide particles, carrier surface acidity, catalytic activity and anti-coking property, and is prepared by economical process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of honeycomb-shaped-shaped methanation catalyst, which involves dissolving aluminum nitrate in distilled water, obtaining immersion liquid (A), immersing cordierite honeycomb-shaped ceramic in the resultant solution, drying the resultant material, sintering, obtaining cordierite honeycomb-shaped ceramic-coated alumina film carrier, immersing the obtained carrier in immersion liquid (B) obtained by dissolving nitrate of nickel, calcium or magnesium and lanthanum in distilled water, discharging the resultant material, drying and sintering.
NOVELTY - Preparing fermentable sugar and nano silicon dioxide comprises (i) adding rice hull into 0.05-30 wt.% concentration mixed acid solution and reacting for 30-300 minutes at 50-200 degrees C to obtain residual solid and fermentable sugar crude product solution, (ii) high pressure carbon dioxide separating the fermentable sugar crude product solution to obtain fermentable sugar precipitate, and (iii) burning residual solid in oxygen or air atmosphere at 500-1000 degrees C for 10-360 minutes to obtain nano-silicon dioxide.    USE - The method is useful for preparing fermentable sugar and nano silicon dioxide (claimed).    ADVANTAGE - The method is simple, economical and utilizes raw materials which are widely distributed, is energy saving and environmentally friendly, and realizes controlling of aperture of nano-silicon dioxide. The fermentable sugar is further processed to obtain fuel ethyl alcohol.
NOVELTY - An organic wastewater treatment-methane production microbial electrolytic cell device comprises microbial electrolytic cell shell (1) set with anode electrode (8) and cathode electrode (4), external direct current voltage-stabilized power supply (6), inlet water pipe (9), water distributor (10), sludge discharge pipe (11), valve (12), drain pipe (2), gas collecting pipe (3), inlet water control valve, drain control valve, gas monitoring device, operation panel, and automatic control device e.g. computer or microcontroller.    USE - An organic wastewater treatment-methane production microbial electrolytic cell device (claimed).    ADVANTAGE - Organic wastewater treatment-methane production microbial electrolytic cell device is easy to scale, reduces cost, and has simple structure and low construction cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of organic wastewater treatment-methane production microbial electrolytic cell device. (Drawing includes non-English language text).    Microbial electrolytic cell shell (1)    Drain pipe (2)    Gas collecting pipe (3)    Cathode electrode (4)    Direct current voltage-stabilized power supply (6)    Anode electrode (8)    Inlet water pipe (9)    Water distributor (10)    Sludge discharge pipe (11)    Valve (12)
NOVELTY - Bioorganic fertilizer comprises potato stalk, highland barley straw, broad bean straw, wheat straw, radix sophorae flavescentis, pine needle, radix isatidis, chitin, phosphoric acid, monopotassium phosphate, dipotassium hydrogen phosphate, Verticillium powder, Bacillus thuringiensis powder, Aschersonia powder, caterpillar powder, cortex fraxini, and Stemona japonica.    USE - As bioorganic fertilizer.    ADVANTAGE - The bioorganic fertilizer improves fertility of soil and promotes decomposition of heavy metals in soil.    DETAILED DESCRIPTION - Bioorganic fertilizer comprises 25-35 pts. wt. potato stalk, 25-35 pts. wt. highland barley straw, 25-35 pts. wt. broad bean straw, 25-35 pts. wt. wheat straw, 1-2 pts. wt. radix sophorae flavescentis, 1-2 pts. wt. pine needle, 1-2 pts. wt. radix isatidis, 0.5-1.5 pts. wt. chitin, 1-3 pts. wt. phosphoric acid, 5-9 pts. wt. monopotassium phosphate, 4-7 pts. wt. dipotassium hydrogen phosphate, 8-12 pts. wt. Verticillium powder, 0.1-0.2 pt. wt. Bacillus thuringiensis powder, 0.1-0.2 pt. wt. Aschersonia powder, 0.3-0.5 pt. wt. caterpillar powder, 1-3 pts. wt. cortex fraxini, and 1-2 pts. wt. Stemona japonica.
NOVELTY - A flutriafol intermediate is prepared by coupling benzaldehyde compound and phenylboronic acid compound in solvent with presence of transition metal catalyst under alkaline condition in which solvent is mixed solvent comprising organic solvent and water.    USE - Preparation of flutriafol intermediate (claimed).    ADVANTAGE - The preparation has low cost, less waste, and high yield, and can repeatedly use catalyst.    DETAILED DESCRIPTION - A flutriafol intermediate of formula (C) is prepared by coupling benzaldehyde compound of formula (A) and phenylboronic acid compound of formula (B) in solvent with presence of transition metal catalyst under alkaline condition in which solvent is mixed solvent comprising organic solvent and water.    R1=alkyl, haloalkyl, or halo; and    R2=H, alkyl, or halo.
NOVELTY - One-pot synthesis of ketoconazole drug intermediate cis-bromo ester comprises taking 2,4-di-chloroacetophenone and glycerol as brominating agent in solvent; taking catalyst; brominating methyl ketone carbonyl, carrying out carbonyl group and glycerol ketal reaction; and reacting bromo ketal solution with benzoyl chloride.    USE - Method for one-pot synthesizing ketoconazole drug intermediate cis-bromo ester (claimed).    ADVANTAGE - The method has high yield, simple operation, high safety, low cost and less pollution. It fits industrial production.
NOVELTY - Using alkaline anion exchange resin to reduce acid value of biodiesel involves pre-processing alkaline anion exchange resin, mixing pre-processed alkaline anion exchange resin to biodiesel, and then stirring the mixture at certain temperature for certain time. The mixture is kept for maintaining acid value of biodiesel. The alkaline anion exchange resin is alkaline styrene anion exchange resin 201X2, 201X4, 201X7, 202X7, 201X8, D290, D296, D201, D261, D280, D284, D262, D201GF, D301R, D301G, D371, D392, D380 or D382.    USE - Method for using alkaline anion exchange resin to reduce acid value of biodiesel (claimed).    ADVANTAGE - The method ensures low energy consumption, simple operation, lower cost and environment pollution.    DETAILED DESCRIPTION - Alkaline anion exchange resin is used to reduce acid value of biodiesel involves pre-processing alkaline anion exchange resin, mixing pre-processed alkaline anion exchange resin to biodiesel, and then stirring the mixture at certain temperature for certain time. The mixture is kept for maintaining acid value of biodiesel. The alkaline anion exchange resin is alkaline styrene anion exchange resin 201X2, 201X4, 201X7, 202X7, 201X8, D290, D296, D201, D261, D280, D284, D262, D201GF, D301R, D301G, D371, D392, D380 or D382. Potassium hydroxide is added to the mixture, and then heated at 10-80 degrees C for 1-24 hours. The acid value of biodiesel is less than 0.5mg potassium hydroxide/g.
NOVELTY - Biodiesel production involves mixing methyl alcohol, 0.8-4 wt.% concentrated sulfuric acid and 45-75 wt.% asphalt obtained from plant in a reactor (1) at normal pressure at 60-65 degrees C for 1-4 hours under stirring condition continuously. The resulting reaction product is placed into settling separator after adding water, and then kept for forming oil phase and water phase. The formed lower layer is separated, where the upper layer product is placed into degassing tower (3) for removing product impurities including water vapor and methanol gas to obtain crude methyl ester in liquid state.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method produces biodiesel by using asphalt obtained from plant in a simple and cost-effective manner with high conversion rate and high purity on industrial scale.    DETAILED DESCRIPTION - Biodiesel production involves mixing methyl alcohol, 0.8-4 wt.% concentrated sulfuric acid and 45-75 wt.% asphalt obtained from plant in a reactor (1) at normal pressure at 60-65 degrees C for 1-4 hours under stirring condition continuously. The resulting reaction end product is placed into settling separator after adding water, and then kept for forming oil phase and water phase. The formed lower layer is separated, where the upper layer product is placed into degassing tower (3) for removing product impurities including water vapor and methanol gas to obtain crude methyl ester in liquid state. The obtained crude methyl ester is placed into coarse methyl ester negative pressure suction tower which is connected with a pressure reducing rectifying tower for performing distillation at 180-240 degrees C to get biodiesel in bottom.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biodiesel production method. (Drawing includes non-English language text).    Reactor (1)    Sedimentation separator (2)    Degassing tower (3)    Methanol rectifying tower (4)    Vacuum system (5)
NOVELTY - Fermentation device comprises hydrolysis feed cabin (24), heating feeder (25), hydrolysis feed heater (26), homogeneous chemical hydrolysis feed cabin (10), hydrolyzing material inoculator (13), fermenting cabin (11), a hydrolysis feed distributor (14), hydrolyzing material thruster (16-1 to 16-5), hydrolyzing material outlet (15), discharging cabin (12), hydrolyzing device (20) and circulation fan (23). The discharging cabin is connected with discharging cabin. The fermenting cabin is made of reinforced concrete body.    USE - Fermentation device for fermenting biogas.    ADVANTAGE - The fermentation device is cost-effective and convenient to use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for fermenting biogas, which involves:    (A) fermenting the biomass by mixing mixture feed in a compartment;    (B) heating the material in the hydrolysis feeder;    (C) inoculating the homogenized mixture in the compartment; and    (D) realising the pressure of the air flow.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fermentation device.    Homogeneous chemical hydrolysis feed cabin (10)    Fermenting cabin (11)    Discharging cabin (12)    Hydrolyzing material inoculator (13)    Hydrolysis feed distributor (14)    Hydrolyzing material outlet (15)    Hydrolyzing material thruster (16-1 to 16-5)    Hydrolyzing device (20)    Circulation fan (23)    Hydrolysis feed cabin (24)    Heating feeder (25)    Hydrolysis feed heater (26)
NOVELTY - The device has a pre-heater and a heat exchanger whose heat medium outlets are connected with an inlet of an evaporator. The negative pressure evaporator steam outlet is connected with heat medium inlet and heat medium outlet of the heat exchanger through a steam pipeline of the heat exchanger. The heat exchanger is connected with the heat medium inlet and heat medium outlet of the pre-heater. The negative pressure evaporator is connected with a liquid fertilizer discharge port and a filter-biology drying device by a concentrate liquid pipeline.    USE - Negative pressure urine collecting device used in public toilet.    ADVANTAGE - Since the negative pressure urine collecting device is featured with a simple structure, the device is operated conveniently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a negative pressure urine collecting method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the negative pressure urine collecting device. (Drawing includes non-English language text)
NOVELTY - Preparing biodiesel oil using wild apricot oil comprises (i) adding adsorbent into wild apricot oil, removing solid impurities, absorbing and refining to remove phospholipid and free fatty acid, (ii) mixing wild apricot oil with methanol and alkali catalyst, stirring uniformly, and reacting, (iii) precipitating and separating glycerol, (iv) mixing the resulting product with methanol and alkali catalyst, stirring and reacting, where the adding of methanol is 20-70% of methanol added in the step (ii), (v) precipitating and separating glycerol, and (vi) washing with water and drying.    USE - The method is useful for preparing biodiesel oil using wild apricot oil (claimed).    ADVANTAGE - The biodiesel oil meets national standard GB/T20828 oil requirements. The method is simple, reduces loss of materials and chemical consumption, does not discharge waste, and produces good quality product.    DETAILED DESCRIPTION - Preparing biodiesel oil using wild apricot oil comprises (i) adding adsorbent into wild apricot oil, removing solid impurities, absorbing and refining to remove phospholipid and free fatty acid, (ii) mixing wild apricot oil with methanol and alkali catalyst, stirring uniformly, and reacting at 40-70 degrees C for 10-60 minutes under normal pressure, where molar ratio of wild apricot oil and methanol is 1:2-4, (iii) precipitating and separating glycerol, (iv) mixing the resulting product with methanol and alkali catalyst, stirring and reacting at 40-70 degrees C for 20-60 minutes under normal pressure, where the adding of methanol is 20-70% of methanol added in the step (ii), (v) precipitating and separating glycerol, and (vi) washing with water and drying.
NOVELTY - Solid biological granular fuel comprises 11-19 pts. rice straw powder, 100-120 pts. corn straw powder, 20-35 pts. sunflower straw powder, 25-32 pts. coal slurry, 50-60 pts. soybean straw powder, 14-20 pts. rice cake, 14-23 pts. rice bran, 6-9 pts. camphor tree branch, 20-30 pts. rice hull powder, 10-15 pts. chicken manure and 5-10 pts. peat.    USE - Used as solid biological granular fuel.    ADVANTAGE - The fuel has calorific value of up to 5000 kilocalories, good ventilation property, good thermal efficiency, reduces ignition point and increases combustion from 1.5 hours to more than 3 hours.
NOVELTY - Preparation of biodiesel involves adding adsorbent to Xanthoceras sorbifolia oil, removing phospholipids and free fatty acid, obtaining refined Xanthoceras sorbifolia oil, mixing refined oil with methanol and alkali catalyst, stirring, reacting, performing sedimentation of resultant product, separating glycerol, mixing resultant product with methanol and alkali catalyst, stirring, reacting at 40-70 degrees C for 20-60 minutes, performing sedimentation reaction of resultant product, separating glycerol, washing resultant material with water and drying.    USE - Preparation of biodiesel (claimed).    ADVANTAGE - The method enables economical and simple preparation of biodiesel having high quality with high conversion rate, reduced chemical consumption and suppressed generation of waste.    DETAILED DESCRIPTION - Preparation of biodiesel involves adding adsorbent to Xanthoceras sorbifolia oil, removing phospholipids and free fatty acid, obtaining refined Xanthoceras sorbifolia oil, mixing reined oil with methanol and alkali catalyst, stirring, reacting at 40-70 degrees C for 10-60 minutes, performing sedimentation of resultant product, separating glycerol, mixing resultant product with methanol and alkali catalyst, stirring, reacting at 40-70 degrees C for 20-60 minutes, performing sedimentation reaction of resultant product, separating glycerol, washing with water and drying. The molar ratio of Xanthoceras sorbifolia oil and methanol is 1:2-4. The concentration of methanol is 20-70%.
NOVELTY - System (10) comprises (a) separation tank (14) for separating waste into solid and liquid wastes, (b) fermentation tank (16) for performing anaerobic fermentation of the solid waste to obtain biogas, (c) first gas processing unit (18) for purifying the biogas, (d) power generation unit (21) for subjecting purified biogas to combustion for generating power, and (e) algal culture unit (22) connected with the first gas processing unit.    USE - The system and method are useful for bio-green waste treatment, preferably agricultural waste treatment, (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for bio-green waste treatment, which involves adding waste and/or odor component to the separating tank, separating waste into solid waste and liquid waste, subjecting the solid waste to anaerobic fermentation to produce biogas, passing the biogas to the first gas processing unit provided with algal solution for purifying the biogas, conveying purified biogas to the power generation unit for combusting purified biogas to generate power and produce exhaust gas, and introducing the exhaust gas into the algal culture unit.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of system for bio-green waste treatment.    System (10)    Interior space (12)    Separation tank (14)    Fermentation tank (16)    First gas processing unit (18)    Power generation unit (21)    Algal culture unit (22)    Aeration tank (24)    Second gas processing unit (26)    Aeration tower (182)    Reaction tower (184)
NOVELTY - Biological organic fertilizer comprises 10-25 % potassium fertilizer, 15-25 % filler, 1-5 % bacteria, 1-3 % ferrous sulfate, 1-15 % humic acid and up to 100 % molasses waste, where molasses waste comprises 35-95 % organic matter.    USE - Biological organic fertilizer used for promoting growth of lotus (claimed) and preventing root rot disease.    ADVANTAGE - The biological organic fertilizer is economic and has high nutritional value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biological organic fertilizer, which involves:    (A) mixing nitrogenous fertilizer, phosphate fertilizer, potassium fertilizer, filler, bacteria, ferrous sulfate, humic acid and molasses waste to obtain mixture;    (B) fermenting mixture for 16-28 hour under room temperature to obtain fermentation product;    (C) adding nitrogenous fertilizer, phosphate fertilizer and molasses waste into fermentation product and then stirring to obtain another mixture; and    (D) drying obtained mixture and then granulating to obtain the product.
NOVELTY - Preparing solid alkali catalyst comprises mixing sodium metasilicate nonahydrate, calcium oxide and potassium fluoride dihydrate in a mole ratio of 2:5:(1.5-3), grinding the mixture to pasty, drying the paste at 70-90 degrees C for 5-7 hours and baking the paste at 300-500 degrees C for 3.5-4.5 hours.    USE - The solid alkali catalyst is useful in biological diesel oil preparation technology field.    ADVANTAGE - The solid alkali catalyst can be prepared with good solid base catalysis effect in simple manner.
NOVELTY - A sodium metasilicate nonahydrate, calcium oxide and potassium fluoride dihydrate in molar ratio of 2:5:1.5-6 are mixed and ground. The mixture is low-temperature dried at 70-90 degrees C for 5-7 hours, and low-temperature baked at 400-450 degrees C for 3.5-4.5 hours, to obtain sodium metasilicate/calcium oxide/potassium fluoride solid alkali catalyst.    USE - Preparation of solid alkali catalyst used for preparing biodiesel.    ADVANTAGE - The method enables preparation of solid alkali catalyst having excellent catalytic characteristics, by simple method.
NOVELTY - Preparing solid alkali catalyst comprises mixing zinc oxide, calcium hydroxide and potassium fluoride dihydrate in a mol ratio of 2:1:(1.5-2), adding deionized water to the obtained mixture in a mole ratio of (2.5-3.5):16, drying the mixture at 70-90 degrees C for 5-7 hours and lower baking the mixture at 250-500 degrees C for 5-7 hours.    USE - The solid alkali catalyst is useful in biological diesel oil preparation technology field.    ADVANTAGE - The solid alkali catalyst can be prepared with good solid base catalysis effect in simple manner.
NOVELTY - A sodium metasilicate nonahydrate, calcium oxide and potassium fluoride dihydrate in molar ratio of 2:5:1.5-6 are mixed and ground. The mixture is low-temperature dried at 70-90 degrees C for 5-7 hours, and low-temperature baked at 450-500 degrees C for 3.5-4.5 hours, to obtain sodium metasilicate/calcium oxide/potassium fluoride solid alkali catalyst.    USE - Preparation of solid alkali catalyst used for preparing biodiesel.    ADVANTAGE - The method enables preparation of solid alkali catalyst having excellent catalytic characteristics, by simple method.
NOVELTY - 0.05-0.50 %Mass phosphoric acid is added to raw material, reacted, 1-5 %mass water is added, continuously reacted at 70-90 degrees C for 2-10 hours is centrifuged. The resultant material is heated at less than 390 degrees C, to obtain oil vapor, catalytic cracking of oil vapor is carried out, condensed and maintained, to obtain mixed oil of upper layer. The mixed oil and methanol are reacted in presence of acid catalyst, the resultant reaction mixture is maintained, layered, the upper layer of the mixed oil is separated, washed with water to pH of neutral and fractionated, to obtain biodiesel.    USE - Production of biodiesel (claimed).    ADVANTAGE - The method provides biodiesel with high quality, by simple and economical process.    DETAILED DESCRIPTION - 0.05-0.50 %Mass phosphoric acid is added to raw material, reacted at 70-90 degrees C for 30-90 minutes, 1-5 %mass water is added, continuously reacted at 70-90 degrees C for 2-10 hours is centrifuged. The resultant material is heated at less than 390 degrees C, to obtain oil vapor, catalytic cracking of oil vapor is carried out, condensed and maintained, to obtain mixed oil of upper layer. The mixed oil and methanol are reacted in presence of 0.5-3 %mass acid catalyst at 65-70 degrees C for 2-3 hours, the resultant reaction mixture is maintained, layered, the upper layer of the mixed oil is separated, washed with water to pH of neutral, fractionated and less than 205 degrees C fraction and 205-360 degrees C fraction are collected, to obtain biodiesel. The raw material is chosen from waste oil, acidified oil and waste animal fat. The molar ratio of mixed oil and methanol is 1:1.5-2.1.
NOVELTY - A plant oil is recovered from waste clay by extracting plant oil in waste clay until waste clay oil rate is less than or equal to 2%, separating extraction solvent and oil by fractionation, reusing extraction solvent, adding methanol and sulfuric acid in oil in which molar ratio of methanol:oil is 8-9 and weight ratio of sulfuric acid:oil is 0.01-0.02, performing esterification at 30-65 degrees C for 30-120 minutes until free fatty acid content is less than or equal to 2%, distilling esterified oil at 105-120 degrees C to remove residual methanol and water until moisture content is less than or equal to 0.5%, and adding methanol and basic catalyst.    USE - Recovery of plant oil from waste clay (claimed).    ADVANTAGE - Recovery process has no spontaneous combustion risk, low cost, increased yield, and high conversion rate.    DETAILED DESCRIPTION - A plant oil is recovered from waste clay by extracting plant oil in waste clay until waste clay oil rate is less than or equal to 2%, separating extraction solvent and oil by fractionation, reusing extraction solvent, adding methanol and sulfuric acid in oil in which molar ratio of methanol:oil is 8-9 and weight ratio of sulfuric acid:oil is 0.01-0.02, performing esterification at 30-65 degrees C for 30-120 minutes until free fatty acid content is less than or equal to 2%, distilling esterified oil at 105-120 degrees C to remove residual methanol and water until moisture content is less than or equal to 0.5%, adding methanol and basic catalyst in which molar ratio of methanol:oil is 12 and weight ratio of basic catalyst:oil is 0.01-0.02, performing transesterification at 60-70 degrees C for 30-60 minutes to convert oil to methyl ester and glycerol, separating methyl ester and glycerol, standing to deposit large proportion of glycerol to bottom by gravity, isolating methyl ester with lighter weight, neutralizing, washing, separating water, and distilling to remove residual basic catalyst, methanol, and water.
NOVELTY - A biodiesel is prepared by adding lipid, aliphatic alcohol, and solid alkali in reaction container, performing transesterification in which solid alkali is zinc oxide(ZnO)/calcium hydroxide (Ca(OH)2)/potassium fluoride (KF) and sodium silicate (Na2SiO3)/calcium oxide (CaO)/KF mixture, heating, controlling hourly volume space velocity, placing reaction solution in conical container, distilling to remove fatty alcohol, separating glycerol, adding nonionic surfactant, and filtering using ceramic membrane film to separate fatty acid monoglyceride and obtain high purity biodiesel.    USE - Preparation of biodiesel (claimed).    ADVANTAGE - The method is simple, does not result to saponification product accumulation, produces high purity glycerol by product, requires low transesterification temperature and pressure, has high yield, and low cost, raw materials are adaptable, and product has high purity.    DETAILED DESCRIPTION - A biodiesel is prepared by adding 1-4 mass% lipid, aliphatic alcohol, and solid alkali in reaction container, performing transesterification in which solid alkali is ZnO/Ca(OH)2/KF and Na2SiO3/CaO/KF solid mixture, and molar ratio aliphatic alcohol:lipid is (8-15):1, heating under water bath condition at 50-80 degrees C and 2-6 MPa, controlling hourly volume space velocity at 0.3-4/hour, placing reaction solution in conical container, distilling to remove fatty alcohol, separating glycerol, adding 0.1-10 mass% not less than 1 nonionic surfactant as filter aid, and filtering using ceramic membrane film to separate fatty acid monoglyceride and obtain high purity biodiesel in which hydrophilic-lipophilic balance value of nonionic surfactant is 3-25, film material is inorganic carbon film i.e. aluminum oxide or titanium oxide, ceramic film aperture is 0.02-1.4 mu m, membrane separation temperature is 10-120 degrees C, and membrane separation pressure is 0.08-0.5 MPa.
NOVELTY - Fuel comprises 44-70 wt.% of methanol, 8-20 wt.% of ethyl alcohol, 10-25 wt.% of aromatic hydrocarbon, 2-7 wt.% of emulsifier, 1-5 wt.% of corrosion inhibitor, and 0.5-1.5 wt.% of paraffin oil. The emulsifying agent is a mixture of acetone and methyl acetate. The corrosion inhibitor is acetic acid tert-butyl ester, acetic acid isobutyl ester or ethyl acetate.    USE - The fuel is useful in a vehicle (claimed).    ADVANTAGE - The fuel has good combustion property, stability, anti-corrosive property and combustion property, and strong water resistance.
NOVELTY - A blended fuel comprises 25-40 wt.% gasoline, 20-38 wt.% methanol, 8-18 wt.% ether which is diisobutyl ether, tetraamyl methyl ether, methyl tert.-butyl ether, ethyl tert.-amyl ether, and diisopropyl ether mixture, 5-13 wt.% ester which is acetate, glycerol monostearate, methyl acetate, and propyl nitrate mixture, and 10-20 wt.% low-carbon alcohol which is glycerol, isobutanol, butanol, isopropanol, ethanol, and tert.-butanol mixture.    USE - Blended fuel for vehicle (claimed).    ADVANTAGE - Fuel has improved fuel performance, reduced emission and sulfur content, and lower cost.
NOVELTY - Producing biodiesel comprises (i) adding oil, fatty alcohol and solid base into a reaction kettle, carrying out transesterification, heating the reaction kettle in the water bath; (ii) placing the reaction mixture in conical retort, distilling off the fatty alcohol, and separating glycerin; (ii) adding non-ionic surfactant as a filter aid into the obtained mixture, separating fatty acid monoglyceride through the ceramic membrane to obtain high purity biodiesel.    USE - The method is useful for producing biodiesel (claimed).    ADVANTAGE - The biodiesel has high purity, glycerol concentration, yield, and low cost.    DETAILED DESCRIPTION - Producing biodiesel comprises (i) adding oil, fatty alcohol and solid base into a reaction kettle, carrying out transesterification, where the solid base is zinc oxide/calcium hydroxide/potassium fluoride and disodium silicate mixture and the oil accounts for 1-4 mass%, heating the reaction kettle in the water bath at 50-80 degrees C under pressure of 2-6 MPa, where the molar ratio of aliphatic alcohol with oil is 8-15:1, and the reaction liquid hourly space velocity is 0.3-4/hour; (ii) placing the reaction mixture in conical retort, distilling off the fatty alcohol, and separating glycerin; (ii) adding at least one non-ionic surfactant as a filter aid into the obtained mixture, separating fatty acid monoglyceride through the ceramic membrane to obtain high purity biodiesel, where the non-ionic surfactant has hydrophilic-lipophilic balance value of 3-25, and the nonionic surfactant adding amount is 0.1-10 wt.%; the ceramic membrane is ceramic support material, the membrane material uses inorganic carbon, aluminum oxide or titanium oxide as inorganic film, the ceramic membrane pore size is 0.02-1.4 mu m, and the membrane separation is carried out at 10-120 degrees C, and the transmembrane pressure is 0.08-0.5 MPa.
NOVELTY - Biodiesel preparation involves adding lipid, fatty alcohol and a mixture of zinc oxide, calcium hydroxide and potassium fluoride into a reaction kettle, and then heating the reaction kettle at 50-80 degrees C temperature and 2-6 megapascal pressure to obtain a reaction mixture. The reaction mixture is placed in conical retort to separate alcohol and glycerin. Nonionic surfactant is added to the mixture, and then treated with a material. The material is selected from carbon, alumina or titanium oxide.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method enables preparing biodiesel with high yield in a simple and cost-effective manner.    DETAILED DESCRIPTION - Biodiesel preparation involves adding lipid, fatty alcohol and a mixture of zinc oxide, calcium hydroxide and potassium fluoride into a reaction kettle, and then heating the reaction kettle at 50-80 degrees C temperature and 2-6 megapascal pressure to obtain a reaction mixture. The reaction mixture is placed in conical retort to separate alcohol and glycerin. Nonionic surfactant is added to the mixture, and then treated with a material. The material is selected from carbon, alumina or titanium oxide. The product is filtered through ceramic membrane, and then processed at 10-120 degrees C temperature and 0.08-0.5 megapascal pressure to obtain the desired product.
NOVELTY - Waste fluids treatment involves contacting effluent with biomass in an anaerobic tank, and introducing the resulting mixture into a tank in which membrane filtration is performed under strong agitation by biogas bubbling. The treated water is separated from the biomass by returning to the anaerobic tank overflow contact by ascension effect of the biogas bubbles. The biogas recirculation is occurred in upper portion of both tanks towards lower portion of the tank.    USE - Method for treating waste fluids containing organic oils and fats.    ADVANTAGE - The method facilitates anaerobic treatment of waste fluids containing high lipid content, minimizes shear forces characteristics of other pumping methods, and allows adequate filtration for anaerobic beta-oxidation of long chain fatty acids, and energetic valorization of the residual material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the waste fluids treatment method.    Anaerobic reactor (1)    Filtration tank (2)    Submerged membrane system (3)    Treated water (5)    Biogas (9)
NOVELTY - This utility model relates to a hot gas generation device for drying tea, comprising a furnace body, a wind conveyor, an exhaust channel, a diffusion plate, and the first clapboard, second clapboard, the third clapboard, fire plate, the first wood gasification room, second wood gasification room, wood pneuma chemical tank, a hearth, a fixing plate, a heating tube, support leg, the first baffle, second baffle and seal door. A tea drying a pneuma one generator The utility new type provide a, satisfy each item technology The drying of tea, the tea production and application of a drying hot air tea happen metal furnace has sufficient combustion, soot discharged at least a pneuma and energy-saving environment-friendly structure design is reasonable and operation is convenient, the cost is the tea production and application of a tea drying hot metal furnace. happen, a non-pressure boiler is without tempering and gas leakage phenomenon, high safety performance.
NOVELTY - Method for preparing organic fertilizer, involves (a) weighing fresh cow dung, and water-absorbent resin powder, mixing weighed raw materials uniformly, adjusting water content of cow dung, and then allowing mixture to stand, (b) adding microbial agent to mixture, obtained in step (a) and mixing uniformly, (c) adding mixture into anaerobic fermentation tank, and performing an anaerobic fermentation, and (d) collecting fermented material, drying fermented material at room temperature, crushing dried material and packing to obtain the product.    USE - The method is useful for preparing organic fertilizer which is used for cultivating crop and vegetables (all claimed).    ADVANTAGE - The prepared fertilizer enables to increase yield of crop and vegetables.    DETAILED DESCRIPTION - Method for preparing organic fertilizer, involves (a) weighing fresh cow dung, and water-absorbent resin powder, mixing weighed raw materials uniformly, adjusting water content of cow dung to 60-70%, and then allowing mixture to stand for 12-24 hours, (b) adding 0.001-2% microbial agent to mixture obtained in step (a), and mixing uniformly, (c) adding mixture obtained in step (b) into anaerobic fermentation tank, and performing an anaerobic fermentation at 45-65 degrees C for 20-30 days, and (d) collecting fermented material from fermentation tank, drying fermented material at room temperature, crushing dried material and packing to obtain the product.
NOVELTY - Corn special fertilizer (100 wt.%) comprises 15-25 wt.% chicken manure, 30-50 wt.% quail manure, 6-15 wt.% phosphate rock, 6-15 wt.% humic acid, 6-15 wt.% urea, 6-15 wt.% potash fertilizer and 1-3 wt.% microorganism. The fertilizer is prepared by mixing chicken manure, quail manure and humic acid and stirring mixture, maintaining 45-48% water content in mixture, fermenting mixture using microorganism, maintaining 25% water content in the fermented product, mixing product with remaining raw materials and crushing mixture into powder, sieving and granulating powder.    USE - As corn special fertilizer (claimed).    ADVANTAGE - The special fertilizer increases corn yield and improves quality and disease resistance capacity.    DETAILED DESCRIPTION - Corn special fertilizer (100 wt.%) comprises 15-25 wt.% chicken manure, 30-50 wt.% quail manure, 6-15 wt.% phosphate rock, 6-15 wt.% humic acid, 6-15 wt.% urea, 6-15 wt.% potash fertilizer and 1-3 wt.% microorganism. The fertilizer is prepared by mixing chicken manure, quail manure and humic acid and stirring the mixture, maintaining 45-48% water content in the mixture, fermenting the mixture using microorganism for 20 days, where the mixture is turned once after 12 days, maintaining 25% water content in the fermented product, mixing the product with remaining raw materials and crushing mixture into powder, sieving and checking powder, and granulating powder.
NOVELTY - Bioorganic fertilizer comprises 100 kg organic matter and 1-2 kg microbial composition comprising Bacillus subtilis, B.licheniformis and yeast.    USE - As bioorganic fertilizer.    ADVANTAGE - The bioorganic fertilizer improves soil fertility, and provides long lasting effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) taking 60-70 %mass furfural residue and 30-40 %mass fresh cow dung as raw materials, adding microbes to the raw materials, fermenting the mixture at 10-30 degrees C for 3-5 days, and drying the fermented product until moisture content reaches less than 30 wt.%, and (b) mixing product obtained in step (a) and microbial composition, crushing the mixture to particle size of 100 meshes, and drying the crushed product at 70-80 degrees C for 1 minute.
NOVELTY - The biogas tank comprises an input sub-tank, an output sub-tank, a main tank composed of two semi-spherical condensed halves comprising an upper halve and a lower halve sealingly attached together, an air collecting pipe, an input pipe, and a residue exhaust pipe. The main tank is present in a spherical form with high load bearing capacity. The upper halve is provided with a top auxiliary portion in a semi-spherical form and superposed on a bottom auxiliary portion. The input sub-tank and output sub-tank are in spherical form and narrow at the top.    USE - The biogas tank is useful for treating waste and generating biogas (claimed).    DETAILED DESCRIPTION - The biogas tank comprises an input sub-tank, an output sub-tank, a main tank composed of two semi-spherical condensed halves comprising an upper halve and a lower halve sealingly attached together, an air collecting pipe, an input pipe, and a residue exhaust pipe. The main tank is present in a spherical form with high load bearing capacity. The upper halve is provided with a top auxiliary portion in a semi-spherical form and superposed on a bottom auxiliary portion. The input sub-tank and output sub-tank are in spherical form and narrow at the top. The input pipe, the residue exhaust pipe and the air collecting pipe are fixedly mounted in the tank. The input pipe is disposed higher than the residue exhaust pipe. A recessed portion on the upper halve is smaller than a recessed portion on the lower halve.
NOVELTY - This new utility model claims of one type of high temperature carbonizing furnace, comprising a furnace body, a furnace body set with inner combustion cavity, gas collection pipe and transmission device, a furnace body top and bottom respectively provided with feedstock and wherein, to set with one-way feedstock inlet seal valve, equipped with one-way discharging seal valve, the top combustion cavity set with tail gas outlet, and lower part connected with, combustion cavity set with inner part of tubular guide heat insulator, a heat guide top insulator equipped with an air outlet, the air outlet connecting to gas collection pipe, upper gas collecting pipe via gas pipeline connected with combustion engine and combustion in the combustion mouth position, the transmission device comprises drive shaft, rolling shaft and transmission steel belt. This new utility model and existing technology compared with the advantages as: simple structure, reducing machine fault happen, use electric integrated, suitable use, is good for the organic matter cracking, reducing dust as combustible gas volatilized.
NOVELTY - This new utility model claims of one of organic solid waste drying carbonization integrated system, comprising preheat device, drying carbonizing integrated device and cooling device, the preheat device comprises preheat cavity body, spiral conveyor one, wherein one set with feedstock of separate hot plate and under plate and feeding conveyor, said drying carbonization integrated device comprises drying carbonization cavity, drying carbonizing in cavity body middle part, upper heat set with hot air way hole, bottom set with air board, air plate for uniformly distributing hot air, forming dry chemical in the combustion cavity and carbonization cavity, drying and carbonizing in cavity equipped with connected pipe, the cooling device comprises cooling pipe, cooling pipe set with spiral conveyor four, cooling pipe connected with discharging port one top, bottom connected with discharging port two. This new utility model and existing technology compared with the advantages as: compact structure, reduce processing cost, drying pipe and carbonization pipe adopt U type design, shortens the drying time, increase productivity, reducing dust blow out, increase energy use rate.
NOVELTY - This new type utility claims one a biogas desulfurizing tower, comprising a tower body, upper end of the tower body is set with an air outlet, the tower body from up below include removing fog area, spraying area, absorbing area and slurry area, absorbing area connecting with the air inlet, further comprising a. one section inner demister removing the fog area and a section of a demister, set with a spraying device of the spraying inner area, set with a stirrer and the slurry circulation pump is a slurry area side edge, input end of the slurry circulation pump and a slurry area a, output end of the slurry circulation pump and a spraying device connection. This utility new type provide the one a biogas desulfurizing tower, using the one segment unique a demister, a demister section and spraying device, each valid part of arrangement, and of the interval a between in the most suitable range of inner, so solves the problem that the existing technology in use to a biogas desulfurizing tower, and most of the structure design of efficiency caused by unreasonable and deviation is low is solved.
NOVELTY - This new utility model claims of one of organic solid waste high temperature carbonization system, including between a furnace body, a drying chamber and carbonization chamber, drying chamber and carbonizing chamber equipped with heat insulating interlayer, inside the drying chamber provided with transmission device and one infrared heating tube, the inner carbonizing chamber equipped with combustion cavity, gas collection pipe and top transmission device two; the combustion cavity set with tail gas outlet, and lower part connected with, combustion cavity set with inner part of tubular guide heat insulator, a heat guide top insulator equipped with an air outlet, the air outlet connecting to gas collection pipe, gas collecting pipe via gas pipeline connected with combustion engine and combustion in the combustion port to upper part. This new utility model and existing technology compared with the advantages as: simple structure, reducing machine malfunction generating; increasing release space of combustible gas, which is good for the organic matter cracking, reducing dust as combustible gas volatilized, then influence the combustion and dust and combustible gas and back backlog and issue process.
NOVELTY - This utility new type relates to biogas engineering with fermentation jar technology field, specific relates to a methane fermentation jar one mix device, a fermentation jar comprising a cylindrical jar body and semi-spherical top of the external tank body set with water pump, a tank body by lower to upper in turn. pipeline, mixed pipeline, a pipeline pipeline, pipeline, pipeline and mixed pipeline through a valve, mixed valve and valve and water pump water outlet is connected with water pipeline through water valve and water pump pumping opening is connected with mixed pipeline from one side is inserted into the tank body, and a vertical distance between the tank body centre shaft is jar body bottom circle radius is 0.6-0.8 times of the pipeline is set on one end inner jar body is a closed structure, inserting a part inner jar body is set with a a opening. This utility new type has simple structure, is convenient to use, enhance the biogas slurry mixed effect, increase the utilization rate, reduce energy consumption, if a failure occurs in a process operation, without need to empty fermentation tank, time saves time and labour force.
NOVELTY - This utility new type refers to a processing device, one is a centralized drying, smoke venting integrated welding table multi-rod combined unit, comprising a multi-rod machine welding table along one line in parallel to arrangement is provided with a centralized feeding, uniformity of add material system, a drying system, a smoke system and finished product conveying screen, a, the utility model is new type solves the problem that the current single-rod machine welding table independently processing a low efficiency, high energy consumption, a high cost, environment pollution, this utility new type is mainly used for the sawdust, crop straw, branch, bamboo, peanut shell, sunflower seed shell, furfural residue, cotton pole, pole, corn stalk, corn core and each of shrub, residual branch and so on by crushing, drying after processing of raw material, a pressurizing and heating a is made .
NOVELTY - Device comprises a tubular shapes furnace in which a gas outlet is formed for leading condensation of different fractions of oil and water mixture at different temperatures.    USE - Device for performing controlled pyrolysis of waste composite product (claimed).    ADVANTAGE - The device enables performing controlled pyrolysis of waste composite product in a simple and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for performing controlled pyrolysis of waste composite product.
NOVELTY - Energy crop biomass and by-products production involves planting species Nicotiana tabacum in greenhouses, providing seeds in special nurseries under controlled conditions to achieve germination and seedling growth. The seedlings are planted in field for a predetermined period, where the plants are harvested two or three times after mowing in a year by cutting approximately 2-3 cm above the ground to obtain a green mixed biomass crop. The obtained green biomass is dehydrated at 80-90 degrees C, and then refined the dried biomass by crushing, grinding and sieving to separate pure seeds.    USE - Method for producing crop biomass and by-products for producing biodiesel or cattle feed.    ADVANTAGE - The method produces crop biomass and by-products in a simple and cost-effective manner, and improves importance of Nicotiana tabacum species.    DETAILED DESCRIPTION - Energy crop biomass and by-products production involves planting species Nicotiana tabacum in greenhouses, providing seeds in special nurseries under controlled conditions to achieve germination and seedling growth. The seedlings are planted in field for a predetermined period, where the plants are harvested two or three times after mowing in a year by cutting approximately 2-3 cm above the ground to obtain a green mixed biomass crop. The obtained green biomass is dehydrated at 80-90 degrees C, and then refined the dried biomass by crushing, grinding and sieving to separate pure seeds. The pure and dried biomass is separated as a thermal power source, where the seeds are pressed through a hot pressing process at 80-100 degrees C to get bio-oil.
NOVELTY - This utility new type relates to one with a generation device of garbage processing device, garbage dry distillation furnace including the garbage coking process unit, a garbage carbon treatment unit, a cooler and a generation. Garbage carbonization furnace set with combustion room, a feeding port, a furnace body, a hearth and waste carbon residue outlet, lower part of the hearth set with decomposition pneuma outlet. The combustion room is one head set with burner, the other one head and waste heat boiler connected. Set with fuel nozzle burner and air entrance. The waste heat boiler is set with steam coil pipe, a steam disk pipe connecting to power device, lower part of boiler is set with a slag pool, pool set with slag. Decomposing pneuma outlet connecting to the garbage coking process unit, a garbage carbon outlet through a cooler to garbage carbon processing unit. This utility new type the garbage processing device and generation device of combine, the high temperature smoke pneuma of garbage processing process used for generation, processing the waste, eliminate the pollution, but also changes waste into value and rationally use the a resource. (ESM) of the invention is the invention patent with daily
NOVELTY - This new type utility claims one solar energy carbon dioxide a microwave through photocatalysis of fuel device, comprising water pool, carbon dioxide jar, a remote anti-explosion catalytic tube, catalytic groove and transverse catalytic core, lengthways catalytic core, a remote anti-explosion monitor, combustible gas jar, the liquid fuel tank, microwave power supply, a magnetron, a solar energy water heater, an air energy water heater and a remote anti-explosion detection system. A carbon dioxide pressure pulse and microwave induced catalytic, produce liquid fuel (such as methanol, formic acid, t-butylperoxy) and a combustion gas (carbon monoxide, hydrogen, a), a carbon dioxide energy use is; and this reaction process by a simplified operation step, a valid conversion of high technology.
NOVELTY - A hydraulic pressure driving granulator comprises cutter plate (1), cutting knife (2), chopping block (3), hole (4), slide blushing (31), multi-knife blade, hydraulic block, and pushing mechanism.    USE - Hydraulic pressure driving granulator used for weed suppression and straw fuel plate.    ADVANTAGE - The granulator has granular fuel combustion property and avoids too small particles and pressing plate burning effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of hydraulic pressure driving granulator.    Cutter plate (1)    Cutting knife (2)    Chopping block (3)    Hole (4)    Slide blushing (31)
NOVELTY - The device comprises a raw material inlet, an air flow vortex crusher, an air blower, an injector, a reaction furnace, an integrated reaction device, a heater, a vent pipe, a panel, a green algae plant, a light source, an exhaust port, a reaction area, an absorbing area, a plant photosynthesis area. The raw material inlet, air flow vortex crusher, air blower, injector, reaction furnace and integrated reaction device are connected with an upper and lower part of reaction area. The injector is provided with gas injection device.    USE - The device is useful for reducing carbon dioxide in a biomass gas (claimed).    ADVANTAGE - The device simply and economically reduces the carbon dioxide in the biomass gas in an eco-friendly manner.    DETAILED DESCRIPTION - The device comprises a raw material inlet, an air flow vortex crusher, an air blower, an injector, a reaction furnace, an integrated reaction device, a heater, a vent pipe, a panel, a green algae plant, a light source, an exhaust port, a reaction area, an absorbing area, a plant photosynthesis area. The raw material inlet, air flow vortex crusher, air blower, injector, reaction furnace and integrated reaction device are connected with an upper and lower part of the reaction area. The injector is provided with a gas injection device. The reaction furnace is provided with a fluidized bed type carbonization furnace.
NOVELTY - Preparing fuel rod comprises primarily mixing blue carbon powder and biomass powder, combustion improver, sulfur-fixing agent and bentonite to obtain a first mixed material, secondarily mixing the first mixed material and an adhesive to obtain a second mixture material, using a ring module molding machine for molding the second mixed material to obtain a molding material, and then drying the molding material.    USE - The method is useful for preparing fuel rod (claimed).    ADVANTAGE - The fuel rod: has low volatile content, low sulfur content and high heat productivity; is economical; can replace anthracite in suburbs village or entire country rural areas during warming and cooking in winter season; can greatly reduce the haze; and improves the air quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the fuel rod prepared by the above mentioned method.
NOVELTY - Preparation of low-viscosity soybean oil methyl ester involves mixing soybean oil and methanol, carrying out transesterification of methanol and soybean oil under catalysis of solid super-acid or solid super-alkali into triglyceride, adding saturated brine solution to the resultant product, centrifuging at high speed of 1000-3000 rpm for 15-40 minutes, removing lower aqueous phase, and obtaining upper layer of soybean oil methyl ester.    USE - Preparation of low-viscosity soybean oil methyl ester used for bio-diesel and printing inks, and as cleaning agent.    ADVANTAGE - The method enables environmentally-friendly preparation of low-viscosity soybean oil methyl ester having reduced emission of volatile organic compounds and staining.
NOVELTY - Device comprises a main chamber (3), which is provided with a lower main chamber for receiving biomass. The lower portion of the main chamber is provided with a grinding unit (5), a cutting unit (18) and an air vent. The air vent (7) rotates the cutting unit, which is installed on the lower end of the main chamber to produce whirlpool. The inner side of the main chamber is provided with an outlet (17) and a flange (21), where flange connects lower portion of the main chamber with outer chamber.    USE - Device for processing biomass feedstock (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device.    Main chamber (3)    Grinding unit (5)    Air vent (7)    Outlet (17)    Cutting unit (18)    Flange (21)
NOVELTY - The device has a device body provided with a microwave dryer (1), a feeding hoisting machine (2), a feeding hopper (3) and a feeding spiral conveying machine (4) and a microwave splitting furnace body (5). The microwave splitting furnace body is connected with a discharge spiral conveying joint. A temperature device unit is connected with a pressure detecting device unit, a safety valve and a gas pipeline system (7). A microwave feed-in system (8) is connected with a waste collecting system (9), a cooling water system, a control system (11) and an atmosphere system (12).    USE - Continuous microwave heating biomass and organic waste splitting device.    ADVANTAGE - The device reduces heating temperature and increases reaction speed, and has high biomass and organic quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a continuous microwave heating biomass and organic waste splitting device.    Microwave dryer (1)    Feeding hoisting machine (2)    Feeding hopper (3)    Feeding spiral conveying machine (4)    Microwave splitting furnace body (5)    Gas pipeline system (7)    Microwave feed-in system (8)    Waste collecting system (9)    Control system (11)    Atmosphere system (12)
NOVELTY - The device has a single cylinder connected with an air inlet that is fixed with a vertical carbonization furnace. A measuring point is fixed with the air inlet. A chimney is fixed with a top part of the vertical carbonization furnace.    USE - Mobile bar-shaped biomass molding fuel furnace carbon product yield improving device.    ADVANTAGE - The device has high molding carbon production yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a mobile bar-shaped biomass molding fuel furnace carbon product yield improving method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a mobile bar-shaped biomass molding fuel furnace carbon product yield improving device.
NOVELTY - The device has a biomass pyrolysis gasification device connected with a chemical chain making hydrogen reaction device through a pyrolysis pneumatic conveying pipe. The chemical chain making hydrogen reaction device is provided with first, second and third sections. The prolysis pneumatic conveying pipe is connected with a reaction gas entrance end. The first section is fixed with an oxidation-reduction reaction section. An oxygen carrier is fixed with an inner area of the second section. The third section is fixedly connected with an air flow buffer section.    USE - Biomass pyrolysis and thermal pyrolysis pneumatic chemical chain made hydrogen generation device.    ADVANTAGE - The device realizes hydrogen generation process in a convenient manner and reduces energy consumption rate, and has high regulating gas flow and control speed.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass pyrolysis and thermal pyrolysis pneumatic chemical chain made hydrogen generation device.
NOVELTY - The method involves conveying organic-matter-containing foreign waste water to a waste water groove. Organic substance-containing waste substance and solid impurity in water is removed. Organic substance-containing waste filtering process is performed. Organic substance-containing waste water impurity content is about 1%. Industrial pulverized coal pneumatic is formed during air and oxidized reaction process. Inner temperature of a coal generating furnace is maintained at 950-1050 degrees Celsius. Pressure force of the coal generating furnace is generated for about 4. 5-5.0 MPa.    USE - Industrial coal, gas and waste water organic matter harmless treating method.    ADVANTAGE - The method enables replacing water vapor reaction raw material by using organic waste water, maintaining coal powder and fully mixed coal gas with high temperature, and directly burning with air and oxidized to generate industrial coal, simply treating organic waste water harmless, and realizing waste water recycling operation, and reducing environmental protection pressure so as to increase enterprise benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an industrial coal, gas and waste water organic matter harmless treating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating an industrial coal, gas and waste water organic matter harmless treating method.'(Drawing includes non-English language text)'
NOVELTY - The system has a feeder (200) whose two ends are respectively connected with storage hopper (100) and wood chips grain machine (300). The storage hopper is provided for storing the wood conveying to the wood chips grain machine. An atomizing and spraying device (400) is provided at the inlet of chips grain machine for atomizing water spray to wood. A compressing air pipeline is connected with air storage device. The water pipeline and compressing air pipeline are provided with control valve.    USE - Granulating system of wooden meal product.    ADVANTAGE - The wooden meal raw material is humidified. The qualification rate of the product is improved effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a granulating method of wooden meal product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the granulating system of wooden meal product.    Storage hopper (100)    Feeder (200)    Wood chips grain machine (300)    Spraying device (400)
NOVELTY - The method involves drying a biomass granule through extrusion portion. A float grass is conveyed into an upper portion of a hopper through a conveying belt (4). The float grass is subjected to extruding process using an extruding device, and conveyed to an inner portion of an oven tank (13). The float grass is subjected to a temperature of 120 degrees C-160 degrees C for 8-12 minutes. The grass is crushed in a separator (6). The crushed grass is dehydrated. The dehydrated crushed grass is conveyed to a molding machine (2).    USE - Method for preparing biomass granule.    ADVANTAGE - The yield of the biomass granule is improved, while improving the convenient preparation of the biomass granule.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process for preparing biomass granule.    Molding machine (2)    Pressure roller (3)    Conveying belt (4)    Separator (6)    Oven tank (13)
NOVELTY - This utility new type claims a one with radiating fin of rotating furnace, comprising a rotating cylinder, a feeding system, a feeding system comprising a disc feeding machine, a scraper feeding machine and the feeding spiral machine, a disc feeding machine by the scraping plate feeding a feeding spiral machine, a feeding spiral machine is connected to rotary drum, disc feeding machine through the scraping plate feeder, a feeding spiral machine the material in a drying section part in the rotating cylinder, set with a carbonization section radiating fin part, set with heating room outside a carbonization section part, set with shovelling plates in a drying section part, the material entering into carbonizing segment rear drying in a drying carbonizing in carbonized section, discharging end of carbonization section part and material collecting cabinet a, material cabinet and carbonization material cooling of a spiral, a carbonization section and drying section temperature part of part always maintain high temperature, which avoids the leading-out pipeline and leading-out fan blocking, which ensures the production of a. This utility new type of carbonization section part with inner and outer heating both, with multiple heating function.
NOVELTY - This new type utility claims one a full mixing anaerobic reactor, the application range is wide, and it is very fit b industrial waste water treatment. A condition using a sludge or anaerobic flocculent sludge operation, degassing deposition module based on a special design, this precipitate can be turbulence in a flow of the gas under the water and mud separating, mix circulation. stir the slurry fully mix, so as to ensure efficient. Relative low volume load and optimization of a degassing precipitation system, ensuring stable operation and anaerobic sludge is increased, a time short, operation control is simple, which can satisfy for odor, sludge yield and purification level of a more severe.
NOVELTY - This utility new type claims a shut-off one biogas pool belonging to the biogas fermentation device field of technology. Marsh liquid pool by pool body, and discharging wherein compose, pool body in a part close to a feeding port set with baffle and interlayer, the bottom of pool body set with solid outlet wherein, a said insulating layer set with a honeycomb-shaped structure, honeycomb-shaped structure is attached with a deodorizing. This utility new type of partition marsh liquid pool to increase, in boarder in the pool can be valid to prevent new raw material, or flow of a raw material is not fully fermented, which ensures the liquid wherein the extraction of biogas slurry is pure, honeycomb-shaped structure and active carbon can be valid to reduce odor and gas germ, into a field of biogas slurry without peculiar smell.
NOVELTY - A one household biomass pyrolysis gas device, relating to a one gas production device, in particular one a biomass pyrolysis gas production device, by high temperature splitting furnace, water in the purifier, a fan, an air storage tank, a biomass gas stove, heat preservation hot water tank, a pipeline combination, all the combustible solid object conversion to a combustion gas, which can not only alone fine raw material and thick raw material mixed, grassland pasturing available livestock manure as raw material, plain in available straw as raw material, in mountainous area with wood as raw material, if use wood as raw material, but also can generate charcoal, rear gas not only in producing cast using a production storage and use, a produced gas without tar and impure gas, but also can be a conversion to a water storage for use in a gas production process, a easy operation, use cost is low, energy-saving and environment-friendly.
NOVELTY - This utility new type relates to one use a husbandry waste carbon-containing material producing biological carbon, of a biological vinegar and biological tar. This utility new type producing biological carbon, of a biological vinegar and biological tar, comprising pyrolysis device, a dust remover, a cooling separating tower and settling tower, a settling tower is vertically set, tower comprise shell and the inner cavity, the inner cavity is a small cone-shaped, the top part of a shell and the inner cavity is provided with a connected material wherein, in middle part of the shell and the inner cavity is provided with a connected biological vinegar outlet, lower part of shell is provided with a cavity and a connected biological tar outlet, the bottom of shell is provided with a cavity connected and a slag outlet, an air inlet of the air outlet and the pyrolysis device of connected dust remover, a dust remover air outlet and a cooling separating tower of connected air inlet, a condensing liquid outlet of cooling separating tower and feeding wherein a settling tower connected. This utility new type structure is simple, the cost is low, operation is simple, and it will not cause air pollution.
NOVELTY - Biogas purification to obtain of the biology natural gas of liquefied natural gas device, comprising refrigeration circulation system and a light system, refrigeration circulation system including cooling tank, the cooling tank with cooling inner flow channel, the flow channel is divided into evaporative cooling and deep cooling section and cooling section, removing light component comprising a rectifying tower, a flash tank, a condenser, a first decompression valve and second decompression valve, rectifying tower condenser is located above the deep-cooling section of the first throttle valve and the rectifying column is connected with one end and super-cooling section at the bottom of a rectifying tower, and the other end of cooling section in turn by the condenser, second throttle valve and flash tank is connected with the top of a rectifying tower by the condenser and the first decompression valve is connected with the top part and second decompression valve of the flash tank. The device the biological natural gas is made in a liquefied natural gas at the same time in the biology natural gas of hydrogen, nitrogen and carbon monoxide light component gas separating, that of a liquefied natural gas product, compare stable.
NOVELTY - The utility model claims a new marsh gas purification device, marsh gas purification device by water and gas cabinet sealing device connected with marsh gas purification device comprises set liquid cavity, filtering cavity, air liquid separation cavity; one end filtering cavity is set with gas entrance, the other end and gas-liquid separation cavity connected with the gas liquid separation cavity provided with gas outlet, set in respectively connected and filtering liquid cavity and gas-liquid separating cavity, provided with liquid discharge port and liquid level controller, and position on lower part of filter cavity and gas-liquid separating cavity, and cavity is set with filtration with glass fiber filter element; air liquid separation cavity provided with gas liquid separating component. After added with biogas filter separator, gas and water content, impurity would greatly reduce, saves the spare parts and engine to consume material cost, system process operation stable, production efficiency is greatly improved; the device investment running cost is low, installation use is simple and convenient.
NOVELTY - This utility new type provide a one excrement sewage processing marsh gas pool, comprising pool body and pneuma biogas bag group, the pool body from lower to upper in turn set with a whole flat layer, waterproof layer, insulating layer and thick sand layer, the sand layer thickness of inner is embedded with multiple heat pipe, a biogas pneuma bag group including the first biogas pneuma bag unit and second biogas pneuma bag unit, a biogas pneuma bag unit the first and second methane pneuma bag unit are set with a thick sand layer above the first biogas pneuma bag unit and between the second biogas pneuma bag unit through a pipeline, the first biogas pneuma bag unit of sewage entrance and the first conveying pump connected with the inlet sewage outlet and second conveying pump of second biogas pneuma bag unit is connected with a second outlet of the conveying pump is further connected and one solid-liquid separator, a first methane pneuma bag unit and the top end of second biogas pneuma bag unit are set with one methane pneuma hole, inner bottom is paved with an aeration pipe. This utility new type fermentation efficiency is high, the decomposition speed is fast, greatly increase the production efficiency, at the same time the energy consumption is low, and operation cost is low.
NOVELTY - Time in inner This utility new type claims a solar energy auxiliary heat type one. Overground fermentation cylinder for marsh gas, comprising tank (1), a solar energy heat collector (2), an air source heat pump hot water unit (3), a circulation water tank (4), a hot water tank (5) and heat exchange coil (6), heat exchange coil (6) b. marsh gas tank (1), a time comparing a strong solar radiation, use solar energy heat collector (2) to collect solar energy, through heat exchange coil (6) methane (1) in temperature stable, or without solar radiation in solar radiation, use air source heat pump hot water unit (3) is a hot water maintaining tank (1) is temperature stable. This utility new type of beneficial effect is: provide a one air source heat pump hot water device and solar energy hot water collecting heat device combined operation of device, high efficient maintaining biogas fermentation temperature, fermentation temperature to maintain the methane in a high range so as to solve solar energy collecting heat load change caused by temperature fluctuation of fermentation, and reliable operation.
NOVELTY - This utility new type claims a one solar energy electrolytic water hydrogen producing device, comprising electrolysis groove, ion exchange film, a cathode gas collecting device, an anode gas collecting device and electrolytic electrode, in which further include in sea water filter device and solar energy photovoltaic battery, electrolytic groove used for containing seawater, seawater filter device of electrolysis hydrogen electrolytic groove is connected to the sea water by the filter rear into electrolytic groove, solar energy photovoltaic battery electrically connected with one converter, converter through lead electrically connected with the male and female electrolytic electrode, using sea water as the hydrogen electrolysis raw material, water resource is enough, wide raw material source, a low cost, clean without pollution, at the same time it also can bring additional product in a electrolytic process, solar energy photovoltaic battery through the solar energy conversion a rear electric energy to a power supply cell, compared with using traditional electric power electric energy power supply has low of cost, power supply energy is enough, the pure natural advantages of without pollution.
NOVELTY - This new utility model claims of one of heat accumulating type biomass gasification combustion device, it comprises upper suction type gasification furnace and heat boiler system, wherein also comprising with fuel gas supercharging device, the supercharging device comprises fuel gas in pairs set ejector, ejector heat boiler system for generation of steam and/or smoke as medium, the pair of suction type gasification furnace generating fuel gas by the injection, and forming high pressure/high speed gas jet is injected to the heat boiler system for burning. This new utility model meet of high temperature low oxygen heat accumulating type combustion method for combustion process requirement of flow field, and avoid of generating dust on heat storage body, to ensure the stable operation of the heat accumulating type combustion. This new utility model is full, success, and NOx generation amount small, process the gage small, small, smoke gas discharge amount small, its heat efficiency high, energy saving, environmental protection in the following high temperature low oxygen environment.
NOVELTY - Processing food waste involves crushing large amounts of wastes, pressing crushed wastes, sieving pressed waste, separating solid and liquid content from mixture, separating oil and water from mixture, carrying out magnetic separation of mixture, crushing separated materials, filtering crushed materials to remove organic and inorganic impurities, collecting organic particles, disinfecting collected particles, fermenting collected particles, and recycling collected biogas, biogas residue and biogas slurry produced during fermentation.    USE - The method is useful for processing food waste, preferably kitchen waste using the system (all claimed).    ADVANTAGE - The method is environmentally-friendly.    DETAILED DESCRIPTION - Processing food waste involves (a) crushing large amounts of wastes, (b) pressing the crushed wastes to remove organic and inorganic impurities, sieving the pressed waste, and adding organic matter to the sieved waste, (c) separating solid and liquid content from the mixture, and spraying hot water on the separated mixture, (d) separating oil, water and organic impurities from the mixture, (e) carrying out magnetic separation of the mixture, (f) crushing the separated materials, (g) filtering the crushed materials to remove organic and inorganic impurities, (h) collecting the organic particles, and disinfecting the collected particles, (i) fermenting the disinfected particles, and (j) recycling collected biogas, biogas residue and biogas slurry produced during fermentation. An INDEPENDENT CLAIM is included for system for processing food waste which comprises feeding port, crushing device, primary filter pressing unit, solid-liquid separation apparatus, oil-water separation apparatus, magnetic sorting device, deep crushing device, secondary extrusion filtering device, collecting apparatus, inoculating unit, and recycling unit.
NOVELTY - The method involves putting kitchen waste and garden waste into a storage pit according to proportion. The kitchen waste and garden waste are mixed to waste mixture that is delivered to a crusher. The waste mixture is delivered into a rotary kiln reaction furnace for washing the waste mixture. Tar and dust are removed during washing process. Pyrolysis pneumatic is separated by using a de-water separator and mixed with water stream. A heat source unit is fixed with a rotary reaction furnace pyrolysis device. The kitchen waste and garden waste are treated in pyrolysis process.    USE - Kitchen and garden pyrolysis waste solution processing method.    ADVANTAGE - The method enables increasing pyrolysis pneumatic quality, carbon quality and carbon yield and directly supplying heat into a rotary kiln so as to reduce usage of pyrolysis auxiliary energy and operation cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a kitchen and garden pyrolysis waste solution processing method.'(Drawing includes non-English language text)'
NOVELTY - The furnace has a feeding device fixed on bottom part of a furnace body and a dust-removing device. A driving system is connected with an inner side of an ash removing device that is provided with a tower-shaped fire grate. A top part of the furnace body is fixed on multiple heat pipes. The furnace body is sealed with the dust-removing device through liquid seal to form a gap. The tower-shaped fire grate is extended into an inner side of the furnace body. An inner side of the tower shaped fire grate is connected with an external fan. The feeding device is fixed on a feeding pipe.    USE - Tower type biomass gasification furnace.    ADVANTAGE - The furnace has high safety and working efficiency and quick crushing operation, and reduces tar flow to a combustion device through a pipeline and ensures quick slag feeding operation into de-dusting device.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a tower type biomass gasification furnace.
NOVELTY - A W-type molecular sieve is prepared by mixing potassium hydroxide (KOH), potassium feldspar, and water in reactor in which KOH containing water has concentration of 70-80 mass%, and mass ratio of KOH and potassium feldspar is 3:1, placing in 140-175 degrees C oil bath, refluxing while stirring for activation for 5-8 hours to obtain sub-molten salt, and adding aluminum hydroxide (Al(OH)3), silica (SiO2), and/or water in which molar ratio of SiO2 and alumina (Al2O3) is 5-20:1, molar ratio of potassium oxide (K2O) and SiO2 is 1-3, and molar ratio of water (H2O) and SiO2 is 40-120:1.    USE - Preparation of W-type molecular sieve for seawater potassium ion exchange adsorbent and slow-release potassium fertilizer.    ADVANTAGE - W-type molecular sieve is solid and has bar-shaped cluster, low energy consumption, low potassium feldspar activation temperature, and wide raw material source. Process is simple and has no waste liquid.    DETAILED DESCRIPTION - A W-type molecular sieve is prepared by mixing KOH, potassium feldspar, and water in reactor in which KOH containing water has concentration of 70-80 mass%, and mass ratio of KOH and potassium feldspar is 3:1, placing in 140-175 degrees C oil bath, refluxing while stirring for activation for 5-8 hours to obtain sub-molten salt, adding Al(OH)3, SiO2, and/or water in which molar ratio of SiO2 and Al2O3 is 5-20:1, molar ratio of K2O and SiO2 is 1-3, and molar ratio of H2O and SiO2 is 40-120:1, calculating required KOH using molar amount of K2O, aging at 25-70 degrees C for 2-15 hours, crystallizing at 90-180 degrees C for 8-72 hours, filtering, recycling crystallization mother liquor, washing filter cake, and drying.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram for preparing W-type molecular sieve. (Drawing includes non-English language text).
NOVELTY - A glucosamine segment-containing 1,3,4-oxadiazole derivative (I) is new.    USE - New glucosamine segment-containing 1,3,4-oxadiazole derivative is used for preparing composition (claimed).    ADVANTAGE - The glucosamine segment-containing 1,3,4-oxadiazole derivative is manufactured efficiently with high yield, by simple and safe method with reduced environmental pollution.    DETAILED DESCRIPTION - A glucosamine segment-containing 1,3,4-oxadiazole derivative of formula (I) is new.    R=CH3-, C4H9-, C6H5-, 4-CH3C6H4-, 3-CH3C6H4-, 2-CH3C6H4-, 4-CH3OC6H4-, 3,4-di-CH3OC6H4-, 3-CH 3OC6H4-, 4-FC6H4-, 2,3-di-FC6H4-, 4-ClC6H4-, 2-ClC6H4-, 4-BrC6H4-, 4-IC6H4-, 3-IC6H4-, 4-OHC6H4-, 4-NO2C6H4-, 3-NO2C6H4-, 3-C6H4N-, 2-C5H3S-, 5-Cl-2-C5H2S- or 4-(N,N-di-CH3)-C6H4-.    An INDEPENDENT CLAIM is included for manufacture of glucosamine segment-containing 1,3,4-oxadiazole derivative (I). N-(2-acetamido-3,4,6-tri-O-acetyl-2-deoxy- beta -D-pyranose)-N'-amidothiourea compound of formula (II) and p-toluenesulfonyl chloride are dissolved in tetrahydrofuran and organic base, reacted at 20-65 degrees C for 3-10 hours, and the reaction solution is evaporated under reduced pressure, to obtain N-(2-acetylamino-3,4,6-tri-O-acetyl-2-deoxy- beta -D-pyranose)-5-substituted-1,3,4-oxadiazol-2-amine of formula (III). The compound (III) and methanol are mixed in base solution, reacted at 0-25 degrees C for 0.5-4 hours, evaporated under reduced pressure, recrystallized using aqueous ethanol, to obtain glucosamine segment-containing 1,3,4-oxadiazole derivative (I) (N-(2-acetamido-2-deoxy- beta -D-pyranose)-5-substituted-1,3,4-oxadiazol-2-amine).
NOVELTY - The device has a fluidized section (1) whose lower part is connected with a filter section (8). A side wall of the fluidized section is connected with a spiral feeding device (7). A bottom part of the fluidized section is connected with a cloth air plate (3) and a constant-pressure wind room (2). The constant-pressure wind room is connected with the cloth air plate. A side wall of the constant-pressure wind room is connected with a gasification agent entrance (4). A combustion pneuma outlet (12) is connected with a side wall of the filter section.    USE - Biomass rich hydrogen gas catalyzing and gasifying device.    ADVANTAGE - The device maintains catalytic activity, solves biomass tar catalytic splitting process problem to allow catalyst to be quickly inactivated and increases gasification efficiency of biomass, biomass energy development and wide application prospect.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass rich hydrogen gas catalyzing and gasifying device.    Fluidized section (1)    Constant-pressure wind room (2)    Cloth air plate (3)    Gasification agent entrance (4)    Spiral feeding device (7)    Filter section (8)    Combustion pneuma outlet (12)
NOVELTY - The method involves placing rubbish raw materials to a heat accumulating type rotary bed pyrolyzing furnace. The rubbish raw materials are heated in the rotary bed pyrolyzing furnace that comprises a carbon discharging mechanism and a gas collecting pipe. High temperature pyrolysis gas in the rotary bed pyrolyzing furnace is discharged by using the gas collecting pipe. Pyrolytic carbon is placed to a fixed bed gasification device for performing gasification process by a rotary bed pyrolyzing furnace heating device that is connected with a heat accumulating type gas radiation pipe.    USE - Comprehensive pyrogenation gasification furnace domestic rubbish processing method.    ADVANTAGE - The method enables performing the pyrogenation gasification furnace domestic rubbish comprehensive processing process with low operation cost and better economic benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a comprehensive pyrogenation gasification furnace domestic rubbish processing system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a comprehensive pyrogenation gasification furnace domestic rubbish processing system.'(Drawing includes non-English language text)'
NOVELTY - This utility new type belonging to the biomass energy use field, claims a one for agricultural and forest biomass continuous pyrolysis charring device. The device comprising. add material, c, carbonizing device and a pyrolysis and carbonization device heating device is heating device, a pyrolysis device comprising pyrolysis furnace, pyrolysis furnace is through out of the pyrolysis tube and a pyrolysis tube inner is set with spiral conveyor, a solution pipe output end and a carbonizing device; the carbonization device comprising shell and a heat exchange tube, the heat exchange tube set in inner shell. The device using a two independent and controllable pyrolysis device and charring device of efficient rapid a biomass continuous, steady carbonization, obviously increase the conveying efficiency of use. The preparation of product distribute a product quality is controllable, energy use rate is high.
NOVELTY - This utility new type relates to a one integrated two step method of biomass and coal co-pyrolysis device, set with two through conveying pipeline, the coal and a biomass conveying to reactor in, a heating through a high power heating furnace and middle power heating furnace, so as to realize the biomass and coal pyrolysis alone, which avoids both the difference of a pyrolysis temperature a is caused by a bad effect, thermal pyrolysis of biomass and coal pyrolysis integrated in one of a reactor inner, pyrolysis of biomass pyrolysis and coal are set is the best reaction temperature, hydrogen a pneuma pyrolyzed under de-section biomass pyrolysis is a section coal supply of the hydrogen-rich atmosphere, which is good for liquid fuel increase. A through a one integrated reactor inner co-pyrolysis, a biomass pyrolysis tar and complementary of coal pyrolysis tar, reduces the oxygen content of biomass pyrolysis tar, improve the quality of co-pyrolysis oil. At the same time, operation is simple, it can process normal pressure operation, or pressurizing operation, which is good for enlarging a device scale.
NOVELTY - This utility new type provide a one continuous whole biomass pyrolysis furnace. The biomass continuous whole pyrolysis furnace comprising heat insulation shell and flue gas heating chamber, a pyrolysis chamber set with a smoke pneuma inner heating cavity, wherein it further set with pyrolysis pneuma tar splitting room inner smoke pneuma heating cavity and a semi coke calcining chamber, a pyrolysis chamber, a pyrolysis tar splitting pneuma and semi coke burning room are vertically the inner flue gas heating chamber, and passes through the spiral air channel, upper, lower end are extended out the flue gas heating chamber, set with material entrance in lower end of pyrolysis room, the upper end set with pyrolysis pneuma exit and semi coke exit, the upper end is a pyrolysis chamber pyrolysis pneuma outlet and pyrolysis pneuma tar splitting room of pyrolysis pneuma entrance connected, semi coke exit through semi coke entrance of transverse auger semi coke sintering room and connected. This utility new type the pyrolysis, tar splitting, semi coke sintering three a process section, increase the quality and conversion efficiency of carbon, pneuma inner in same one a gas supply chamber.
NOVELTY - A one liquid slag biomass pneuma for furnace, comprising a furnace body, a furnace body top to bottom in turn is divided into clear the furnace body, a furnace body gasification area and slag discharging area furnace body, a furnace body top part set with a clear synthesis pneuma exit, the furnace body side wall set with clear biomass feed port, a gasification furnace body side wall set with a gasification agent entrance, a furnace slag discharging area side wall set with an external heat source interface, a furnace slag discharging area at the bottom set with liquid slag outlet, said liquid slag exit is set with a porous bottom plate, said liquid slag exit side wall outside is connected with a high temperature spray gun, the liquid slag outlet lower part set with a chilling room, chilling room side wall outside the water inlet pipe is connected with the bottom of the chilling room form slag pool below the slag water pool set with slag. This utility new type solves the pneuma in a furnace slag discharging difficulty, gas releasing leakage, a, a biomass fuel of high temperature gasification and smoothly discharging the bottom of the furnace body.
NOVELTY - This utility new type claims a one for preventing biomass fixed bed gasification furnace a regulating structure, comprising an annular pipe, the annular pipe is set with a multi-separating plate, the annular pipe uniform separating plate is not connected is semi arc, each a semi arc are arranged one the connected air inlet pipe and annular branch tube of two root into biomass fixed bed gasification furnace in a semi arc area, air inlet pipe mounted with a regulating valve, the upper two of the branch pipe between the annular furnace wall is mounted with one of a thermoelectric couple. After temperature through the annular separating pipe is a multi-semi arc area, and each in a semi arc arranged air inlet tube, an annular branch tube and a thermocouple, the thermocouple measurement through a semi arc area of each air inlet pipe of air inlet amount adjusting, each a semi arc area is a holding temperature is basically the same, a gasification medium is in a uniform distribute inner furnace, after further detecting temperature of thermoelectric couple through feedback regulating a control valve adjusting a semi arc of each air inlet quantity, realize automatic control.
NOVELTY - This utility new type claims a gasification furnace of one three-level feeding system, the feeding system comprising one level , a material clock a three-level level , the first-stage and below end of second level clock are set with material discharge wherein, lower end of the material wherein is set with fan-shaped air door, a fan air door baffle plate, comprising fixing connected pole and rotating shaft, rotating electric machine the rotating shaft of one end connect in outside of a housing, a rotating shaft the other end through fixing connecting rod is welded in a blocking plate, the material of the lower part set with anticlockwise limiting pin, wherein said upper rotating shaft is set with a convex structure, the convex block structure of side is set with clockwise limiting block fixed connecting a rotating electric machine a, the utility model is new type using three-level feeding, which ensures the time in feeding material clock always has one channel seal in seal state, which solves the problem of gas, is at the same time to reduce friction between the fan air door and to prevent the fan air door of abrasion, increase the use life of device, the biomass gasification furnace feeding operation more smoothly.
NOVELTY - This utility new type outside one relates to a biomass gasification furnace is ash disk ash discharging system, wherein the ash outlet system including a water component, component and pedestal component ash disc, the ash disc component set with a water component and pedestal component set between the water set component comprising set inner wall water jacket interlayer and outside wall water jacket, a water interlayer is set in water set outside wall set a water inner wall set between the water set in the interlayer set with cooling water. This utility new type is following advantages, 1) structure design, disassembling and assembling maintenance change is convenient, the cost is low, 2) the ash discharging system external to save a airlock, twisting in the existing device, through using machinery structure, the reliability is greatly increase, easy operation, and prolongs the use life of gasification furnace. Because it reduces a component, and the cost is reduced greatly.
NOVELTY - This new type utility claims one biomass gasification furnace is a rotary location device, the biomass gasification furnace comprising reaction area,, air inlet pipe and pedestal, the rotating device including a sliding groove structure, a slide rail structure and a roller, the slide rail structure set in the bottom, the groove structure is set with the upper part of a pedestal, the ash tray through sliding groove and sliding rail structure activity connection pedestal and a reaction area, the ash pan is the circumference of the bottom surface of a circumferential side set with a multi-location idler wheel, inner side of the location roller set with a rolling ring is fixed in a pedestal up. This utility new type inner outside two set using a device to a rotating work of biomass gasification furnace, biomass gasification furnace upper ash tray is convenient to flexibly adjust and accurate location of the rotary location device is integrated a steady, use life is long, the normal cleaning and feeding work gasification furnace reaction area of furnace body;
NOVELTY - This utility new type provide a one biological granule drying device, comprising burning room, drying room and exhaust gas treatment device, the combustion room is opened with a air entrance, the inner combustion room is set with heat exchanger, said heat exchanger through air supply main pipeline and the drying room connect, the drying room and the heat exchanger and through a return pipeline, said return pipeline set with a fan, a gas and a heat exchanger in circulation in the drying room, the air supply main pipeline passes through the drying chamber, the inner drying room is further set with multi-air supply of a pipeline, multi-pieces of the air a pipeline are connected and the air supply main pipeline, the air supply pipeline and a connection at the air supply main pipeline is set with an adjusting valve, the upper air pipeline are set with a multi-a wind adjusting plate, a waste gas treatment device and the combustion room through dust removing pipeline connection. This utility new type provide a biological granule drying device, it can release energy pressure, reducing crop stem leaves combustion produce is pollution.
NOVELTY - Gaseous space This utility new type claims a one biological diesel oil purifying system, comprising fatty acid methyl ester storage jar (12), the first condensing device (21), a second condensing device (31), the first temporary storage tank (24), second jar (33), biological diesel oil methyl ester in storage jar (12) form heating gaseous mixture from fatty acid methyl ester storage jar (12) is gaseous space entering into the first condensing device (21) is gas space and a first isolate liquid is condensed, the first isolate a liquid from the liquid space of the first condensing device entering into the first temporary storage jar of liquid space, separating the first separating object of gaseous mixture from the first condensing device a gaseous space entering into second condensation device is condensed and a liquid second isolate a second condensing device, liquid second isolate from the liquid space of second condensing device entering into second storage jar of liquid space. This utility new type only needs one secondary heating and purifying a different carbon atom number ester of two level or more, the complex of the existing technology and distilling process, reduces the complexity of purifying system.
NOVELTY - This utility new type is a one simple structure, increase stir device in a marsh gas pool, breaking shell of water surface in biogas pneuma pool, a slag with a stir device of automatic discharging marsh gas pool. A technology method according to is the one with a stir device of automatic discharging marsh gas pool, comprising biogas pool main body, marsh gas pool cover, a material inlet and outlet wherein, the key point is that: a vertical to a cover set with air pipe in the marsh gas pool, the lower end of this pipe extends into the gas in the marsh gas pool main body, set with a stir shaft in through out of this gas in tube, under the stir shaft end rotating connection in the marsh gas pool main body, upper end connecting power input device, further connecting with a stir leaves mechanism in lower end part of this stir shaft; the stir leaves mechanism by at least one stir blade and a pole piece compose, centre line of said stir blade and a stir shaft parallel to each other and stir blade connecting pole through a lower end part of a stir shaft.
NOVELTY - This utility new type relates to a built-in feeding pipe of one new slag removing machine for methane fermentation jar, comprising a marsh gas fermentation jar 1, a feeding pipe 2, a discharge pipe 3, the outer colour steel plate 4, insulating layer 5, (6), bracket (7) and the pneuma hole 8. A b with that of external feeding in existing marsh gas engineering pipe insulating wastes time and labour, waste cost, easy to block, , affect beautiful appearance, convenient construction and so on. This biogas fermentation jar is the feeding pipe of the small letter type from the bottom of fermentation a jar inner jar directly obliquely inserted to jar, jar and the top is welded with bracket and fixed. This utility new type has time construction time and labour force, saves the cost, convenience and practicability, beautiful appearance and so on.
NOVELTY - This utility new type claims a one household biomass energy furnace, comprising observing, observing under set with feeding port, the biomass fuel through add material entering into the hearth, wherein the hearth outside set with a water jacket, the lower part close to the water jacket mounted with a secondary air door and wind shield plate, lower water set set with a water inlet, the water inlet is one downward secondary air channel, one air channel entrance with a wind plate, a furnace upper part is the first most boiler, the first peripheral is second cooker boiler, boiler ring first and second lower part is boiler, fire blocking ring side set with smoke pneuma outlet, the lower part fire blocking ring set with the water wherein, pneuma outlet through air pipe entering into a combustion furnace, a combustion furnace bottom is most second catalyst, the second catalyst periphery part is the first catalyst, the first catalyst periphery part is a secondary air channel, this most lower part is furnace tank, set with a ventilation hole above a hearth, increase oxygen combustion. This utility new type has simple structure, good property of it is fit to popularize application.
NOVELTY - Fish feed a flat machine. Flat moulding grain machine processing biomass granule is solidified molding technology is a one, In recent year in the development process of biomass granulating industry in the flat mould machine to the firm and durable, strong raw material adaptability and so on gradually obtain favour of producer, the current of a machine feeding room, a formation rate is low, use complex, working cost is high, a pressure roller pressed film slipping. This utility new type is compose comprising: transmission tank (2), a transmission tank is above the motor (1), a transmission tank of a main shaft (3), a main shaft of a wheel (5), pressing wheel in the feeding room (4), the feeding room are provided with material plate (6), the press wheel and the lower part of the material plate are both with flat-die (7), the flat die is provided with a cutter (8), the cutting knife is provided with material sweeping plate (9), the sweeping plate material wherein a (10). This utility new type fish feed for processing.
NOVELTY - A kind of one compound particle and preparation system, can make material prepared into compound granule. The compound particle and preparing system comprises reaction tank and drive device. Reaction tank for one section is round and cylindrical shell, reaction tank can rotate, the inner wall of the reaction tank palisade fixing sheet is provided with multiple interval is set with the individual, each individual palisade from one end reaction tank and extending to the other end, each strip part and axis of the reaction tank is set with inclined, and each strip part and axis of the reaction box is included angle between same, driving device is set outside the reaction tank, and reaction tank and connected with the driving device and driving reaction tank can rotate, to make the whole multi-palisade reaction tank with rotation then form one wind power for driving in material enter into reaction tank or driving compound particle from reaction tank and output. The compound grain in the system not only has simple structure, and can make the material heated in reaction tank is more uniform.
NOVELTY - This new utility model claims of one indoor zero discharge of cultivation methane series combustible gas collecting system, comprising marsh gas pool (1), cultivation greenhouse (2), methane gas storage space (3), a methane gas collection device (4), a methane gas transporting pipe (5), a flame-retardant layer (8), ventilating air inlet window (9), a methane pool water sealing groove (10), a methane series this utility model with new design and unique structure, collecting ruminant cultivation industry (for bovine cultivation main) discharge of combustible gas, and storage in marsh gas pool and matched, can effective reducing carbon discharge of livestock breeding, for farmers provide sufficient green clean fuel, relieving burden of farmer, increase farmer income. Designing the production manufacturing cost low, suitable for installation in the large-scale cultivation area, in any ruminant animal and is suitable for large scale cultivation.
NOVELTY - A one based on in-situ marsh gas purifying reactor a bioelectrochemical principle, belonging to the field of environmental protection and a renewable energy use field, reactor comprising reaction pool, reference electrode, biological cathode, an anode room and chemical anode, wherein reference fixing is immersed in a liquid in a reaction pool in the side of the opening of the reaction pool and the lower part, biological cathode and anode room is located in reaction pool, anode in the anode room, reaction pool at the same time as the cathode room and anaerobic digestion pool, constant potential rectifier through a biological cathode potential, rear biological cathode start period is finished, the surface forming at the same time producing biogas and biogas pneuma and purifying function of biological film, continuous operation time adjusting organic load and the cathode potential to a synchronous anaerobic biogas and biogas purifying in situ the best property, the utility model is new type biological method and the in situ method a two idea at the same time to a biogas purifying process in not only realize the increment and a carbon emission reduction, but also simplify the biogas purifying system.
NOVELTY - Outside inner inner one a straw gasification furnace, comprising furnace body (1), a furnace body (1) of lower part with a combustion room (2) and the ash room (3), ash room (3) is provided with a scraper ash. (4), a combustion chamber (2) of inner furnace wall is equipped with a blowing device (5), an ignition device (12), a lower transmission device (6), a furnace body (1) top part is provided with a charging cabin (7), a container (7) is provided with a feeding device (8), a furnace body (1) of upper part is equipped with a gas transmission device (9), a furnace body (1) is provided with a gas purification device (10), pipeline of upper, lower gas. (6), (9) and gas purification device (10), the gas purification device (10) of the top part is provided with an air outlet device (11), an air outlet device (11) is a rubber tube and cooker. The advantage is: fully use waste plant pole,, saving energy, protection environment.
NOVELTY - This utility new type claims a heating gas of a suction type biomass gasification furnace, comprising outside tube, middle tube, inner tube, tube form the gas channel, a gasification produce a gas through the lower part of gas channel flow to gas outlet, middle tube is provided with a transfer piece, gas outlet in lower part of outside tube, the temperature under side of middle tube is higher a the time of gas is continuously heating, holding the gas of high temperature, a tar in gas is always exist to gas way, solves the problem that the tar separating s. Although the material layer would reduce the initial temperature of gas, but the gas of low temperature can be heating to high temperature is intermediate tube lower part of a gasification furnace can be a material layer is thickened, for gasification of gas to produce a better filter to reduce dust of produce. This gasification furnace to make produce a gas maintain a relatively high temperature at the same time of reduce the produce of dust, which can solve a current sucking type biomass gasification furnace the exist of corresponding.
NOVELTY - This utility model new supply of one of marsh gas treatment system, comprising the wet desulphurization tower, decarburization tower, drying device, an inclined plate sediment pool, gas outlet of the wet desulphurization tower and gas entrance phase of part under the decarburization tower connected, gas outlet of the decarburization tower upper part and gas entrance of the drying device connected mutually, upper part of the removing tower is provided with calcium hydroxide solution import, liquid outlet and the inclined plate part is under the decarburization tower sediment pool and liquid entrance mutually connected. And the existing technology, this utility new type by wet desulphurization tower with sulphur, decarburization tower to obtain calcium carbon and biological natural gas, implementation of sulphur, biology natural gas, and recycling the third valuable resource of calcium carbon, to have maximum resource using marsh gas, at the same time, use calcium hydroxide solution as absorb liquid and decarburization tower, absorb liquid and needs no steam or electric heating regeneration, reducing of production cost, to obtain the calcium can carbon paper itself is used for production and realization of comprehensive use of resource.
NOVELTY - This new utility model claims of one pig site with a kind of marsh gas generating device, pig site for marsh gas generating device mainly comprises marsh gas fermentation tank, organic fertile rotten ferment pool, set heat pipe, heating coil, material pipe, gas pipe and air storage tank, the marsh gas fermentation tank is sunk semi buried structure, wherein is set with organic fertile rotten ferment pool, marsh gas fermentation tank through material pipe and fertile decomposed fermented organic connection pool, marsh gas fermentation tank inner wall set with heating coil, inner heating plate pipe and organic fertile decomposed fermentation pool is set heat tube connection, a marsh gas fermentation tank by gas pipe and air storage tank connected, under this utility new type cultivating environment in intensive pig for marsh gas production and has mechanism fertile phase combination, use with mechanism process in production of fertile heat overcomes the marsh gas fermentation device for production of insufficient problem, realize efficient stable production of marsh gas, to efficient use of energy.
NOVELTY - This new type utility claims one internal cyclone dust collector of a biomass gasification furnace, wherein comprising cyclone dust collector, nozzle, rotary furnace wall and furnace body, lower part of the furnace body is set with rotating furnace wall, rotating furnace wall is provided with an air inlet, furnace body of upper part is set with a storage hopper of add material device, a cyclone dust remover is set on the inner furnace body, a cyclone dust collector is set with a air outlet connected to furnace body, a cyclone dust collector with a tangent air inlet set below the tangent air inlet set with a nozzle, the lower part of cyclone dust collector by a pipe connecting to water. This utility new type the first time dust removing and collecting and it is convenient to process, it can prevent air blockage, ensure long-term stable of gasification furnace operation.
NOVELTY - This utility new type claims a piggery marsh gas waste liquid one farmland irrigating system, the system mainly comprising a fermentation tank, chlorella culture tank, a liquid discharging pipeline, a water pipeline, water pump, farmland, a filter screen, a filter minutissima; the bottom of fermentation tank through liquid outlet pipeline and water pump and chlorella culture tank is connected, chlorella culture tank corresponding to the liquid discharging pipeline is set with a filter screen, chlorella culture tank through water transmission pipeline and water pump and farmland, chlorella culture tank corresponding to water pipeline is set with a filter minutissima, this utility new type use biological technology for chlorella liquid taking methane waste water purification treatment of the marsh gas waste liquid purification a a irrigation water and reduce carbon emission at the same time also a chlorella harvesting and creates the economic benefit, this system process is simple, the cost is low, valid methane waste liquid pollute the environment to solve a problem.
NOVELTY - Medical, life garbage gasification combustion furnace, belonging to the garbage treatment field, relating to a garbage gasification of one combustion furnace. This utility new type comprising combustion chamber, one chamber pneuma, and feeding and discharging bin, a combustion chamber and pneuma chemical chamber are a horizontal tank, pneuma for chamber combustion chamber, combustion chamber and substantially coaxial, slightly downward inclined pneuma in chamber, a combustion chamber relative rolling. Feeding material from entering into pneuma chemical chamber, gas in combustion chamber in combustion, a rear gas by gasification of biomass material in a chemical chamber heating pneuma, pneuma one chamber from the air outlet tube of a discharging bin, a discharging cabin. This utility new type because of using rotating in a gasification chamber, the pneuma in chamber of uniform material heating and gasification. And pneuma cabin by using normal pressure design, which ensures working safety. This utility new type is suitable for the medical and household garbage raw material of primary treatment.
NOVELTY - This utility new type relates to a household garbage one recovery processing system, comprising garbage collecting tank, a garbage collecting tank through a conveying belt conveying the rubbish to crusher process crushing, inner of rear crushed garbage conveying to solar energy generator inner and inner use the solar light to the solar energy generator taking the heating of a garbage gasification, gasification produce a rear inner gas pipeline entering into dry distillation furnace through a distillation, rear a rear dry distillation gas bag-type dust remover through dust removing by a cooling spray tower, a gas cooling rear by rear gas collecting tank entering into active carbon filter filter delivery to a combustion gas collecting tank. This utility new type design is reasonable, use is convenient, through this a treatment system, the solar energy generator to decompose the gasification household organic garbage, which not only fully valid use of domestic garbage, but also can use the household garbage produce a combustion gas, which avoids the waste of resource, increase the valid use rate of resource, at the same time protection environment.
NOVELTY - This utility new type relates to one a hydrogen-oxygen mix gas happen device, the comprising: containing electrolyte of electrolytic groove, mounted in the inner electrolytic groove, arrangement intervals, and electric source and is connected with the electrolyte for electrolytic process to produce hydrogen oxygen mix gas of a plate, wherein the said electrolysis groove is further mounted with electrolytic groove and inner connected a circulation pipeline, in this circulation pipeline set with for flow of electrolyte in circulation pipeline pressure of pressurizing part; the electrolytic groove of inner part set with multiple isolating a arrangement, and the connected end of the water circulation pipeline of, the electrode plate for a jet of spraying mouth. This utility new type the hydrogen-oxygen mixed gas happen device, not with a pneuma eliminate bubbles and for a plate to impact, so that it can prevent a plate, can be a plate produce over-current and over-voltage prevention to prevent decomposition of electrolyte has low efficiency, as a plate electrode of electrolyte injection area is increased, which can increase the removing efficiency of pneuma.
NOVELTY - Field of technology. The utility new type relates to solid waste treatment of, especially relates to a one and emission reduction environment-friendly solid waste gasification device, this utility new type environment-friendly emission reduction of solid waste gasification device processing solid waste is more complete, and reinforcing and emission reduction environment-friendly solid waste gasification device of recycling use; comprising lifting hopper, a gasification furnace, water cooler, a water filter and a drying dehumidifier; gasification furnace set with a feed inlet and a discharge wherein the inner gasification furnace set with a working cavity, a feed and discharge wherein and working cavity are set with a carbon layer and a inner working cavity, lifting hopper mounted at a feeding port, wherein a discharging water cooler and gasification furnace, water filter and water cooler, drying dehumidifier and water filter.
NOVELTY - A biological fuel granule machine one seal room, including seal room, the seal room upper part of outside edge set with a groove, a groove and a discharge, wherein the seal room lower part outside of side is welded with a vertical reinforcing plate, the reinforcing plate of a seal between room set with a waste hole, this utility new type because of the action of vertical reinforcing plate, the bearing is obviously better than that of the current seal room, and the groove and discharging wherein a valid seal, a seal effect is better, and the discharging is more smooth, and does not affect normal operation of a device, the design the waste hole a waste is collected, it will not produce smoke dust diffuse a condition, a valid to ensure the safety of operation staff, so this utility new type is better than that of the current technology in a safety and production efficiency.
NOVELTY - Wood tar extracting tank door ignition port, one is used for a kind of plant and extraction from plant insecticidal pesticide main component wood plant acid and production period, mother liquid wood tar extracting box door and ignition port. Use metal square barrel is made of outside diameter longer 0.2 meter wide 0.12 meter square of ignition port, with hinge can movably ignition port cover for chain, wherein edge plane of ignition groove put sealing material sealing, closing the ignition port cover and buckle when an ignition mouth square shape body is normal.
NOVELTY - Wood tar extracting tank, one is used for the plant in a plant insecticidal pesticide main component extract pyroligneous liquor plant acid prior product mother liquid of wood tar extracting box body, 3 long, explosion, explosion-proof wherein high is 2.5 long, 2.5 wide metal body and a top of a front pressure of inner diameter 0.6 of the circular explosion-proof, inner diameter 0.25 in the top part of rear smoke pneuma discharge port, a middle of a movable metal interlayer door body is a pressure of inner diameter 0.6 a of the left and right two is a inner diameter 0.1 of the lower part of the circular viewing port, door body left and right two is a 0.22 long 0.12 wide rectangular ignition wherein a, inner wall body is red into the heat preservation wall tile, the bottom is a air heat insulation hollow brick, a trapezoidal metal steel top and metal keel of top part compose the mix of earth ramming insulating structure.
NOVELTY - This utility new type relates to a one use solar energy processing organic garbage gasification system, comprising solar energy generator, solar energy generator through a pipeline and air pump and organic waste collection tank, an air pump of the solar energy generator inner produce a gas pipeline through a dust remover, a gas input gas collecting tank rear by dust, a gas inner gas collecting tank and filter rear to combustible gas collecting tank by filter. This utility new type design is reasonable, use is convenient, through this a treatment system, fully use the solar energy, the solar energy generator to decompose the gasification household organic garbage, which not only fully valid use of domestic garbage, but also can use the household garbage produce a combustion gas, which can be used for generation or as energy, avoids the waste of resource, increase the valid use rate of resource, at the same time protect the ecological environment.
NOVELTY - This new type utility claims biology natural gas preparation device, this device comprising a first screw compressor in turn through pipeline, the first purification tank, the gas buffer tank and the first film module system, high pressure outlet a product gas conveying pipeline of the first film component system, low pressure outlet through pipeline in turn a second screw compressor, second purification tank and the second film module system, second film module system high pressure outlet of a gas buffer tank, a low pressure outlet is connected with waste pneuma discharge pipeline. This method comprising: the original gas by the first screw compressor rear pressurizing entering into the first purification tank and the first film module system, high pressure product pneuma orderly entering into second purification tank and a second film component a rear by product gas conveying pipeline a, low pressure gas entering into second screw compressor, concentrate pneuma reflux entering into gas buffering tank, the rest waste gas discharging. This utility new type using two level a and two level film separating, reducing compressor power at the same time in the film a, processing cost is low.
NOVELTY - This utility new type relates to one used for a large-middle biogas engineering in stir raw material tank, a tank main body is located underground, the top is higher than the ground, top tank set with material entrance and biogas slurry refluxing liquid entrance, liquid entrance return conveying pipeline and into a tank body, conveying pipeline outlet direction a conveying pipeline to the outlet of tank body corresponding to cross a center of a circle of a center of a circle, tangent to a circle conveying pipeline of a radius of, the bottom of the tank body set with heating coil, a heating disk pipe set with heat source inlet and outlet, the side of the bottom of the tank body is also set with slurry outlet. The stir tank through using fermentation tank inner fluid of reflux liquid to the tangent direction entering into the tank body, use a fluid force for a raw material, stir the mixture material to the using of energy consumption. A heating device for a material inner bottom of the tank body of the tank body heating process, temperature of inner to the slurry entering into the fermentation tank temperature has been reached, the needed fermentation of the fermentation tank for heating inner step of homogenizing, which is good for a fermentation process.
NOVELTY - This utility new type provide a one methane, wind energy and solar energy integrated ecological circulation system, mainly by wind energy and photovoltaic composite electric power happen unit and storage unit, a marsh gas happen unit, marsh gas and solar thermal composite use unit, heating device, air circulation exchange unit for sunlight greenhouse and compose, the wind energy and solar energy composite power happen unit output electric energy and conveying to biogas heating device and storage unit, a biogas heating device for marsh gas happen a heating unit, in livestock sunshine warming shed is built toilet and animal and vegetable garden house, marsh gas happen of produce in a unit for conveying to the vegetable or plantations grass. This utility new type fully use low temperature, wind of high cold area can and solar energy and human and animal excreta produced marsh gas clean energy, increase area herdsman life quality, valid and protect the grassland area, reduces air pollution, a green clean energy source of sustainable use.
NOVELTY - Sludge is treated by storing sludge having moisture content of 80% into sludge storage tank, anaerobically fermenting, stabilizing through microorganism metabolic activity under anaerobic condition, obtaining methane and carbon dioxide (CO2), sterilizing sludge, adding number 4 additive, dewatering, pretreating, chemical conditioning for 3-6 minutes, adding number 2 additive to kill germ and virus, passivating with heavy metal to destruct colloidal structure of sludge, stirring, concentrating, and mechanically dewatering sludge having moisture content of 50-60%.    USE - Treatment of sludge for manufacture of fermented soil nutrient, production of fuel, and manufacture of environment-friendly brick and ceramic materials (all claimed).    ADVANTAGE - Process removes heavy metal and generates harmless substance, and product improves crop production and soil.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) production of fuel which involves drying dewatered sludge; and    (2) manufacture of environment-friendly brick and ceramic materials which involve adding fly ash into dried and dewatered sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram for treatment of sludge. (Drawing includes non-English language text).
NOVELTY - The method involves pressing biomass material into a block through a compressor. Temperature of a combustible gas combustion section is about 1100 to 1200 degree Celsius. Instant drying process is performed. A preheating biomass gasification section is obtained. Temperature of a biomass gasification section is 900 to 1000 degree Celsius. Combustion gas is entered into the combustible gas combustion section. A heat heating working medium of a fuel gas combustion section is obtained. The working medium is connected to an electricity generating device.    USE - Biomass gasification generating method.    ADVANTAGE - The method enables increasing biomass combustion heat utilization rate, reducing environment pollution and ensuring considerable economic benefit and better application prospect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a step type steam generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a step type steam generator.
NOVELTY - The machine has a fuel cabin whose top part is connected with a pressing material system. A lower port of the fuel cabin is fixed with a convection chimney that is connected with a vacuum butterfly valve. An inner wall of the fuel cabin is connected with an inner insulating layer. A middle part of the fuel cabin is fixed with an inner cooling cabin. A combustion chamber is fixed around a tower soaking oxygen distribution disk. A middle part of a mixed gas chamber is formed with a drain hole. Two sides of the drain hole are matched with a tar discharging hole.    USE - Multi-point catalytic biomass gasification machine.    ADVANTAGE - The machine uniformly conveys oxygen in the fuel cabin, accelerates air outlet speed by multi-point catalyst, improves yielding performance, increases settling speed of tar and dust and gas purity, saves biomass fuel consumption and satisfies large gasification machine requirements by realizing rapid cooling process.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a multi-point catalytic biomass gasification machine in partial section.
NOVELTY - The device has a cyclone pyrolysis chamber (1) connected with a suspension combustion chamber (3) that is arranged with a port. A lower end of the suspension combustion chamber is fixedly connected with a switching fire grate (4). A lower part of the switching fire grate is connected with a vane (8). An air ring is fixedly connected with a lower part of an ash bucket (5). The fire grate and the air ring are arranged with an ignition hole set (9). The lower part of the suspension combustion chamber is inserted in an ignition fuel add material pipe (7).    USE - Biomass cyclone pyrolysiscombustion composite gasification device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass cyclone pyrolysiscombustion composite gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass cyclone pyrolysiscombustion composite gasification device.    Cyclone pyrolysis chamber (1)    Suspension combustion chamber (3)    Switching fire grate (4)    Ash bucket (5)    Ignition fuel add material pipe (7)    Vane (8)    Ignition hole set (9)
NOVELTY - This new utility model is one of chain fire grate moving bed mixing suction type biomass gasification furnace, comprising gasification furnace cement base, a scraper slag remover, remove ash machine motor, remove ash trolley, air chamber furnace bottom, furnace bottom air distribution room, air in furnace chain type dust remove system, chick remove coke device, lower furnace reaction chamber, repair workbench, gasification furnace main body reaction chamber, furnace top high temperature chamber, gravity automatic choke automatic explosion door, a gas pipe, a feeding and lower hopper. This new utility model is can regeneration of biomass, for domestic garbage by using the gasification furnace transformation for new energy " biomass gas, treatment of municipal domestic garbage, the domestic garbage for conversion as can combustion of biomass gas, will seriously pollute domestic garbage of life quality change into clean energy in furnace in, to change waste as treasure of target, which completely solves of municipal domestic garbage and industrial production using traditional energy discharge to atomphere and to cause environmental pollute the environmental protection problem, the applied range is wide, green environmental protection.
NOVELTY - This utility new type relates to a one fertilizer production device, specifically is a biological carbon production with one plant stalk straw carbonization furnace. Comprising heating furnace, set in a coking heating furnace inner hearth, through gas pipe in series in a carbonization chamber of tar collecting chamber and gas cleaning chamber, a heating furnace inner hearth is further set with a fire grate, a fire grate set in the lower part of the carbonizing room, set up with a door in a wall between furnace grate carbonization room and a coal feeding port, a slag outlet door set with a lower with a in a furnace wall below the fire grate, a carbonization chamber a two end tubular structure, carbonizing room and furnace wall of heating furnace of a fixed, carbonizing room of outside wall set with heat absorbing fin, carbonizing room of inner cavity in coaxial mounting with a packing auger, a carbonization room of upper end connected feeding pipe, lower end of carbonization room connected discharging pipe, the feeding pipe and the discharging pipe are set with closed valve. This plant stalk straw carbonization furnace coal to a heat source, the structure is simple, the heat efficiency is high, the energy consumption is low, tar and coal carbonization process and produce a by-product in a collecting a use.
NOVELTY - The device has an absorbing pool connected with a sedimentation pool. A grid machine is arranged with a biological filter pool through a water pump. The biological filter pool is provided with a sludge part that is connected with a reverse flushing device. The reverse flushing is arranged with an aeration disk. A porous plate is fixed with gravel filler. The biological filter pool is connected with a nitrogen absorbing pool. The nitrogen absorbing pool is connected with a sludge phosphorus absorbing pool and provided with a medicine adding device.    USE - N and P-type bar sewage device.    ADVANTAGE - The device reduces nutrition substance content and absorbent time, improves resource availability, water body transparency and recycling and cleaning efficiency, irrigation and flushing effect and realizes saturation adsorption, rolling and crushing process and phosphate fertilizer material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an N and P-type bar sewage method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of an N and P-type bar sewage device.
NOVELTY - Gas-phase methanol esterification reactor comprises a reaction kettle (1) and a circulation pump. The top of the reaction kettle is provided with a raw material lipid feeding inlet (2), an acidic catalyst feeding inlet (4) and an air outlet (3). The bottom of the reaction kettle is set with a lipid outlet (8) and a lipid inlet (11). The lipid outlet is connected to an inlet of circulation pump through a first pipeline. An outlet of the circulation pump is connected to the lipid inlet through a second pipeline. The first pipeline or second pipeline is connected with gas-phase methanol pipeline.    USE - Used as a gas-phase methanol esterification reactor.    ADVANTAGE - The methanol esterification reactor: has low reaction pressure, quick reaction speed and high production efficiency; and saves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the gas-phase methanol esterification reactor.    Reaction kettle (1)    Raw material lipid feeding inlet (2)    Air outlet (3)    Acidic catalyst feeding inlet (4)    Lipid outlet (8)
NOVELTY - This utility new type claims a from one type environment-friendly gasification heating furnace, comprising burning room, the heat exchange room and the gasification room, combustion chamber is horizontally arranged, a gasification room and heat exchange chamber are vertically arranged in the combustion room above form gasification type combustion of U type body structure, the inner top plate of the combustion room close to the first channel position downward position of a room with a turbulent flow baffle plate, a combustion room of the bottom corresponding to the gasification room and heat set with a dreg collecting pit, inner combustion room is provided with air supply, the heat exchange room of the top part set with a the U-type structure in the furnace body smoke pipeline of forming negative pressure, a gasification chamber is provided with gasification agent supply port, air supply port, a smoke pipeline and valve operation condition set with a common used for regulating a U type body structure of a gasification agent supply opening. This utility new type of self-type environment-friendly gasification heating furnace has simple structure, convenient operation, high combustion efficiency, little pollution to the environment and reduce the investment cost and operation cost.
NOVELTY - This utility new type claims a smokeless gasification section one combustion hot-blast furnace, comprising burning room, the heat exchange room and the gasification room, combustion chamber is horizontally arranged, the bottom of gasification room and heat exchange chamber are vertically arranged in the combustion room above form gasification type combustion of U type body structure, a gasification room and the bottom of the heat exchange room are a first channel and the second channel and the combustion room is connected with the inner top plate of the combustion room close to the first channel position downward position of a room with a turbulent flow baffle plate, a combustion room of the bottom corresponding to the gasification room and heat set with a dreg collecting pit, inner room close to the first channel position is provided with one secondary air supply, heat exchange chamber near the combustion room position is provided with a secondary rotational flow air supply port, the top part of the gasification room set with fuel inlet, gasification room inner bottom set with fire grate, gasification chamber is provided with adjacent grate of gasification agent supply opening. This utility new type smokeless gasification section of combustion hot-blast furnace has simple structure, convenient operation, high combustion efficiency, little pollution to the environment and reduce the investment cost and operation cost.
NOVELTY - The cabinet has a cabinet body whose upper part is connected with an air outlet tube. A bottom part of the cabinet body is connected with a water inlet tube. A labyrinth water washing room is connected with the air outlet tube. An air inlet tube is connected with a lower part of the cabinet body, where the air inlet tube is pyramidal shaped. A side plate is connected with a baffle plate. A pneuma hole is formed on a side wall of the cabinet body. Clapboard is fixed in the cabinet body. The labyrinth water washing room is arranged with a side part of the clapboard.    USE - Biomass pneuma purification cabinet.    ADVANTAGE - The device improves labyrinth water washing efficiency and removal rate of quantitative biomass pneuma.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional view of a biomass pneuma purification cabinet.
NOVELTY - Method for treatment of spray dryer exhaust gas involves drying liquid in spray dryer to produce dried substance and exhaust gas, passing at least some of spray dryer exhaust gas through heat exchanger to produce a cooled spray dryer exhaust gas, passing at least some of cooled spray dryer exhaust gas through condenser to produce dried spray dryer exhaust gas, passing at least some of the dried spray dryer exhaust gas through the heat exchanger to produce warmed spray dryer exhaust gas, and returning at least some of warmed spray dryer exhaust gas to the spray dryer.    USE - The method is useful for treatment of spray dryer exhaust gas (claimed).    ADVANTAGE - The method enables to treat spray dryer exhaust gas with reduced energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for spray dryer exhaust gas treatment system.
NOVELTY - Invention relates to bio-energy and can be used as a universal digestion tank for processing of manure of animals, poultry, domestic and agricultural waste into methane and organic fertiliser. The reactor of anaerobic digestion of biomass comprises a housing 1 in the form of a sealed container, comprising four sections: preparatory (acidic) 2, neutral 3, alkali 4 and of methane digestion 5, separated by vertical partitions 6, 7, 8. The reactor is additionally equipped with a diaphragm electrolytic cell 12, one output 18 of which with the analyte solution is connected to the acid fermentation section 2, and its other output 21 with the catholyte solution is connected to the sections of neutral 3 and alkaline fermentation 4. In the reactor housing 1 along its length the additional fixing units 11 of vertical partitions 6, 7, 8 are made, made with the ability of replacement with the change in the volumes of sections of fermentation.    USE - Agriculture.    ADVANTAGE - Invention enables to increase efficiency of the reactor of anaerobic digestion of biomass.6 cl, 1 dwg
NOVELTY - The method involves separating fixed ammonium residual ammonia water and residual gas by a gas-liquid separator (1). The residual gas is continuously passed into a coal gas primary cooler (2). The fixed ammonium residual ammonia water is observed by the coal gas primary cooler. The fixed ammonium residual ammonia water is passed into a fixed ammonium removing process unit. Free ammonia residual ammonia water is passed into a free ammonia removing phenol treatment unit. A fixed ammonium decomposition process is performed by the fixed ammonium removing process unit.    USE - Coking residual ammonia water dephenolization processing method.    ADVANTAGE - The method enables reducing amount of sewage output and biochemical processing pressure. The method enables effectively recovering phenol residual ammonia water and achieve heat exchange among different separation processes so as to improve reasonable use effect. The method enables ensuring low energy consumption, processing cost and COD value so as to simplify basis of biochemical waste water treatment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a coking residual ammonia water dephenolization processing method.    Gas-liquid separator (1)    Coal gas primary cooler (2)    Mechanical clarification groove (3)    Absorbing settling oil remover (5)    Absorbing settling degreaser (6)
NOVELTY - An ethanol is manufactured from biomass feedstock by adding greater than or equal to 1 types of disinfectant to culture solution in culture tank which uses biomass feedstock at the process of carrying out saccharification fermentation process, and producing ethanol.    USE - Manufacture of ethanol from biomass feedstock (claimed).    ADVANTAGE - Proliferation of microorganisms is suppressed efficiently and ethanol is produced efficiently.
NOVELTY - Microbial catalyst which uses microalgae as substrate, comprises transgenic Tetrahymena pyriformis which is in state of expressing nucleic acid encoding polypeptide fragment of cellulase or its enzyme activity.    USE - The microbial catalyst which uses microalgae as substrate, is useful for producing biofuel, preferably ethanol and/or organic acid (all claimed).    ADVANTAGE - The catalyst eliminates chance of using plant biomass as raw materials for biofuel production and thus prevents environmental disruption, reduces cost of biofuel production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing biofuel, which involves cultivating the above-mentioned transgenic T.pyriformis in presence of microalgae.
NOVELTY - Preparing 3-(p-hydroxyphenyl)-propionic acid amide (II) amide involves carrying out catalytic hydrogenation reduction of hydroxycinnamic acid amide derivative (I) in side chain double bond in presence of a metal catalyst.    USE - The method is useful for preparing 3-(4-hydroxyphenyl)propionic acid amide (claimed), which is useful in pharmaceuticals, agrochemicals, cosmetics, plastic raw material, electronic information material, and optical material.    ADVANTAGE - The method has excellent productivity, is cost-effective, environmentally-friendly, and produces high yield of 3-(p-hydroxyphenyl)-propionic acid amide.    DETAILED DESCRIPTION - Preparing 3-(p-hydroxyphenyl)-propionic acid amide of formula (II) involves catalytic hydrogenation reduction of hydroxycinnamic acid amide derivative of formula (I) in side chain double bond in presence of a metal catalyst.    R=H, hydroxyl, or methoxy.
NOVELTY - Compost is prepared by subjecting compost raw materials to fermenting and drying processes using closed-type fermentation-drying apparatus, obtaining organic materials of fermented product, and granulating obtained product, where value of ignition loss of compost raw material before fermentation and drying processes is A %mass the value of ignition loss of compost after fermentation and drying processes is B %mass, and the value of (A-B) is 5-30 %mass.    USE - The compost is useful as fertilizer.    ADVANTAGE - The compost has excellent preservability and mechanical properties, contains optimal amount of decomposed organic matter, and improves germination rate of plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the compost, which involves (a) leaving 10-20% space to the closed-type fermentation-drying apparatus with respect to the internal volume of the apparatus, and supplying the compost raw material to the apparatus, (b) fermenting and drying the compost raw material under predetermined conditions, and (c) taking out a portion of the organic materials of fermented and dried product from the closed-type fermentation-drying apparatus, adding compost raw material into the organic materials which remained in the closed-type fermentation-drying apparatus for performing fermentation and drying process, and granulating the organic materials taken out from the closed-type fermentation-drying apparatus.
NOVELTY - Manufacture of biodiesel fuel involves reacting oil and fat containing fatty-acid glyceride and dialkyl carbonate in presence of sodium-methoxide catalyst to produce fatty-acid alkyl ester. The sodium-methoxide catalyst is obtained by dissolving solid sodium methoxide in organic solvent having boiling point less than that of dialkyl carbonate, and distilling-off organic solvent under reduced pressure.    USE - Manufacture of biodiesel fuel (claimed).    ADVANTAGE - The biodiesel fuel is manufactured without producing glycerol by-product.
NOVELTY - A hydrogen generating apparatus (1) consists of a charged particle generation unit (4) which generates charged particles and hydrogen from hydride gas by discharge, a gas dissociation unit (6) which generates hydrogen further by colliding with the particles containing hydrogen atom or hydride gas which remains after generating charged particles by electric field, and a hydrogen recovery system (9) which collects the hydrogen generated by the discharge and hydrogen generated by the collision of the charged particles.    USE - Apparatus is used for generating hydrogen (claimed) in hydrogen refueling station for electric vehicle.    ADVANTAGE - Hydrogen is efficiently generated using the apparatus, by safe and simple method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen generation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generating apparatus.    Hydrogen generating apparatus (1)    Charged particle generation unit (4)    Gas dissociation unit (6)    Hydrogen recovery system (9)    Gas injecting nozzle (10)
NOVELTY - The system (10) has high pressure gas-liquid separation apparatus (14) carrying out gas-liquid separation of hydrogen derived from water-electrolysis apparatus (12). Hydrogen piping (18) supplies hydrogen that water content is removed and derived from water-electrolysis apparatus to hydrogen storage unit. Cooling mechanism (20) provided in water-electrolysis apparatus or hydrogen piping cools hydrogen. Temperature sensor (22) from which detection temperature changes is provided in cooling mechanism according to whether fluid which flows through fluid detection unit is gas or liquid.    USE - High-pressure water electrolysis system.    ADVANTAGE - Since the temperature sensor from which detection temperature changes provides in cooling mechanism according to whether fluid which flows through fluid detection unit is gas or liquid, the temperature sensor provided in the cooling mechanism identifies gas and liquid from the change of the detection temperature. Thus, the high-pressure water electrolysis system prevents reliably that liquid water is contained in hydrogen, and obtains favorable product hydrogen by simple and economical structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for operating high-pressure water electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the high-pressure water electrolysis system. (Drawing includes non-English language text)    High-pressure water electrolysis system (10)    Water-electrolysis apparatus (12)    High pressure gas-liquid separation apparatus (14)    Hydrogen piping (18)    Cooling mechanism (20)    Temperature sensor (22)
NOVELTY - Natural capsaicin is produced by preparing chili oil resin, emulsifying agent, caustic acid, hydrochloric acid, and salt, dissolving caustic soda in water to form 5% alkali water, heating to 60-70 degrees C, adding 50 wt.% chili oil resin, stirring to dissolve and obtain chili oil resin concentrated solution, adding 5-10 times the weight of water, heating to 40-60 degrees C, mixing, dissolving to obtain dilute solution, titrating with hydrochloric acid to adjust pH to 6-9, standing, cooling for 72-96 hours, crystallizing, separating using centrifuge, filtering to collect mother liquor, and washing crystals.    USE - Production of natural capsaicin (claimed).    ADVANTAGE - Production of natural capsaicin is simple, safe, low-cost, and environment-friendly and has improved product yield.    DETAILED DESCRIPTION - Natural capsaicin is produced by preparing chili oil resin, emulsifying agent, caustic acid, hydrochloric acid, and salt, dissolving caustic soda in water to form 5% alkali water, heating to 60-70 degrees C, adding 50 wt.% chili oil resin, stirring to dissolve and obtain chili oil resin concentrated solution, adding 5-10 times the weight of water, heating to 40-60 degrees C, mixing, dissolving to obtain dilute solution, titrating with hydrochloric acid to adjust pH to 6-9, standing, cooling for 72-96 hours, crystallizing, separating using centrifuge, filtering to collect mother liquor, washing crystals with water, drying to obtain capsaicin finished product, adding 4-6 times the weight of salt to mother liquor, stirring and saturating, standing for 10 days to precipitate gel solid on liquid surface, filtering, recycling mother liquor, and emulsifying to obtain aqueous capsaicin product.
NOVELTY - Fertilizer comprises 10-40 pts. traditional Chinese medicine slag, 5-25 pts. peel, 5-15 pts. kelp soil, 5-15 pts. bean curd skin, 20-50 pts. poultry droppings, 5-20 pts. nitrogen fertilizer, 5-15 pts. phosphate fertilizer, 5-10 pts. bone residue, 10-25 pts. poultry wool, and 30-70 pts. beer.    USE - The fertilizer is useful for planting Impatiens balsamina.    ADVANTAGE - The fertilizer has balanced nutrition, and increases the production of Impatiens balsamina.
NOVELTY - The apparatus has an air nozzle portion that is arranged in an upper portion of the cassette and having an air movement for an air flow channel. Several nozzle holes which are defined along an inner side of the air nozzle section (20), which are directed towards the membrane electrode arrangement (MEAs) are arranged in the cassette, and are in communication with the air flow channel. An air intake portion is formed for a supply of ionized air from the outside to supply the ionized air to the air flow channel of the air nozzle section.    USE - Apparatus for removing static electricity for production device for fuel cell stack.    ADVANTAGE - The static electricity between the MEAs and the intermediate layer is removed, so that a failure and reject rate of the mounting unit for the finished multi-layer MEAs is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the apparatus for removing static electricity for a device for producing a fuel cell stack.    Cassette (10)    Raised portion (11)    Support element (12)    Nozzle section (20)    Air flow duct (21)
NOVELTY - The plate (10) has a flow area (12) provided with a first flow element (34) and a second flow element (36). The first flow element is formed to flow around a reactant into a first side (44) and arranged downstream to a main flow direction (38). The second flow element is formed to flow around the reactant into a second side (46). A vector (48) is extended from an upstream end to a downstream end of the first flow element. Another vector (50) is extended from an upstream end to downstream end of the second flow element. The flow area is provided in an active region (16) of the plate.    USE - Polar plate for a fuel cell (claimed) for generating electrical power. Can also be used for a high temperature polymer electrolyte (HT-PEM) membrane fuel cell and a low temperature polymer electrolyte membrane (NT-PEM) fuel cell.    ADVANTAGE - The first flow element is formed to flow around the reactant into the first side and arranged downstream to the main flow direction, and the second flow element is formed to flow around the reactant into the second side, thus ensuring optimum transfer of the reactants on a membrane electrode unit of a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of a portion of polar plate.    Polar plate (10)    Flow area (12)    Active region (16)    Flow elements (34, 36)    Main flow direction (38)    Sides (44, 46)    Vectors (48, 50)
NOVELTY - Reducing ammonia emissions during drying liquid biogenic waste materials, comprises adjusting pH value of waste materials to less than or equal to 6.2, and adding iron(III) salt including ferric chloride, ferric chloride sulfate and ferrous sulfate.    USE - The method is useful for reducing ammonia emissions during drying liquid biogenic waste materials (claimed).    ADVANTAGE - The method reduces ammonia in exhaust air from drying plants of liquid biogenic waste materials, and is cost-efficient and environmentally friendly.
NOVELTY - The present invention discloses an apparatus of using electrolysis ozone generator to readily manufacture ozone water and hydrogen water, which comprises an ozone-water mixing keg, a pure water keg, a pure water replenishment device, an electrolysis ozone generator, and a circuit control board, characterized in that the electrolysis ozone generator is connected with the hydrogen-water mixing keg, the hydrogen-water mixing keg is connected with the water inlet through a hydrogen-water inlet solenoid valve, and the hydrogen-water mixing keg is connected with a hydrogen-water aeration keg; the ozone-water mixing keg is connected with the water inlet through an ozone-water inlet solenoid valve, the ozone-water mixing keg is connected with the ozone-water aeration keg, and the ozone-water aeration keg and the hydrogen-water aeration keg are connected to the sewage outlet and the water outlet, respectively. The present invention is simple in structure and practical, low-cost, energy-efficient, and extremely easy to use, whereby highly pure hydrogen produced by the electrolysis ozone generator can be stored in order to produce hydrogen water at any time.
NOVELTY - The system (1) comprises a plasma processing part, in which the heated waste gas is delivered from a heating portion (13). The heating portion is provided for heating up the waste gas. The heating portion is processed in a heating source for the heating at a plasma processing part (15). and which is ejected. A heating housing includes a body, which is arranged to surround a portion or the whole of a gas flow line. The methane gas is provided for reducing atmosphere composition supplied in the plasma processing part.    USE - System for treating waste gas.    ADVANTAGE - The plasma processing part, in which the heated waste gas is delivered from a heating portion and the heating portion is provided for heating up the waste gas, thus reduces the energy damping for the waste gas heating, reduces the high-capacity fluorid from the waste gas treating system, ad also reduces the generation of the secondary pollutant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a waste gas treating method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a waste gas treatment system. (Drawing includes non-English language text).    Waste gas treating system (1)    Dust collection part (11)    Heating portion (13)    Plasma processing part (15)    Wet processor (17)
NOVELTY - The device has a porosity anode adhered with a fluoride group cation exchange membrane that supplies pure water to a porosity cathode as a raw material. The porosity cathode electrolyzes the pure water. Dissolution hydrogen molecule density of the electrolyzed water is 1ppm. The porosity cathode is formed with a hole. A gap formed between the fluoride group cation exchange membrane and the porosity cathode is filled with an ion-exchange resin material. A raw material sprinkler pipe is connected with a side of a solid solution zone hydrogen molecule water tank.    USE - Device for generating electrolyzed dissolved hydrogen water in a solid solution zone hydrogen molecule water tank (claimed) to clean a semiconductor device. Can also be used for producing drinking water.    ADVANTAGE - The porosity anode is adhered with the fluoride group cation exchange membrane that supplies the pure water to the porosity cathode as the raw material, and the porosity cathode electrolyzes the pure water so as to easily produce dissolved hydrogen water, and extend expiry time of the dissolved hydrogen water.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a device for generating electrolyzed dissolved hydrogen water in a solid solution zone hydrogen molecule water tank.
NOVELTY - The apparatus (15) has an anode cell (8) accommodated in saturated salt solution (7) or seawater. Phosphate ion, ammonium-ion and magnesium ion are contained in organic waste water (5). A partial partition wall of a magnesium ammonium phosphate (MAP) crystal production tank (6) is provided with the anode cell fixed in a cation exchange part (1) and air cathode cell (10) fixed in an anion exchange part (3). A magnesium ammonium phosphate crystal is manufactured by the MAP crystal production tank. An anode (11) is made of magnesium metal or magnesium alloy.    USE - Air-cell-type reaction apparatus for use during treatment process of waste water. Uses include but are not limited to precipitation water, pigsty waste water, dairy-cow-shed waste water, organic industrial waste water and sodium chloride aqueous solution i.e. electrolyte.    ADVANTAGE - The apparatus has large electrochemical reaction rate, so that large exothermic reaction energy of the apparatus can be attained. The solubility of the organic waste water is small, so the magnesium hydroxide and MAP are easy to separate into solid and liquid at precipitation or filtration in a convenient manner. The apparatus saves energy resources.    DETAILED DESCRIPTION - The air cathode cell is provided with an air cathode (12). The air cathode is made of porous metal, magnesium and porous carbon material. An INDEPENDENT CLAIM is also included for an air-cell-type reaction method.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic top view and longitudinal cross-sectional views of an air-cell-type reaction apparatus.    Cation exchange part (1)    Anion exchange part (3)    Organic waste water (5)    Crystal production tank (6)    Saturated salt solution (7)    Anode cell (8)    Air cathode cell (10)    Anode (11)    Air cathode (12)    Air-cell-type reaction apparatus (15)
NOVELTY - Reclamation of slope in fast fertilization of purple soil comprises improving organic and inorganic fertilizer carbon structure, enhancing organic and inorganic nutrient synergistic fertility, and conducting reclamation of arable land by choosing purple soil reclamation slope with gradient of less than 20 degrees , using rich agricultural organic waste from rural area, mixing biological and agronomic practices, using reclamation barren slope purple soil as carrier, constructing nutrient, microbes, crops soil structure with medium fertility level and conducting fast and continuous improvement program.    USE - the method is useful for reclamation of slope in fast fertilization of purple soil (claimed).    ADVANTAGE - The method is easy and simple to operate, uses accessible raw materials, is economical, does not affect normal use of reclaimed soil, really realizes the cultivation of fertilizer, and has good social and economic benefits.
NOVELTY - Producing fertilizer mixing phosphoric acid and urea at a molar ratio of 1.8:1.1-1.4 then heating at 4 degrees C/minute, raising the temperature to 84-104 degrees C and then stirring for 30 minutes to obtain urea phosphate slurry, adjusting a pH of the slurry, using ammonia, to 3.3-3.6 and then stirring, placing the slurry in a cooling crystallizer to cool at 25 degrees C, crystallizing the mixture and then filtering to obtain filtrate containing ammonium dihydrogen phosphate, and adding trace elements, potassium, and mother liquor to the obtained filtrate and then drying.    USE - The method is useful for producing fertilizer, which is useful for blueberries (claimed).    ADVANTAGE - The method is capable of economically producing the fertilizer in an environmentally friendly manner.    DETAILED DESCRIPTION - Producing fertilizer mixing phosphoric acid and urea at a molar ratio of 1.8:1.1-1.4, where the concentration of phosphoric acid is 68-72% and then heating at 4 degrees C/minute, raising the temperature to 84-104 degrees C and then stirring for 30 minutes to obtain urea phosphate slurry, adjusting a pH of the slurry, using ammonia, to 3.3-3.6 and then stirring, placing the slurry in a cooling crystallizer to cool at 25 degrees C, crystallizing the mixture and then filtering to obtain filtrate containing ammonium dihydrogen phosphate, and adding trace elements, potassium and mother liquor to the obtained filtrate and then drying.
NOVELTY - Promoting growth of gas hydrates, comprises passing gas hydrate promoter solution into gas and then stirring at temperature of 0-20 degrees C, a pressure of 0-15 MPa and a rotating speed of 400-600 revolutions per minute (rpm) for 3-13 minutes, where the concentration of the gas hydrate promoter solution is 100-1000 parts per million (ppm).    USE - The method is useful for promoting growth of gas hydrates (claimed).    ADVANTAGE - The method effectively promotes the growth of gas hydrates in an economical manner, and reduces the surface tension of gas hydrates.
NOVELTY - Preparing tobacco-specific organic fertilizer comprises preparing a substrate material using 80-90 pts. pig manure (moisture content of 70-80%) and 10-20 pts. seed cake (rapeseed cake or a mixture of rapeseed cake and peanut bran), allowing the housefly eggs to access on the substrate material, incubating the housefly larva on culture material for biotransformation, where the tobacco-specific material is converted into tobacco-specific organic fertilizer.    USE - The method is useful for preparing tobacco-specific organic fertilizer (claimed).    ADVANTAGE - The method is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for tobacco-specific organic fertilizer.
NOVELTY - A biological fermentation fertilizer comprises 100 pts. wt. shrimp powder, 70-100 pts. wt. shell powder, 40-50 pts. wt. cedar, 20-30 pts. wt. prepared chicken manure, 10-15 pts. wt. humic acid, 5-10 pts. wt. Bacillus subtilis var natto, 5-10 pts. wt. citric acid, and 1-4 pts. wt. plant ash.    USE - A biological fermentation fertilizer used for black tulip flowering period (claimed).    ADVANTAGE - The fertilizer improves black tulip flowering rate, and achieves bigger and fuller flowers.
NOVELTY - Industrial production of seaweed fertilizer is carried out by adding water, calcium hydroxide and potassium hydroxide in reaction kettle, then adding dry seaweed, and raising temperature to 70 degrees C and reacting for a period of time adding filter liquid with nitric acid for neutralization, and adding ammonium phosphate to obtain seaweed extract liquid to be directly used as liquid seaweed fertilizer; and mixing filter residue and furfural residue, exposing to sunlight, then stirring until pH reaches 5.5-7 to obtain soil solid fertilizer.    USE - Method for industrial production of seaweed fertilizer (claimed) used for organic vegetables.    ADVANTAGE - The method utilizes furfural production residue to reduce waste and avoid environment pollution. The prepared liquid seaweed extract is pure natural green fertilizer, and can provide nitrogen, phosphorus, potassium, and calcium elements needed for metabolism of plants and so that plants can adapt to external environment.
NOVELTY - Potted flower fertilizer comprises 5-8 pts. wt. bean cake, 10-15 pts. wt. wheat and corn straw, 2-3 pts. wt. sesame cake, 1-2 pts. wt. wooden meal, 3-5 pts. wt. plant ash, 0.3-0.5 pt. wt. peanut shell, 0.2-0.3 pt. wt. conch meal, and 30-35 pts. wt. human and livestock manure.    USE - Potted flower fertilizer.    ADVANTAGE - The potted flower fertilizer can supply the needed nutrients for growing potted flower and provides potted flower with deep green leaves and bright color.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of potted flower fertilizer comprising uniformly mixing the raw materials except plant ash, putting into a sealed jar, fermenting at 28-32 degrees C for 32-38 days, adding plant ash, continuously fermenting for 5-8 days and obtaining the finished product.
NOVELTY - Cowpea fertilizer comprises 16-18 pts. mass nitrogenous fertilizer, 10-12 pts. mass phosphate fertilizer, 10-12 pts. mass potash fertilizer, 10-20 pts. mass chitin, 20-30 pts. mass algae, 80-100 pts. mass fermented dairy manure, 3-5 pts. mass diammonium phosphate, 1-3 pts. mass humic acid, 20-30 pts. mass plant ash, 40-60 pts. mass cassava residue and 20-30 pts. mass lees.    USE - Cowpea fertilizer.    ADVANTAGE - The cowpea fertilizer increases the cowpea production rate and quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cowpea fertilizer comprising mixing the raw materials, crushing and fermenting in a closed jar, preheating the screw mixer at 70-90 degrees C, maintaining the temperature, adding the raw materials into the screw mixer, mixing while maintaining mold head pressure at 1.2-1.4 MPa, and forming cowpea granular fertilizer.
NOVELTY - Fertilizer accelerator comprises an adsorbent and polyglutamic acid crosslinked product in a mass ratio of 1:(20-50).    USE - Used as fertilizer accelerator.    ADVANTAGE - The method: comprises activated carbon, which ensures adsorption and fixation of polyglutamic acid biological macromolecule; has faster decomposition rate in comparison with conventional microbial fermentation; prolongs the fertilizer effect (from 7-10 days to 60 days); and provides fertilizer, which is applied only once.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the fertilizer accelerator, comprising (a) placing adsorbent in polyglutamic acid producing microbial fermentation broth and fermenting polyglutamic acid, and (b) crosslinking polyglutamic acid.
NOVELTY - Preparing a green roof growing media comprises taking green garden waste and then crushing, adding municipal domestic sludge to the garden waste, uniformly mixing to obtain a mixture, regulating water content to 55-65%, stirring the mixture, ventilating the mixture for 10-15 minutes, composting the mixture at 50-60 degrees C for 15-20 days under high temperature aerobic conditions to obtain a compost, stopping composting for 45-50 minutes, circulating air for 30-40 days, adding perlite and garden waste to the compost, mixing, again composting the mixture for 15-20 days, and uniformly stirring.    USE - The method is useful for preparing a green roof growing media (claimed).    ADVANTAGE - The method prepares the green roof growing media with increased utilization rate and reduced cost in an eco-friendly manner.    DETAILED DESCRIPTION - Preparing a green roof growing media comprises taking green garden waste and then crushing, adding municipal domestic sludge to the crushed garden waste, uniformly mixing to obtain a mixture, where the green garden waste is deadwood, fallen leaves and/or herbs, regulating water content to 55-65%, stirring the mixture having a quality ratio of 25-30, ventilating the stirred mixture having a ventilation rate of 200-300 L/H for 10-15 minutes, composting the ventilated mixture at 50-60 degrees C for 15-20 days under high temperature aerobic conditions to obtain a compost, stopping composting for 45-50 minutes, circulating air for 30-40 days, adding perlite and garden waste having a volume ratio of 5:15:1 to the compost, uniformly mixing, further composting the mixture for 15-20 days, finishing composting, and uniformly stirring.
NOVELTY - Liquid fertilizer comprises 6-10 pts. wt. straw ash, 5-9 pts. wt. potassium fulvate, 1-3 pts. wt. polyacrylamide, 4-8 pts. wt. monopotassium phosphate, 4-11 pts. wt. castor bean, 8-14 pts. wt. carrot, 3-8 pts. wt. sodium tetraborate, 4-7 pts. wt. potassium indole butyric acid, 2-6 pts. wt. ammonium citrate, 3-5 pts. wt. ferrous sulfate, 5-10 pts. wt. colloidal Bacillus mucilaginosus liquid, 3-8 pts. wt. radix stemonae powder, 4-10 pts. wt. soluble potash, 2-8 pts. wt. EDTA and 0.5-2 pts. wt. soil conditioning agent.    USE - Used as a liquid fertilizer.    ADVANTAGE - The liquid fertilizer: has long-lasting effect; and increases absorption rate of crop, increases crop yield and the economic benefit.
NOVELTY - Fertilizer comprises 12-14 pts. wt. rotten cattle manure, 7-9 pts. wt. grass, 4-6 pts. wt. humic acid, 22-25 pts. wt. nitrogen fertilizer, 19-21 pts. wt. phosphate fertilizer, 17-19 pts. wt. calcium chloride, 13-15 pts. wt. composite microorganism fertilizer, 12-14 pts. wt. Actinomyces, 11-13 pts. wt. ammonium oxalate, 9-12 pts. wt. magnesium sulfate, 5-7 pts. wt. boron fertilizer, 3-5 pts. wt. ammonium citrate, 1-3 pts. wt. hymexazol, 2-4 pts. wt. planted neomycin, and 50-60 pts. wt. water.    USE - The fertilizer is useful for cabbage (claimed) to promote the growth.    ADVANTAGE - The fertilizer improves the nutrition substance and taste of the cabbage, and increases the yield and quality of the cabbage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer, comprising uniformly mixing the above raw materials and then sealing and fermenting for 6 hours.
NOVELTY - Cabbage fertilizer comprises 25-27 pts. wt. farmyard manure, 19-21 pts. wt. borax, 15-17 pts. wt. ammonium sulfate, 13-14 pts. wt. complex microbial fertilizer, 11-13 pts. wt. potassium sulfate, 10-13 pts. wt. monopotassium phosphate, 9-11 pts. wt. manganese slag, 7-9 pts. wt. ammonium citrate, 4-6 pts. wt. plant ash, 5-7 pts. wt. cow dung, 2-3 pts. wt. humic acid organic fertilizer, 1-3 pts. wt. amino acid, 1-2 pts. wt. germ fertilizer, 2-4 pts. wt. thiram wettable powder, 1-3 pts. wt. carbendazim and 40-50 pts. wt. water.    USE - The fertilizer is used for promoting plant metabolism, preventing and treating plant diseases and insect pests.    ADVANTAGE - The fertilizer provides required nutrition element for cabbage growth; increases plant growth, and permeability of soil; and promotes absorption, and increase use rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing cabbage fertilizer comprising mixing farmyard manure, borax, ammonium sulfate, complex microbial fertilizer, potassium sulfate, monopotassium phosphate, manganese slag, ammonium citrate, plant ash, cow dung, humic acid organic fertilizer, amino acid, germ fertilizer, thiram wettable powder, carbendazim, and water, stirring for 30 minutes, homogenizing, and drying to obtain cabbage fertilizer.
NOVELTY - Fertilizer comprises 26-28 pts. wt. water, peanuts and green manure mixture, 24-26 pts. wt. ammonium carbonate, 19-22 pts. wt. calcium superphosphate, 15-17 pts. wt. microbial growth regulators, 13-16 pts. wt. tea seed cake fertilizer, 11-14 pts. wt. cattle manure, 9-12 pts. wt. fly ash, 1-3 pts. wt. carbendazim, 2-3 pts. wt. urease inhibitor, 4-6 pts. wt. sulfuric acid, 3-5 pts. wt. sodium borate, 4-9 pts. wt. Kudzu root powder, 6-8 pts. wt. organophosphorus fertilizer, 3-5 pts. wt. borax, 1-3 pts. wt. thiram wettable powder, and 50-60 pts. wt. water.    USE - The fertilizer is useful for white gourd (claimed) to promote fruit.    ADVANTAGE - The fertilizer enhances disease resistance ability in white gourd, has long lasting effect, increases yield of white gourd, and can be simply prepared with rich nutritional value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer comprising mixing the above raw materials, uniformly stirring the mixture, homogenizing, sealing, fermenting for 3 hours and then drying.
NOVELTY - Fertilizer comprises 19-22 pts. wt. Chinese trumpet creeper green fertilizer, 18-22 pts. wt. chicken manure, 17-20 pts. wt. calcium superphosphate, 15-18 pts. wt. ammonium hydrogen carbonate, 13-16 pts. wt. microbial growth regulators, 6-8 pts. wt. phosphorus pentoxide, 4-7 pts. wt. slag fertilizer, 6-9 pts. wt. alginic acid, 2-6 pts. wt. Tithonia inulin, 6-9 pts. wt. magnesium sulfate heptahydrate, 8-10 pts. wt. plant ash, 3-5 pts. wt. humic acid, 4-8 pts. wt. dicyandiamide, 2-4 pts. wt. zineb, and 50-60 pts. wt. water.    USE - The fertilizer is useful for melon (claimed) to promote growth.    ADVANTAGE - The fertilizer promotes melon swelling, and improves fertilizer efficiency, soil compaction and fruit sugar content, thus enhancing taste of the melon.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer comprising uniformly mixing the above raw materials and stirring the mixture for 20 minutes.
NOVELTY - Fertilizer comprises 20-22 pts. wt. rotten pig manure, 10-12 pts. wt. fly ash, 19-21 pts. wt. urea, 16-18 pts. wt. ammonium sulfate, 13-15 pts. wt. fused calcium-magnesium phosphate, 12-14 pts. wt. Wang green manure, 10-12 pts. wt. copper sulfate, 7-9 pts. wt. mildew fertilizer, 4-6 pts. wt. Bacillus preparation, 2-4 pts. wt. aminoethyl amine, 1-3 pts. wt. anti-cropping agent, 2-5 pts. wt. humic acid, and 60-80 pts. wt. water.    USE - The fertilizer is useful for betel nut taro (claimed) (Colocasia esculenta).    ADVANTAGE - The fertilizer can be simply prepared with low cost, significantly increases the yield, meat quality, crispiness and delicious taste of betel nut taro, and improves soil compaction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer comprising mixing the above raw materials, uniformly stirring the mixture, sealing, fermenting for 4 hours, drying and then bagging.
NOVELTY - Fertilizer comprises 80-100 pts. wt. dairy manure, 10-12 pts. wt. nitrogen, 4-6 pts. wt. phosphate, 8-10 pts. wt. potash, 20-30 pts. wt. tobacco, 10-12 pts. wt. Rumex acetosa, 8-10 pts. wt. felon herb, 20-30 pts. wt. tea seed cake, 12-14 pts. wt. common Andrographis herb, 5-7 pts. wt. Tripterygium, 2-4 pts. wt. zinc sulfate, and 10-12 pts. wt. humic acid.    USE - The fertilizer is useful for rape plant (claimed) to prevent soil pests, preferably insects.    ADVANTAGE - The fertilizer can be effectively prepared with improved soil fertility and without pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer comprising crushing the above raw materials into powder using a crusher, fermenting the crushed materials in a fermentation tank, pre-heating the fermented material at 80-100 degrees C, and placing the obtained material into a single screw kneader at a pressure of 1-1.2 Mpa, then granulating.
NOVELTY - Preparation of bisphenol B comprises sequentially adding phenol, butanone and composite catalyst into a reaction container, uniformly mixing, reacting at 30-40 degrees C for 8-15 hours, raising the temperature to 55-65 degrees C, filtering while hot, obtaining filtrate and filter residue, placing the filtrate at 200-700 Pa and 75-90 degrees C, removing phenol by evaporation, obtaining crude product, dissolving the crude product in alcohol solvent and obtaining crystal.    USE - Preparation of bisphenol B (claimed).    ADVANTAGE - The method does not require the use of alkali liquid, uses catalyst, which can be repeatedly used, saves the cost, and carries out refining without the need for water, thus, reducing environmental pollution.
NOVELTY - A radioactive cesium is removed by culturing bacteria in humus, Actinomyces and filamentous fungi in culture solution containing carbon source, nitrogen source and mineral source, obtaining cellulase containing liquid, swelling cellulose contained in cellulose containing body by cellulase or humus contained in soil by cellulase, removing by hydration the radioactive cesium by which cellulose containing body is adsorbed, moving removed radioactive cesium by celullase containing liquid and washing liquid and removing from cellulose containing body.    USE - Removal process of radioactive cesium (claimed).    ADVANTAGE - Enough amount of radioactive cesium is removed.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) cellulase comprising swollen cellulose which is contained in cellulose containing body or swollen humus contained in soil; (2) cellulase containing liquid comprising cellulase which is produced by greater than or equal to 1 of bacteria, Actinomyces and filamentous fungi; and (3) manufacture of cellulase containing liquid which involves culturing greater than or equal to 1 of bacteria, Actinomyces and filamentous fungi contained in humus in culture solution containing carbon source, nitrogen source, and mineral source, and obtaining cellulase containing liquid when greater than or equal to 1 of bacteria, Actinomyces, and filamentous fungi produces a cellulase in the culture solution.
NOVELTY - The electrolysis cell stack apparatus (1) has electrolysis cell stack that is included with several electrolysis cells (2) respectively having cathode, solid electrolyte, and anode. A water vapor containing gas introducing unit is provided to supply the gas which contains water vapor in electrolysis cell. A hydrogen-containing-gas derivation unit is provided to recover the gas containing hydrogen. A combustion unit is arranged at hydrogen-containing-gas derivation unit.    USE - Electrolysis cell stack apparatus for use in electrolyzer (claimed).    ADVANTAGE - The hydrogen-containing-gas derivation unit is provided to recover the gas containing hydrogen, thus the electrolysis cell stack apparatus which recovers high concentration hydrogen is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolysis cell of electrolysis cell stack apparatus.    Electrolysis cell stack apparatus (1)    Electrolysis cell (2)    Cover unit (4)    Manifold (7)    Combustion catalyst (23)
NOVELTY - A variant of a parent glycoside hydrolase, comprising a substitution at one or more positions corresponding to positions 21, 94, 157, 205, 206, 247, 337, 350, 373, 383, 438, 455, 467, and 486 of fully defined 513 amino acids (SEQ ID NO: 2), given in the specification, and optionally further comprising a substitution at one or more positions corresponding to positions 8, 22, 41, 49, 57, 113, 193, 196, 226, 227, 246, 251, 255, 259, 301, 356, 371, 411, and 462 of amino acids 1-513 of SEQ ID NO: 2, where the variant has glycoside hydrolase activity, is new.    USE - The variant of a parent glycoside hydrolase is useful in producing a detergent composition, and in a method of degrading cellulose- and hemicellulose-containing biomass (claimed).    ADVANTAGE - The variant of a parent glycoside hydrolase has improved properties including altered temperature-dependent activity profiles, thermostability, pH activity, pH stability, substrate specificity, product specificity, and chemical stability as compared to its parent enzyme.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a detergent composition which comprises the variant and a surfactant; and    (2) a method for degrading cellulose- and hemicellulose-containing biomass, which comprises treating the biomass with an effective amount of the variant and recovering the degraded biomass.
NOVELTY - Manufacturing a (R)-2-amino-3-biphenyl-4-yl-propan-1-ol sulfuric acid compound (Va), involves reduction of a biphenyl compound (III) with a metal borohydride, resulting in an N-acyl protected R-biphenylalaninol compound (IV), and hydrolysis of (IV) using sulfuric acid.    USE - The process is useful for manufacturing a (R)-2-amino-3-biphenyl-4-yl-propan-1-ol sulfuric acid compound (Va), which is useful for producing an active pharmaceutical (claimed) such as a NEP inhibitor. No biological data given.    ADVANTAGE - The process provides N-tert-butoxycarbonyl protected R-biphenylalaninol in an inexpensive, safe and environmentally friendly manner, thus the process is an industrially viable process.    DETAILED DESCRIPTION - Manufacturing a (R)-2-amino-3-biphenyl-4-yl-propan-1-ol sulfuric acid compound of formula (Va), involves reduction of a biphenyl compound of formula (III) with a metal borohydride, resulting in an N-acyl protected R-biphenylalaninol compound of formula (IV), and hydrolysis of (IV) using sulfuric acid.    R = methyl or phenyl; and    R1 = methyl.    INDEPENDENT CLAIMS are included for:    (1) the N-acyl protected biphenylalaninol compound (IV); and    (2) the (R)-2-amino-3-biphenyl-4-yl-propan-1-ol sulfuric acid compound (Va).
NOVELTY - Conditioning fertilizer granules for improved dust control and/or agricultural benefits, involves: providing fertilizer granules having a surface temperature of 50-250 degrees F; introducing an aqueous conditioning agent with or without beneficial agricultural and/or dedusting additives; optionally subjecting the fertilizer granules with an aqueous conditioning agent on it to a mechanical energy exposure and/or a fluidized bed reactor; and removing added moisture from the aqueous conditioning agent from the granules until a final moisture content of the granules is 0-6.5 wt.% of the granules.    USE - The method is useful for conditioning fertilizer granules for improved dust control and/or agricultural benefits (claimed), where the conditioned fertilizer granules are useful to enhance the growth and development of plants and treat plant diseases. No biological data given.    ADVANTAGE - The method reduces the generation of dust during handling, transport, and storage of the fertilizers, and/or increases the agricultural benefits of the fertilizer, thus reducing raw material costs and/or manufacturing costs.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) introducing one or more agriculturally beneficial additives to fertilizer granules in a conditioning vessel, where one or more agriculturally beneficial additives comprises one or any combination of biological material; and    (2) a system for introducing agriculturally beneficial and/or dedusting additives to fertilizer granules.
NOVELTY - Production of partially refined waste glycerol involves refining crude glycerol containing organic impurities, deoiling resultant product using a hydrophobic solvent to extract organic impurities, dewatering the resultant product by drying at an elevated temperature, and desalting the resultant product using a polar solvent to precipitate salt.    USE - Production of partially refined waste glycerol used as adhesive, paint and coating in food, pharmaceutical and cosmetic applications.    ADVANTAGE - The method enables production of partially refined waste glycerol with high yield, by environmentally-friendly and economical process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) partially refined waste glycerol, which is derived from processing natural fats and oils. The partially refined waste glycerol comprises reduced salt and organic impurities; and    (2) process of refining crude glycerol, which involves mixing crude glycerol with hydrophobic solvent to remove organic impurities, drying obtained deoiled glycerol to produce deoiled and dewatered glycerol, and adding polar solvent to precipitate salt and produce deoiled, dewatered and desalted glycerol.
NOVELTY - The electrolytic cell (3) has a media control system which is provided with a media distribution structure (5). The supply channels (2) are arranged on two opposite sides outside the media distribution structure. The inflow regions (4) are optionally arranged between media distribution structure and supply channel. The supply channels include channels (2.1) for water supply, drainage and oxygen removal, and channels for hydrogen removal.    USE - Electrolytic cell for electrolysis stack (claimed).    ADVANTAGE - The uniform supply of the active area in the flow field with the starting materials and the disposal of products are ensured from the flow field. The configuration of the supply channels, the inlet or inflow regions and the designated area is minimized. By the minimization of ranges, the reduction of installation space and cost is achieved and increase in the power density of electrolysis stack is achieved. The blockade of the active surface is prevented and the power density of corresponding electrolysis stack is increased. The water accumulation and the rise of the product gases against gravity are achieved through the electrolysis cell against gravity, preferably by designing the supply channels. The power density of corresponding electrolysis stacks is increased by saving space and costs. The efficiency of the use of available space and the efficiency of supply of the active area are increased. The electrolysis stack is produced at lower cost and higher power density due to the optimized use of the available space and the efficient supply and removal of reactants and products.    DESCRIPTION OF DRAWING(S) - The drawings show the sectional view of the electrolysis stack and plan view of the electrolytic cell.    Supply channel (2)    Channel for water supply, drainage and oxygen removal (2.1)    Electrolytic cell (3)    Inflow region (4)    Media distribution structure (5)
NOVELTY - Fermentative production of 4C-products from lignocellulose-containing biomass by a microorganism-strain comprises using a microorganism-strain with a citrate-phosphate-dextrose-adenine (cpdA) gene in the fermentation as production strain for natural 2,3-butanediol production, in which the gene is inactivated CPDA.    USE - The microorganism-strain comprising inactivated cpdA gene, is useful for natural 2,3-butanediol production for fermentative production of 4C products of sugars derived from lignocellulose-containing biomass (claimed).    ADVANTAGE - The method produces improved yield of 4C products, preferably yield of at least 100 g/l.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the microorganism-strain with a citrate-phosphate-dextrose-adenine (cpdA) gene for natural 2,3-butanediol production, which is able to utilize sugar found in lignocellulose-containing biomass as carbon source, during the fermentative production of 4C products, comprising cpdA gene, except for strains of the species Klebsiella pneumoniae and Serratia marcescens type.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the pKD13 vector.
NOVELTY - The method involves making the inside of a carbonization furnace into anoxic state by filling of superheated steam. A plant is injected in the carbonization furnace, and is carbonized after the filling of the superheated steam. The gas containing the vaporized wood vinegar is discharged from the carbonization furnace. The gas containing the vaporized wood vinegar is cooled and is set as the liquid containing wood vinegar. The pH value of the extracted wood vinegar is 3.5 or less.    USE - Method of extracting wood vinegar.    ADVANTAGE - The wood vinegar is extracted from the plant, without blowing in superheated steam in the carbonization furnace. Since the pH value of the extracted wood vinegar is 3.5 or less, the high quality of wood vinegar is obtained. Since the radioactive substance is immobilized by the charcoal in which plant is carbonized and grown, the radioactive substance is not contained in the gas containing the vaporized wood vinegar. Hence, the gas containing the wood vinegar is discharged safely from carbonization furnace.
NOVELTY - Usage method of fertilizer for promoting rooting in seedlings, involves (a) mixing the fertilizer with soil at the time of seeding, stirring mixture, taking the mixture as soil substrate, adding the soil substrate to seedling tray, filling the tray with the soil substrate up to half of its total volume, spreading seeds on the soil substrate, covering the seeds with the soil substrate up to a height of 2-2.5 cm, and compacting the soil substrate, and (b) spreading 10-15 g fertilizer on the soil every 15-20 days after seed emergence, and sprinkling water on the soil.    USE - Usage method of fertilizer for promoting rooting in seedlings (claimed).    ADVANTAGE - The usage method is simple, and enables to increase rooting rate and root system of seedlings by 4-8 times as compared to existing fertilizers.    DETAILED DESCRIPTION - Usage method of fertilizer for promoting rooting in seedlings, involves (a) mixing the fertilizer with soil in a mass ratio of 1-1.5:60-80 at the time of seeding, stirring mixture, taking the mixture as soil substrate, adding the soil substrate to seedling tray, filling the tray with the soil substrate up to half of its total volume, spreading seeds on the soil substrate, covering the seeds with the soil substrate up to a height of 2-2.5 cm, and compacting the soil substrate, and (b) spreading 10-15 g fertilizer on the soil every 15-20 days after seed emergence, and sprinkling water on the soil, where the fertilizer is prepared by mixing biogas residues and soapstock in a mass ratio of 7:1, adding diammonium hydrogen phosphate, fermented corncob product, oyster powder, urea, seaweed meal, sodium alpha -naphthyl acetate, potassium humate, potassium sulfate and wetting agent to obtained mixture, and obtaining 5.5% aqueous solution of fertilizer.
NOVELTY - A sewage treatment agent comprises active enzyme modified activated carbon granules and aluminum hydroxide, aluminum sulfate, polyaluminum chloride (PAC), polyaluminum sulfate (PAS), polymeric ferric chloride (PFC), and/or polymeric ferric sulfate (PFS) as additive.    USE - Sewage treatment agent used for processing heavy metal polluted sewage and organic pollutant sewage (claimed).    ADVANTAGE - The sewage treatment agent has excellent treatment effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of sewage treatment agent comprising dispersing active enzyme in deionized water, adding activated carbon, stirring at 30-40 degrees C for 10-40 minutes, standing for 2 hours, filtering, and drying; and mixing with additive.
NOVELTY - An aerobic compost and wheat straw stick dry anaerobic fermentation coupling system comprises biological carbon waste gas purifier, straw dry anaerobic fermenter, and aerobic compost device. The biological carbon waste gas purifier has clean waste gas discharge pipe and waste gas biological carbon material discharge valve. The aerobic compost device has decomposed organic fertilizer discharging valve. The straw dry anaerobic fermenter has marsh gas output pipe.    USE - Aerobic compost and wheat straw stick dry anaerobic fermentation coupling system.    ADVANTAGE - The system has simple configuration and low cost. It provides high straw degradation rate, and avoids environment pollution.
NOVELTY - Foliar liquid fertilizer comprises a mixture A, a mixture B and water as a carrier. The mixture A comprises 50-80 pts. wt. dipotassium hydrogen phosphate and 4-6.4 pts. wt. mannitol. The mixture B comprises 2-4 pts. wt. glacial acetic acid.    USE - The foliar fertilizer is useful in field crops comprising rice, wheat and corn, and fruit crops comprising apple, grape and orange (all claimed).    ADVANTAGE - The foliar fertilizer can be safely prepared with high nutrition content, good fluidity, reduced toxicity and low viscosity in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the foliar fertilizer comprising adding the mixture A and water into a reaction container, uniformly mixing, heating the mixture at 80-120 degrees C, reacting the heated mixture for 1-5 hours, adding the mixture B to the reacted mixture, and uniformly stirring.
NOVELTY - Fermented corncob material comprises 40-50 wt.% of corncob, 30-40 wt.% of wood chips, 2-10 wt.% of wheat bran, 2-10 wt.% of rice bran, 1 wt.% of gypsum, 1 wt.% of lime, 1 wt.% of phosphate fertilizer, and 0.1 wt.% of carbendazim.    USE - The fermented corncob material is useful for cultivation of fungus (claimed).    ADVANTAGE - The corncob material rapidly cultivates the fungus at low cost.    DETAILED DESCRIPTION - AN INDEPENDENT CLAIM is also included for cultivating fungus using fermented corncob material comprising crushing corncob with a grinder, dissolving lime, phosphate and carbendazim in water, evenly stirring the mixture, adding other components, composting the mixture, carrying out fermentation, adjusting pH of the mixture to 5-5.4 with lime powder, packaging the mixture in polyethylene bags, and cultivating the mushroom by adding nutrition liquid comprising 0.3-0.4 wt.% of urea, 0.5-1 wt.% of sucrose and 0.3-0.5 wt.% of potassium dihydrogen phosphate.
NOVELTY - Composite microorganism fertilizer comprises 10-50 wt.% of three strains of Bacillus licheniformis, 10-20 wt.% of corn straw, 10-20 wt.% of wheat straw, 2-3 wt.% of chicken manure, 1-2 wt.% of sheep manure, 2-5 wt.% of pig manure, 10-20 wt.% of fruit residue and fruit water precipitate, 2-5 wt.% of humic acid, 1-2 wt.% of cotton seed cake, 2-8 wt.% of amino acid and 5-45 wt.% of sum of nitrogen, phosphorus pentoxide and potassium pentoxide.    USE - The composite microorganism fertilizer is useful for inhibiting bacterial and fungal root rots and scabs in plant.    ADVANTAGE - The composite microorganism fertilizer increases the soil fertility.
NOVELTY - Method for preparing biological fertilizer involves (a) mixing 92.3-99.4 wt.% kelp residues, 0.5-5.2 wt.% sucrose, and 0.1-2.5 wt.% potassium nitrate, (b) inoculating Bacillus amyloliquefaciens into mixture, (c) fermenting mixture at 30-40 degrees C for 10-20 days, and (d) drying and crushing fermented product.    USE - The method is useful for preparing biological fertilizer (claimed).    ADVANTAGE - The method enables to prepare product which promotes growth of plants, improves quality of plants, and protects plants from pathogenic fungi.
NOVELTY - Extraction of sodium p-toluenesulfonate from tiamulin-synthesis wastewater involves adjusting pH of ammoniated tiamulin-synthesis wastewater to 7-8, concentrating under reduced pressure to 75-80 vol.%, cooling to 0-4 degrees C, stirring for 1-2 hours, filtering, mixing filter cake with pure water, adding activated carbon, heating to 80 degrees C, stirring for 30-60 minutes, filtering, cooling obtained filtrate to 2-4 degrees C, recrystallizing, precipitating sodium p-toluenesulfonate, and filtering.    USE - Extraction of sodium p-toluenesulfonate from tiamulin-synthesis wastewater (claimed).    ADVANTAGE - The method enables simple, economical and environmentally-friendly extraction of sodium p-toluenesulfonate from tiamulin-synthesis wastewater by reducing wastewater chemical oxygen demand by 50-60% and wastewater treatment pressure. The amount of sodium p-toluenesulfonate recovered is 310 kg/m3.
NOVELTY - Synthesis of amlodipine free base involves hydrolyzing phthaloyl amlodipine as a raw material using sodium hydroxide aqueous solution at room temperature.    USE - Synthesis of amlodipine free base (claimed).    ADVANTAGE - The method enables economical synthesis of amlodipine free base with high yield, by environmentally-friendly process.
NOVELTY - Synthesis of sulbactam acid comprises carrying out diazotization bromination reaction by continuously adding 6-aminopenicillanic acid in 5-8% aqueous sulfuric acid, 13-15% aqueous hydrobromic acid, and 5-8% aqueous hydrochloric acid; carrying out oxidation reaction; and carrying out reduction reaction.    USE - Method for the synthesis of sulbactam acid (claimed).    ADVANTAGE - The 6-aminopenicillanic acid is added dropwise to avoid dust pollution and improve working environment for site personnel. The method achieves a yield of more than 70%, and HPLC purity of greater than or equal to 99.7%.
NOVELTY - Heterocycle-catalyzed electrochemical reduction of aldehyde compound involves adding aldehyde compound into a solution of an electrolyte and a heterocycle catalyst in a divided electrochemical cell, cathode-reducing aldehyde compound to alcohol(s) and separating alcohol from the solution. Different alcohols are obtained by adjusting cathode material, electrolyte, heterocycle catalyst, pH value and electrical potential. The divided electrochemical cell comprises an anode in a cell compartment (a) and a cathode in cell compartment (b).    USE - Heterocycle-catalyzed electrochemical reduction of aldehyde compound to alcohol e.g. isopropanol, butanol and pentanol used for preparing light alcohol fuel and solvent.    ADVANTAGE - The method efficiently and economically reduces aldehyde compound to alcohol with yield of 50% or more at atmospheric pressure and ambient temperature using water as solvent and pH of more than 4, in short period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for heterocycle-catalyzed hydrodimerization of carbonyl-containing molecules, involves introducing carbonyl-containing molecules into a solution of an electrolyte and a heterocycle catalyst in a divided electrochemical cell, cathode-hydrodimerizing carbonyl-containing molecules into organic product and separating said organic products from the solution.
NOVELTY - Converting cellulose into simple sugars comprises contacting cellulose, in the presence of water, with a compound effective to catalytically cleave ether bonds of the cellulose to give at least one simple sugar. The compound is vitamins, compounds with at least one ylide functionality, porphyrins, flavins and/or pyridoxal-containing molecules.    USE - The process is useful for converting cellulose into simple sugars (claimed) such as free glucose, which is used for producing biofuel such as ethanol.    ADVANTAGE - The process is capable of economically converting cellulose into simple sugars in a continuous and large-scale manner.
NOVELTY - Use of at least one glycosidase of class EC 3.2.1.21, EC 3.2.1.4, EC 3.2.1.7, and/or EC 3.2.1.80 for hydrolyzing at least one glycoside bond in at least one substrate comprising acylated steryl glycoside compound (I), is claimed.    USE - The glycosidase is useful for hydrolyzing at least one acylated steryl glycoside and/or at least one steryl in biofuel, oil and/or fat, and for preparing oil, fat or biofuel (all claimed).    ADVANTAGE - The glycosidase allows simple and cost efficient removal of acylated and non-acylated steryl glycosides from vegetable oils, for the effective production of biofuels with long storage stability.    DETAILED DESCRIPTION - Use of at least one glycosidase of class EC 3.2.1.21, EC 3.2.1.4, EC 3.2.1.7, and/or EC 3.2.1.80 for hydrolyzing at least one glycoside bond in at least one substrate comprising acylated steryl glycoside compound of formula (R1-CO-O-(CmHnOy)y-R2) (I), is claimed.    R1 = a saturated or non-saturated 1-30C alkyl;    R2 = a sterol moiety;    m = 5-7;    n = 9-14;    x = 5-7; and    y = 1-5.    An INDEPENDENT CLAIM is included for a method for hydrolyzing at least one acylated steryl glycoside and/or at least one steryl glycoside in biofuel, oil and/or fat by mixing the glycosidase with the biofuel, oil or fat.
NOVELTY - A gas analyzer has a conduit for gas sample, hollow core photonic crystal fiber(s) (HC-PCF) having distal portion and proximal portion which is in contact with the gas sample in the conduit, a laser positioned to strike the gas sample in the conduit and opposite the HC-PCF, and a Raman spectra detector connected to the proximal portion of hollow core photonic crystal fibers. Raman spectrum is generated when the laser strikes the gas sample that is detected by the Raman spectra detector without regard to the level of attenuation.    USE - Gas analyzer is used for detecting gas e.g. nitrogen, hydrogen, oxygen, carbon dioxide, methane and/or water vapor (all claimed) in soil gas analysis.    ADVANTAGE - The gas analyzer precisely and accurately detects the concentration of gas when used in soil gas analysis.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of detecting gas using gas analyzer.
NOVELTY - Liquid sugar is manufactured by performing carbonization process of biomass containing cellulose at predetermined temperature of 150-500 degrees C and producing carbonized material, contacting carbonized material and polysaccharide and hydrolyzing (S414), and producing liquid sugar containing monosaccharide. The method hydrolyzes biomass-derived polysaccharide containing cellulose and produces liquid sugar.    USE - Manufacture of liquid sugar for manufacture of biomass-derived material (claimed) e.g. ethanol.    ADVANTAGE - The manufacturing method has low environmental impact and is inexpensive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of biomass-derived material which involves using biomass-derived polysaccharide containing cellulose as starting material.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the biomass-derived material manufacturing method. (Drawing includes non-English language text).    Crushing process (S410)    Mixing process (S412)    Hydrolysis process (S414)    Isolation process (S416)    Ethanol manufacturing process (S418)
NOVELTY - Preparing highly active organic fertilizer comprises taking seaweed as raw material, subjecting the seaweed to enzymolytic fermentation using actinomycetes for the first time at 35-42 degrees C for 48-72 hours and then fermenting for the second time using Bacillus at 35-42 degrees C for 48-72 hours, inoculating the fermented product, and filtering the inoculated product to obtain a fermentation liquid and then concentrating.    USE - The method is useful for preparing highly active organic fertilizer (claimed), which is useful for cultivating cotton, tobacco and mulberry.    ADVANTAGE - The method is capable of economically preparing the highly active organic fertilizer with an organic matter content of more than 95 g/l, alginic acid content of more than 20 g/l, and copper, zinc, molybdenum and boron content of more than 4 g/l, thus increasing the yield of the plants.    DETAILED DESCRIPTION - AN INDEPENDENT CLAIM is included for the highly active organic fertilizer prepared by the method.
NOVELTY - A monosaccharide concentrate is manufactured by decomposing biomass which contains monosaccharide to obtain saccharification process liquid and carrying out forward osmosis process of saccharification process liquid.    USE - Manufacture of monosaccharide concentrate (claimed) used as raw material for manufacturing ethanol and lactic acid.    ADVANTAGE - Monosaccharide concentrate can be efficiently and intensively concentrated from saccharification process liquid obtained by decomposing biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the permeate flow rate when carrying out forward osmosis process of artificial saccharified liquid and time-dependent change of xylose concentration. (Drawing includes non-English language text).
NOVELTY - Biomass feedstock which is not directly in contact with a catalyst arranged inside a reactor is thermally decomposed, within the reactor, and the thermally decomposed organic substance is modified according to the catalyst to obtain a hydrocarbon.    USE - Manufacture of hydrocarbon used as fuel e.g. gasoline.    ADVANTAGE - The method enables manufacture of hydrocarbon which does not contain oxygen, efficiently and with high yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a structure of the reactor used in the manufacture of hydrocarbon. (Drawing includes non-English language text)
NOVELTY - Culturing rice seed involves degrading earthworm manure. The degraded earthworm manure is sieved, and then mixed with cow excrement uniformly, where the ratio of the earthworm manure and fine soil is 1:1. The obtained fine soil is sieved, and then fresh chicken manure is spread at the bottom of seedling. Water is sprayed on the mixture, and then rice seeds are cultured.    USE - Method for culturing rice seed (claimed).    ADVANTAGE - The method enables to culture rice that is cost-effective and environment-friendly, and ensures improved fertility, growing property, absorbing ability, survival rate and quality of rice seed.
NOVELTY - Reducing viscosity of a heavy oil involves adding cashew nut shell liquid (CNSL) to the heavy oil in an amount sufficient to reduce viscosity of the heavy oil; or reducing viscosity of a heavy oil involves adding at least one of anacardic acid, cardanol and cardol to the heavy oil in an amount sufficient to reduce viscosity of the heavy oil.    USE - The method is useful for reducing viscosity of heavy oil. The composition is useful as a viscosity reducing agent, an enhanced oil recovery agent, a heavy oil upgrading agent, a wellbore cleaning agent, and/or a cleaning agent for asphaltene-containing materials (all claimed).    ADVANTAGE - The decrease in viscosity of heavy oils increases the ability of the heavy oil mixture to be piped, transported, stored and used. The CNSL and compositions incorporating CNSL provide a safer, renewable, cost effective, green viscosity reducing agent for extraction of oils.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a composition comprising a heavy oil and CNSL, the CNSL present in an amount sufficient to reduce viscosity of the heavy oil; or a composition comprising a heavy oil and at least one of anacardic acid, cardanol and cardol, the at least one of anacardic acid, cardanol and cardol present in an amount sufficient to reduce viscosity of the heavy oil; or a composition comprising at least one of anacardic acid, cardanol and cardol, and at least one of a surfactant, a co-solvent, and water; and    (2) a biofuel composition comprising the composition; a biofuel composition containing CNSL and a heavy oil; a biofuel composition containing at least one of anacardic acid, cardanol and cardol, and a heavy oil; or a biofuel composition containing at least one of CNSL, anacardic acid, cardanol and cardol, and a heavy oil.
NOVELTY - Substrate comprises mouse excrement.    USE - The substrate is useful for cultivating bamboo fungus (claimed).    ADVANTAGE - The substrate is rich in nutrients required for bamboo fungus, provides high economic benefits to farmer, is abundant in amino acid, trace elements, vitamins, saccharides and carbohydrates, and produces high quality bamboo fungus.
NOVELTY - Preparing selenium rich organic fertilizer, involves collecting residue obtained from mushroom cultivation, drying the residue, crushing dried residue, mixing bacterial inoculum, adding pig manure and exogenous sodium selenite, performing fermentation, adding lime, continuing fermentation, increasing temperature, performing fermentation, piling obtained product into heap, maturing heap, drying matured product, crushing dried material, sifting crushed material, and granulating sifted product to obtain granules.    USE - The method is useful for preparing selenium rich organic fertilizer (claimed).    ADVANTAGE - The method provides high quality fertilizer, and is cost-effective, simple, easy to perform and economically beneficial.    DETAILED DESCRIPTION - Method for preparing selenium rich organic fertilizer, involves collecting residue obtained from mushroom cultivation, drying the residue, crushing dried residue to obtain product having particle size of 3-5 mm, mixing bacterial inoculum with the product to obtain product having moisture content of 50-60%, adding mixture to fermentation tank, adding pig manure and exogenous sodium selenite to the tank, performing fermentation at 25-30 degrees C under carbon-nitrogen ratio of 0.1-1%, controlling moisture content at 65-70%, adding 1-2% lime to adjust pH at 6.5-8.5, continuing fermentation for 4 days, increasing the temperature to 60-65 degrees C, performing fermentation for 1-12 days, piling obtained product into a heap of height 2-2.5 m, maturing the heap for 1-15 days, drying matured product, crushing dried material, sifting crushed material, and granulating sifted product to obtain granules.
NOVELTY - Method for preparing compound fertilizer, involves (a) crushing magnesium oxide and calcium oxide, (b) crushing e.g. zinc oxide, manganese oxide, and boric acid, (c) adding cellulase, and protease to water, (d) filtering mycelium residues, and spraying mixture obtained in the step (c), and performing enzymolysis, (e) mixing the crushed powder obtained in the steps (a) and (b), and adding enzymolyzed product to mixture, drying and crushing mixture and adding e.g. potash fertilizer, and (f) granulating, and packing obtained product.    USE - The method is useful for preparing compound fertilizer (claimed).    ADVANTAGE - The method enables to prepare compound fertilizer simply and cost-effectively.    DETAILED DESCRIPTION - Method for preparing compound Fertilizer, involves (a) crushing magnesium oxide and calcium oxide and sieving using sieve of 60-80 mesh size, (b) crushing zinc oxide, iron oxide, copper oxide, manganese oxide, and boric acid, and sieving using sieve of 60-80 mesh size, (c) adding cellulase, and protease in a mass ratio of 1-3:1, adding water to mixture in a mass ratio of 1:50-100 at 30-45 degrees C, (d) filtering 60-70% mycelium residues, and spraying mixture obtained in the step (c), and performing enzymolysis at 25-45 degrees C for 12-72 hours, (e) mixing the crushed powder obtained in the steps (a) and (b) in a mass ratio of 2-5:1, adding enzymolyzed product to mixture in a ratio of 0.1-0.5:10, (f) drying mixture at 80 degrees C, and crushing dried product, and (g) adding nitrogen fertilizer, phosphate fertilizer, and potash fertilizer to chitin, adding mixture to crushed product, stirring mixture, and granulating, sieving and packing obtained product.
NOVELTY - Separation and purification of m-cresol involves adding mixed cresol, urea, toluene and liquid paraffin to a reactor, mixing, forming mixed solvent, thermally-heating resultant product at 65-90 degrees C, heat-preserving at 65-90 degrees C for 1-2 hours, cooling to 40-60 degrees C, crystallizing by cooling to 0-20 degrees C for 1-2 hours, filtering, obtaining solid complex and filtrate (A), adding solid complex to ether solvent at 10-60 degrees C, mixing, subjecting to complex reaction for 0.5-3 hours, filtering, obtaining urea and filtrate (B), vacuum-distilling filtrate (B), and obtaining m-cresol and ether solvent.    USE - Separation and purification of m-cresol (claimed).    ADVANTAGE - The method enables simple and environmentally-friendly separation and purification of m-cresol with high recovery rate, and low solvent consumption and energy consumption, enabling recycle of resources, without producing waste. The separated m-cresol has high purity.
NOVELTY - Preparation of 2-metyhyl-5,7-dihydroxy chromone comprises taking phloroglucinol as raw material, dissolving in organic solvent at - 15-10 degrees C, stirring, adding Lewis acid, dropping acetyl chloride, stir-reacting for 2-5 hours to get 2,4,6-trimethyl hydroxyacetophenone phloroglucin acylation reaction intermediate product, adding anhydrous sodium acetate and dropping acetyl chloride, heating and refluxing, reacting for 1-4 hours, performing cyclization reaction to get 2-methyl-3-acetyl-5,7-diacetoxy chromone; and reacting with alkali for 0.5-3 hours, and adjusting pH using hydrochloric acid.    USE - Method for preparing 2-metyhyl-5,7-dihydroxy chromone (claimed).    ADVANTAGE - The method has easy to obtain raw materials, simple reaction step, low cost, high yield and mild reaction condition. It is fit for industrial production and environmental protection.    DETAILED DESCRIPTION - Preparation of 2-metyhyl-5,7-dihydroxy chromone comprises taking phloroglucinol as raw material, dissolving in organic solvent at - 15-10 degrees C, stirring, adding Lewis acid, dropping acetyl chloride, stir-reacting for 2-5 hours to get 2,4,6-trimethyl hydroxyacetophenone phloroglucin acylation reaction intermediate product, adding anhydrous sodium acetate and dropping acetyl chloride, heating and refluxing, reacting for 1-4 hours, performing cyclization reaction to get 2-methyl-3-acetyl-5,7-diacetoxy chromone; and reacting with alkali for 0.5-3 hours, and adjusting pH using hydrochloric acid to neutral. The mole ratio of phloroglucinol and acetyl chloride is 1:1-1:1.2. The mole ratio of phloroglucinol and anhydrous sodium acetate is 1:2-1:5.
NOVELTY - A phosphorus compound, a zeolite, clay and an aqueous silica precursor are combined in a mix vessel, to form aqueous slurry. The aqueous slurry is spray dried, to form spray dried particles. The spray dried particles are calcined, to form a biomass conversion catalyst.    USE - Preparation of biomass conversion catalyst (claimed) is used in thermo-catalytic conversion of biomass to bio-oil.    ADVANTAGE - The method enables preparation of biomass conversion catalyst having excellent zeolite accessibility, deoxygenation activity in biomass conversion and organic acid resistance, and tunable coke selectivity.
NOVELTY - Processing of hydrocarbon feedstream involves contacting hydrocarbon feedstream with catalyst comprising interstitial metal hydride in presence of hydrogen at 150 degrees C or more and 200 psig or more, and obtaining an upgraded reaction product stream. The interstitial metal hydride comprises least a chemical element (A) chosen from groups 3-11 (including lanthanide, atomic numbers 58-71), and at least a chemical element (B) chosen from groups 13-15 of periodic table.    USE - Processing of hydrocarbon feedstream containing biofuel (claimed) e.g. diesel, kerosene, gasoline, gasoline fraction, biodiesel, biojet fuel and biogasoline.    ADVANTAGE - The hydrocarbon feedstream is economically and efficiently processed. The radiofrequency or microwave energy improves hydroprocessing efficiency. The surface area of active catalytic elements is increased to increase the process reaction rate. The metallic or metal oxide catalytic sites are dispersed to prevent arcing in presence of strong electric or magnetic field which is used to expedite catalytic action. The microwave energy is modulated and controlled to optimize the reaction exchange of the monatomic hydrogen from the interstitial metal hydride.
NOVELTY - Mixed transition metal iron (II/III) catalyst for catalyzing carbon dioxide (CO2) oxidation of carbon or an organic compound, is new.    USE - The mixed transition metal iron (II/III) catalyst is useful for: catalyzing carbon dioxide oxidation of carbon or an organic compound; converting CO2 and carbon to carbon monoxide; converting a hydrocarbon to an oxygenated hydrocarbon; and oxidative dehydrogenation of a first hydrocarbon, preferably butane, ethane, methane or propane (all claimed). The catalyst is useful for carbon monoxide hydrogenation reactions such as Fischer-Tropsch reaction, CO2 utilization for carbon monoxide production, char gasification, and selective oxidations of hydrocarbon reductants, oxidative methane coupling, oxidative dehydrogenation of light alkanes for olefin production, epoxidation of olefins to prepare alkene-oxides, and the preparation of methanol and dimethyl ether synthesis.    ADVANTAGE - The mixed transition metal iron (II/III) catalyst exhibits high reactivity, mobility and stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) converting CO2 and carbon to carbon monoxide, comprising contacting the mixed transition metal iron (II/III) catalyst with a CO2 feed stream under temperature and pressure conditions;    (2) converting a hydrocarbon to an oxygenated hydrocarbon, comprising contacting the mixed transition iron (II/III) metal catalyst with the hydrocarbon and the CO2 feed stream under conditions to form the oxygenated hydrocarbon; and    (3) oxidative dehydrogenation of a first hydrocarbon, comprising contacting the mixed transition iron (II/III) metal catalyst with the first hydrocarbon and the CO2 feed stream under conditions to form a dehydrogenated second hydrocarbon.
NOVELTY - Co-production of ethanol and renewable diesel fuel comprises: distilling ethanol-containing beer within distillation apparatus of ethanol plant to produce ethanol-rich overhead stream (22) and solids-containing, whole stillage stream; recovering corn oil product from ethanol plant (12), and directing stream of corn oil product to renewable diesel plant (14); and reacting corn oil product stream received from ethanol plant with hydrogen in reaction system of renewable diesel plant to produce mixture of reaction products comprising renewable diesel fuel, fuel gas, and naphtha.    USE - The integrated process is useful for co-production of ethanol and renewable diesel fuel.    ADVANTAGE - The process is cost effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an integrated facility for the co-production of ethanol and renewable diesel fuel comprising an ethanol plant comprising distillation apparatus (18) operable to separate an ethanol containing beer into an ethanol-rich overhead stream and a solids-containing, whole stillage stream, and corn oil recovery apparatus operable to produce a corn oil stream, and a renewable diesel plant comprising a reaction system operably coupled with the corn oil recovery apparatus to receive at least a portion of the corn oil stream and produce a reaction product stream comprising renewable diesel fuel, naphtha, and fuel gas.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of integrated ethanol and renewable diesel production facility.    Renewable diesel production facility (10)    Ethanol plant (12)    Renewable diesel plant (14)    Distillation apparatus (18)    Overhead stream (22)
NOVELTY - Filter device (8) for filtering fuel gas produced by gasification of biomass, comprises a filter body comprising a filter medium which is formed as a fabric.    USE - The filter device is useful for filtering fuel gas produced by gasification of biomass (claimed).    ADVANTAGE - The filter device exhibits a longer service life.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a biomass gasification plant (1), preferably wood gasification plant, comprising the filter device; and    (2) exchanging the filter medium in the filter device comprising slicing the second support material and/or the protective material and the exchanging filter medium.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation a wood gasification plant.    Biomass gasification plant (1)    Gasifier (2)    Filter (3)    Filter housing (5)    Filter device (8)
NOVELTY - Phosphine compound (I) and halogenated carbon compound (II) are reacted to obtain phosphine derivative (III). Compound (III) is reacted with 4-((4-methylpiperazin-1-yl)methyl)benzoic acid hydrochloride to obtain phosphorus-containing 4-((4-methylpiperazin-1-yl)methyl)benzoic acid hydrochloride (V). Compound (V) is reacted with N-(5-amino-2-methylphenyl)-4-(3-pyridyl)-2-pyridinamine (VI), to obtain N-5-(4-(4-methyl-piperazino-methyl)benzolamido)-2-methylphenyl-4-(3-pyridyl)-2-pyrimidinamine (VII).    USE - Manufacture of N-5-(4-(4-methyl-piperazino-methyl)benzolamido)-2-methylphenyl-4-(3-pyridyl)-2-pyrimidinamine (claimed).    ADVANTAGE - The method enables simple and economical manufacture of N-5-(4-(4-methyl-piperazino-methyl)benzolamido)-2-methylphenyl-4-(3-pyridyl)-2-pyrimidinamine having high purity with high productivity in a short period of time by environmentally-friendly process.    DETAILED DESCRIPTION - Phosphine compound of formula: P(R1)(R2)(R3) (I) and halogenated carbon compound of formula: Cn(X1)2m+2 (II) are reacted to obtain phosphine derivative of formula (III). Compound (III) is reacted with 4-((4-methylpiperazin-1-yl)methyl)benzoic acid hydrochloride of formula (IV) to obtain phosphorus-containing 4-((4-methylpiperazin-1-yl)methyl)benzoic acid hydrochloride of formula (V). Compound (V) is reacted with N-(5-amino-2-methylphenyl)-4-(3-pyridyl)-2-pyridinamine of formula (VI), to obtain N-5-(4-(4-methyl-piperazino-methyl)benzolamido)-2-methylphenyl-4-(3-pyridyl)-2-pyrimidinamine of formula (VII).    R1-R3=(1-5C)alkyl, (2-5C)alkenyl, (6-12C)aryl or (1-5C)alkyl(6-12C)aryl;    X1=halo;    m=1-3;and    n=0-2.
NOVELTY - Silk fabric deodorant antibacterial agent comprises 50-80 wt.% of titanium, 10-15 wt.% of propylene glycol methyl ether acetate, 5-10 wt.% of organic polysiloxane, 2-10 wt.% of lecithin, 10-30 wt.% of propylene glycol, 3-10 wt.% of hydroxyethyl cellulose, 2-5 wt.% of alginate, 10-20 wt.% of sodium stearate, 2-3 wt.% of ammonia, and 20-30 wt.% of dioctadecyl dimethyl ammonium chloride.    USE - Silk fabric deodorant antibacterial agent.    ADVANTAGE - The silk fabric deodorant antibacterial agent is non-toxic, and can be easily prepared in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the silk fabric deodorant antibacterial agent, comprising mixing titanium oxide, organosiloxane, propylene glycol, sodium stearate and sodium alginate, adding propylene glycol methyl ether acetate, lecithin, dioctadecyl dimethyl ammonium chloride and hydroxyethyl cellulose to the mixture, grinding the mixture at a speed of 2000-5000 rotations per minute for 60 minutes to obtain the mixture, and adding an aqueous ammonia to the mixture to adjust pH value to 6-7.
NOVELTY - Biological fertilizer comprises 35-50 wt.% organic matter, 35-50 wt.% chicken manure, 3-5 wt.% calcium, 1-2 wt.% magnesium, 1-2 wt.% phosphorus, and 5-10 wt.% microbial inoculum. The organic matter comprises rice husk powder and straw powder. The microbial inoculum comprises Bacillus subtilis, yeast, photosynthetic bacteria and actinomycetes.    USE - The biological fertilizer is useful for rice (claimed).    ADVANTAGE - The biological fertilizer is rich in nutrients.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the biological fertilizer, which involves adding organic matter, chicken manure, calcium, magnesium, and phosphate, adding microbial inoculum to mixture, and performing fermentation at 55-65 degrees C for 6-7 days.
NOVELTY - Nutritional liquid comprises 1-1.5 wt.% water-soluble chitosan oligosaccharide, 8-10 wt.% starch-based superabsorbent, and bean sprout filtrate (remainder), where the bean sprout filtrate is prepared by squeezing bean sprout and filtering squeezed product.    USE - The nutritional liquid is useful for improving survival rate of graft (claimed).    ADVANTAGE - The nutritional liquid is cost-effective, and convenient to use, and can be prepared simply in an environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the nutritional liquid, which involves adding the bean sprout filtrate to remaining raw materials, and uniformly mixing obtained mixture.
NOVELTY - 2-Ethoxy-5-(4-methyl-piperazin-1-yl-sulfonyl) benzoic acid and thionyl chloride are reacted, and the reaction solution is aged. The aged solution and 4-amino-1-methyl-3-n-propyl-1H-pyrazole-5-carboxamide are acylated, resultant reaction solution is washed, organic phase is dried, filtered, solvent is evaporated from the filtrate, and obtained solid is dissolved and aged. The resultant solution is cyclized, obtained mixture is dissolved in water, crystallized, resultant mixture is filtered, dried, and obtained crude sildenafil is recrystallized, to obtain sildenafil.    USE - Preparation of sildenafil used for synthesizing drug.    ADVANTAGE - The method enables economical preparation of sildenafil without distilling under reduced pressure to remove excess thionyl chloride, by simple and environmentally-friendly process.    DETAILED DESCRIPTION - 2-Ethoxy-5-(4-methyl-piperazin-1-yl-sulfonyl) benzoic acid and thionyl chloride are reacted in presence of catalyst, intermediate compound (A) is generated, and resultant reaction solution is aged. The aged solution and 4-amino-1-methyl-3-n-propyl-1H-pyrazole-5-carboxamide are acylated using acid-binding agent, and intermediate compound (B) is generated. The resultant reaction solution is washed with water, organic phase is dried, filtered, solvent is evaporated, and obtained solid is dissolved and aged. The resultant solution is cyclized in presence of specific base, and solvent is evaporated from the reaction mixture under reduced pressure. The obtained mixture is dissolved in water, dilute hydrochloric acid is added to adjust pH to 7, crystallized, resultant mixture is filtered, dried, and obtained crude sildenafil is recrystallized, to obtain sildenafil.
NOVELTY - A composition comprises a mixture (A) containing fatty acid methyl ester (a) and fatty acid alkylester (b) of at least one 2-8C alkyl alcohol, and has cloud point of -4 degrees C to -12 degrees C. The mixture (A) has cloud point less than mixture containing only fatty acid methyl ester.    USE - Composition used in compression ignition engine e.g. diesel engine.    ADVANTAGE - The composition has high purity.    DESCRIPTION OF DRAWING(S) - The drawing shows the flow sheet explaining preparation of biodiesel composition.
NOVELTY - The invention relates to a process for preparing an oil having a high content of polyunsaturated fatty acids combined as triglycerides and a Diesel biofuel. According to the invention, the process consists in dehydrating the fish oil up to a maximum water content of 0.05%, treating it with 0.9...1.15% alkaline catalyst dissolved in 19.15...32.1% methanol or ethanol, the reaction mass being then maintained at the temperature of 65...90 degrees C for 60...90 min while stirring, raw glycerine being separated by settling from the raw alkyl esters, wherefrom alcohol is separated by distillation, the alkyl esters are further successively separated by rectification to obtain the distillate 1 and the residue 1, then the distillate 2 and the residue 2, the distillate 1 is mixed with the distillate 2 to form a Diesel biofuel, while the residue 2 is treated with glycerine at a molar ratio of 1:2.3...2.4, with 0.85%...1.05% alkaline catalyst, at a temperature of 125...135 degrees C, for 6...8 h, at a pressure of 25...30 mbar, wherefrom an alcohol condensate is separated by distillation, the resulting raw triglycerides being washed with alcoholic solutions, water and volatile matter being eliminated by distillation to finally result in an oil having a high content of unsaturated fatty acids which is treated with activated carbon and filtered.
NOVELTY - Preparing a liquefied fertilizer comprises pretreating grass wastes with an alkaline solution and then fermenting.    USE - The method is useful for preparing a liquefied fertilizer (claimed), which is useful for promoting plant growth.    ADVANTAGE - The method is capable of effectively preparing the liquefied fertilizer in a rapid and environmentally-friendly manner.
NOVELTY - Processing biological treatment of circulation cooling water comprises (i) placing a filler bed in a circulation cooling water pool, and setting the circulation cooling water pool with a circulation water pump; (ii) adding yeast, purple non-sulfur bacteria, acetic acid bacteria, and Bacillus strain into the cooling water pool in any proportion, and monthly adding 0.05-1% bacterial liquid to maintain water; and (iii) setting a discharge pump in the circulation cooling water pool, and then regularly discharging sludge.    USE - The method is useful for processing biological treatment of circulation cooling water (claimed).    ADVANTAGE - The method: increases circulation cooling water concentration; reduces the supply of water to the circulation cooling water system; and is quick, simple and environmentally friendly.    DETAILED DESCRIPTION - Processing biological treatment of circulation cooling water comprises (i) placing a filler bed in a circulation cooling water pool, and setting the circulation cooling water pool with a circulation water pump; (ii) adding yeast containing greater than or equal to 1x 106 colony forming units (CFU)/ml, purple non-sulfur bacteria containing bacterial concentration of greater than or equal to 1x 105 CFU/ml, acetic acid bacteria containing bacterial concentration of greater than or equal to 1x 109 CFU/ml, and Bacillus strain containing bacterial concentration of greater than or equal to 1x 109 CFU/ml into the cooling water pool in any proportion, and monthly adding 0.05-1% bacterial liquid to maintain water; and (iii) setting a discharge pump in the circulation cooling water pool, and then regularly discharging sludge.
NOVELTY - Sustained-release fertilizer comprises 6-10 pts. wt. dicalcium phosphate, 7-11 pts. wt. urea phosphate, 6-14 pts. wt. sulfate-potassium-magnesium fertilizer, 3-5 pts. wt. Bacillus stearothermophilus, 1.2-3 pts. wt. straw fermentation agent, 1.4-2.8 pts. wt. corn pole, 5.5-9 pts. wt. sustained-release urea, 3.2-6 pts. wt. magnesium sulfate, 1.5-7 pts. wt. borax, 2.2-3.8 pts. wt. coating agent, 3-6 pts. wt. organic nitrogen, 2.4-5.8 pts. wt. silicon dioxide, 1.5-3.6 pts. wt. egg white, 0.6-2.4 pts. wt. bamboo shoot shell and 2.6-4.8 pts. wt. peanut cake.    USE - Used as sustained-release fertilizer.    ADVANTAGE - The fertilizer provides long-term nutritional components for crop, and increases disease resistance and drought resistance ability of crops.
NOVELTY - Preparing liquid soil modifying agent using furfural residue and furfural wastewater, comprises sequentially adding 22.9-40.1 wt.% alkali sludge, 33.3-53.3 wt.% furfural wastewater, 12-15 wt.% urea, 3.8-9.6 wt.% monoammonium phosphate and 4-6 wt.% potassium sulfate into a reaction kettle, stirring and reacting at 40-50 degrees C for 1-2 hours.    USE - The method is useful for preparing liquid soil modifying agent using furfural residue and furfural wastewater (claimed).    ADVANTAGE - The agent improves soil physicochemical property, repairs polluted soil, increases nutrient utilization rate, promotes plant growth, increase yield and can be used in saline, arid and semi-arid lands.
NOVELTY - Slurry bed and fixed bed combined methanation comprises dividing methanation feed gas into two parts of feed gas, mixing a part of the feed gas with water vapor and conveying into a slurry bed methanation system, reacting under methanation catalyst, where the feed gas is natural gas and/or coke-oven gas, passing the gas from slurry bed methanation system outlet to a gas-liquid separator after passing via a heat exchanger, separating condensed water, feeding another part of the feed gas into a fixed bed methanation system for methanation under a catalyst.    USE - The method is useful for slurry bed and fixed bed combined methanation (claimed).    ADVANTAGE - The method: saves energy in comparison with conventional slurry bed methanation process; is simple and convenient; and has temperature control, load distribution and heat balance in comparison with conventional fixed bed methanation process.    DETAILED DESCRIPTION - Slurry bed and fixed bed combined methanation comprises (a) dividing methanation feed gas into two parts of feed gas, mixing a part of the feed gas with water vapor and conveying into a slurry bed methanation system, whose bottom is set with a gas distributor, allowing to enter methanation catalyst into suspension state slurry bed, carrying out methanation reaction, where the feed gas is natural gas and/or coke-oven gas, and (b) passing the gas from the outlet of the slurry bed methanation system to a gas-liquid separator after passing via a heat exchanger, separating condensed water, feeding another part of the feed gas into a fixed bed methanation system, carrying out chemical reaction under a fixed bed methanation catalyst.
NOVELTY - Microbial fertilizer comprises 3-8 pts. wt. potassium humate, 2.5-6 pts. wt. expansive soil, 3.5-7 pts. wt. nitrogen fertilizer, 1.2-3 pts. wt. zinc sulfate, 4-8 pts. wt. soybean meal, 1.3-4.6 pts. wt. Bacillus subtilis, 2.5-7 pts. wt. Bacillus mucilaginosus, 3.4-5.6 pts. wt. yeast, 0.6-2.3 pts. wt. weevil powder, 1.1-2.04 pts. wt. medicinal stone, 1.3-2.5 pts. wt. shell powder, 0.8-2.6 pts. wt. citric acid, 1.5-2.8 pts. wt. carboxymethyl cellulose and 2.1-3.3 pts. wt. effective microorganism (EM) agents.    USE - The fertilizer is useful: for vegetables (claimed), and in microbial decomposition of soil material, and for loosening soil.    ADVANTAGE - The fertilizer reduces the utilization rate of chemical fertilizers, and pollution; and improves the quality, and taste of vegetables.
NOVELTY - A bagasse water quality modifying agent preparing method involves adding lactic acid bacteria in sugarcane bagasse mixed fermentation broth. The fermented material is grinded into particles, naturally dried, urea, boric acid, potassium sulfate, tea bran, cassava are mixed to obtain mixed slag. The fermented material-2 is mixed with nano-ceramic, pulverized particles are mixed and heated, followed by stopping heating, stirring, cooling, to obtain reaction mixture, adding water to the mixture, heating with white phosphorus, phosphorus smoke system, and sealing for fermentation.    USE - Method for preparing bagasse water quality modifying agent.    ADVANTAGE - The method enables preparing modifying agent with increased survival rate of cultivation, reduced disease rate of cultivation, increased the mass cultivation, in simple, environment-friendly, and cost effective manner.    DETAILED DESCRIPTION - A bagasse water quality modifying agent preparing method involves adding lactic acid bacteria in sugarcane bagasse mixed fermentation broth at 55-60 degrees C for 5-8 days. The fermented material is grinded into particles with particle diameter of 500-600 mu m, naturally dried, urea, boric acid, potassium sulfate, tea bran, cassava are mixed to obtain mixed slag. The fermented material-2 is mixed with nano-ceramic with particle size of 600-800 mu m, pulverized particles are mixed and heated at room temperature of 50 degrees C for 20-30 minutes, allowed to stand at 50-65 degrees C for 5-10 minutes followed by stopping heating, stirring, cooling at room temperature, to obtain reaction mixture, adding water to the mixture, heating with white phosphorus, phosphorus smoke system, and sealing for fermentation.
NOVELTY - Binder comprises dextrin, rosin, alcohol, xanthan gum, apple pectin, guar gum, locust bean gum, sodium carbonate, starch, sodium silicate (instant), and corn syrup or pear syrup.    USE - The binder is useful for processing mushroom waste into carbon powder, which is useful for preparing incense dhoop (claimed).    ADVANTAGE - The binder has good binding ability, and enables to prepare incense dhoop having excellent fragrance.
NOVELTY - Binder comprises dextrin, rosin, alcohol, xanthan gum, apple pectin, guar gum, locust bean gum, sodium carbonate, starch, instant sodium silicate, and corn syrup or pear syrup.    USE - The binder is useful for processing mushroom waste into carbon powder, which is useful for preparing incense dhoop (claimed).    ADVANTAGE - The binder has good binding ability, and enables to prepare incense dhoop having excellent fragrance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the binder which involves (a) spraying starch in alcohol solution, mixing uniformly and allowing to stand at 60-70 degrees C for 2-3 hours, (b) crushing rosin and corn syrup or pear syrup into 80-100 mesh size at 0 plus minus 5 degrees C, (c) mixing dextrin, xanthan gum, guar gum, locust bean gum, sodium carbonate and instant sodium silicate uniformly to obtain a mixture, and (d) mixing products obtained in steps (a)-(c) with water, in weight ratio of 8:2, agitating mixture at 70 degrees C for 20 minutes, adding apple pectin and stirring for 10 minutes to obtain the product.
NOVELTY - A magnesium oxide utilizing method involves pulverized rice hull and drying in a drying tank to obtain a base, filtering magnesium oxide powder, mixing rice hull with the magnesium oxide powder and stirring, researching the rice hull through a pyrolysis experiment by using magnesium oxide catalytic followed by obtaining test data.    USE - Method for utilizing magnesium oxide that is used for catalytic pyrolysis of rice hull.    ADVANTAGE - The method enables reducing activated pyrolysis about 10.4% to ensure better pyrolysis process.
NOVELTY - A catalytic pyrolysis method involves utilizing ferric oxide powder, crushing rice hull and drying in oven, mixing ferric oxide powder and rice hull, stirring, followed by observing husk before and after catalytic pyrolysis, and analyzing the experimental data.    USE - Method for catalytic pyrolysis of rice hull.
NOVELTY - A heterotrophic nitrifying Penicillium sp. L1 strain, which is preserved in national microorganism strain preservation management committee normal microorganism centre with preservation CGMCC No. 8615, is new.    USE - Heterotrophic nitrifying Penicillium sp. L1 strain for removing ammonia nitrogen in sewage (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for culturing fungal mycelium, which involves inoculating Penicillium sp. L1 strain into the culture medium at 20-38 degrees C under oscillation of 150 rpm, where the culture medium comprises 3 g/l beef extract, 5 g/l sodium chloride, 10 g/l peptone, l000 ml distilled water, 0.5-5 g/l carbon source sucrose, 0.1-2 g/l nitrogen source ammonium sulfate and remaining component such as 0.1-2 g/l dipotassium phosphate, 1 g/l potassium chloride, 0.5 g/l magnesium sulfate heptahydrate, 0.01 g/l iron sulfate heptahydrate to pH of 7.0-7.4 at 121 degrees C for 20 minutes    (2) use of Penicillium sp. L1 strain for removing ammonia nitrogen in sewage.
NOVELTY - An oxidation catalyst comprises porphyrin derivative which is an element after 3rd period. The porphyrin derivative comprises element of group-13, group-14 or group-15, as main component.    USE - Oxidation catalyst is used for oxidative decomposing of water.    ADVANTAGE - The oxidation catalyst has high versatility with respect to oxidative decomposing of water using efficient light energy, and high reactivity with respect to electrochemical oxidation or chemical oxidation reaction, and is manufactured by easy and economical process.
NOVELTY - Agent comprises organic carrier and fermentation composition comprising microbial strains. The viable count of microbial strain is greater than or equal to 50 billion/g. The fermentation composition has fineness of greater than or equal to 70%, water content of less than or equal to 20%, and pH of 5.5-8.5. The fermentation composition comprises mixture of Bacillus subtilis, Saccharomyces cerevisiae, Aspergillus niger and Trichoderma longibrachiatum.    USE - The agent is useful for decomposing straw (claimed).    ADVANTAGE - The agent utilizes livestock excrement and agricultural waste and hence waste is changed into treasure. The method is environmentally-friendly, reduces bad smell of cultivation factory, and improves surrounding environment for plant cultivation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the agent, which involves (a) activating the B.subtilis, S.cerevisiae, A.niger and T.longibrachiatum, and expanding and mixing culture of B.subtilis, S.cerevisiae, A.niger and T.longibrachiatum to obtain fermentation composition, (b) uniformly mixing the livestock manure, wheat bran, bean cake and calcium carbonate powder in a weight ratio of 10:1-3:1-3:1-2 to obtain mixture, adding B.subtilis to the mixture, fermenting the mixture, adding fermentation enzymes to fermented product, and fermenting obtained mixture to obtain organic carrier, and (c) uniformly mixing the fermentation composition obtained in step (a) with the organic carrier obtained in step (b) to obtain product.
NOVELTY - The apparatus has a tank (6a) equipped with a screw that is formed in a base (6c) for transporting ice. The screw is arranged at a top end (6d) of the tank for transporting and dewatering protein, where the screw is pressed as the protein is transported and dried through a filter cloth cone (6e). A tube is arranged within the screw. Oblique guide rails allows liquid to be moved between inner and outer tubes, where the screw is driven by a bevel gear. An end of a heat exchanger is connected with a tray.    USE - Apparatus for producing sugar, ethanol and soy from leguminous crops e.g. soybean, cereal and oilseed rape.    ADVANTAGE - The apparatus reduces extraction of energy of shipments, and reduces environmental and climate problems at rainforest. The apparatus reduces excess leakage of nitrogen in rivers, lakes and oceans. The apparatus optimizes production of energy, protein and fiber and reduces cultivation time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus for producing sugar, ethanol and soy from leguminous crops.    Tank (6a)    Base (6c)    Top end (6d)    Filter cloth cone (6e)    Storage part (6f)
NOVELTY - An aquaculture activating liquid fermenting method involves adding 10 kg biogas slurry with 2.5 kg composite organic fertilizer, 0.3 kg aquatic animal-specific complex commercial probiotics and 1.25 kg carbon to obtain extraction liquid. The extraction liquid is fermented for 72 hours by adding 90 kg biogas and 5 g composite trace elements, followed by forming wrinkled purple-brown mold and pure, bright, pale yellow-green on the surface of the liquid to finish the whole fermentation process.    USE - Method for fermenting aquaculture activating liquid.    ADVANTAGE - The method enables fermenting aquaculture activating liquid with high efficiency, high microorganism activation rate, better effect of breaking down the culture water and sediment in bait, manure and other organic matter, and degradation of ammonia, nitrite, hydrogen sulfide and other harmful substances, in simple, easy and inexpensive manner.    DETAILED DESCRIPTION - An aquaculture activating liquid fermenting method involves adding 10 kg biogas slurry with 2.5 kg composite organic fertilizer, 0.3 kg aquatic animal-specific complex commercial probiotics and 1.25 kg carbon to obtain extraction liquid. The extraction liquid is fermented for 72 hours by adding 90 kg biogas and 5 g composite trace elements. The fermentation is carried out for 20 days, when the temperature is at 18-25 degrees C, and for 15 days, when the temperature is at 25-35 degrees C to obtain fermented liquid, followed by forming wrinkled purple-brown mold and pure, bright, pale yellow-green on the surface of the liquid to finish the whole fermentation process.
NOVELTY - A roflumilast is prepared by dissolving activating agent in solvent, adding 3-cyclopropylmethoxy-4-difluoromethoxybenzoic acid in solvent, adding alkali for catalyzing, and adding 3,5-dichloro-4-aminopyridine to obtain product.    USE - Method for preparing roflumilast (claimed).    ADVANTAGE - The method does not use thionyl chloride, thus avoiding environment pollution; does not use high temperature decompression distilling; and has high yield of 86-95%.
NOVELTY - Selenium-enriched fermentation liquid foliar fertilizer comprises 5.5 grams/liter sodium selenite or amino acid chelated selenium, and fermentation liquid.    USE - Selenium-enriched fermentation liquid foliar fertilizer used for promoting nutrition absorption or crops.    ADVANTAGE - The fermentation liquid increases selenium content in crops, and has high practicability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of selenium-enriched fermentation liquid comprising mixing raw materials, and fermenting for 15-40 days below normal temperature.
NOVELTY - An environmentally friendly diaper having a urine sensing function is disclosed. The environmentally friendly diaper comprises an outer cloth pocket and an inner pad located at inner surface of the outer cloth pocket and is characterized in that: at least two electrically conductive metal fibers individually mixed in and woven with fabric fibers of the inner pad and two metal buckles are fixed to a front end of the inner pad, the two metal buckles being respectively connected with the two metal fibers; one leading edge of the outer cloth pocket is provided with two fixing holes; one sensing device is packaged in a covering member and the sensing device is coupled to two metal buckles that extend out of the back of the covering member; the metal buckles of the inner pad are combined with the metal buckles of the covering member through the fixing holes of the outer cloth pocket; and the sensing device receives and processes a physical change amount sensed by the two metal fibers for conversion into a servo signal transmitted to a remote servo device.
NOVELTY - This invention provides a tar-self-removal biological fixed bed gasifier system which comprises a tar-self-removal biological fixed bed gasifier including a longitudinally arranged body consisting sequentially of, from bottom to top, a funnel-like tail ash section, a cylindrical reaction section, and a tar removal section. The top of the tar removal section is provided with a gas outlet; the bottom of the tail ash section is provided with a cinder hole; the tail ash section is provided at the lateral side with at least one gasified medium inlet; the upper side of the reaction section is provided with an inlet; a partition board is disposed between the reaction section and the tar removal section; a gas inlet is provided on the partition board for communication with the reaction section; the tar removal section is provided therein with a tar removal device which comprises a condensation cylinder as a cylindrical housing with two opened ends, wherein the lower opening of the cylindrical housing is connected with the gas inlet on the partition board; the wall of the tar removal section, the partition board and the housing of the tar removal device together form a space into which the gas cannot enter; a plurality of bundles formed by cooling tubes are disposed in the cylindrical housing.
NOVELTY - A 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.
NOVELTY - The apparatus has a magnetic separator combined with filters. A feed facility part is provided with a pulverizing device that pulverizes filtered waste of the filters. A dryer is utilized for delivering moisture to an anaerobic digestion facility part that is arranged in the feed facility part. A food rubbish separator is arranged in the feed facility part. A masking number dust collector removes foreign substance in an inner side of a masking gathering water tub. The masking gathering water tub is combined in the anaerobic digestion facility part and provided with an acid fermenter part.    USE - Organic waste resourcing apparatus.    ADVANTAGE - The apparatus effectively performs drying operation about the dehydrated waste to produce fodder.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for converting organic waste into resource    (2) a recording medium for storing a set of instructions to perform a method for converting organic waste into resource.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an organic waste resourcing apparatus.'(Drawing includes non-English language text)'
NOVELTY - Invention relates to agriculture. The method of increasing the efficiency of action of deposits of urban sewage waters as organo-mineral fertiliser comprises semi-fusty cattle (cattle) manure, and for increasing the efficiency of action of deposits of urban sewage waters (DUSW) as organo-mineral fertiliser the semi-fusty cattle manure is added to DUSW at a ratio of 1:1 and is applied at the rate of: DUSW - 40 t/ha, cattle manure - 40 t/ha.    USE - Agriculture.    ADVANTAGE - Invention enables to enrich additionally the deposits of urban sewage waters with organic substances of natural origin, a wide range of macro- and microelements, beneficial microflora, which enables as a whole to increase the efficiency of DUSW as fertiliser.2 tbl
NOVELTY - The electrolysis cell (22,25) has a cathode (3), a solid electrolyte layer (4), and an anode (5) that are successively laminated on a surface of a porous support structure (2) provided with a flow-hole (7) along a longitudinal direction. The gas by which flow-holes provided with water vapor is introduced by an outbound path side stream through-hole (7a). The gas containing hydrogen flows are comprised by an inbound path side-stream through-hole (7b). The support structure is arranged between outbound path side-stream through-hole and inbound path side-stream through-hole.    USE - Electrolysis cell of electrolysis cell stack apparatus used in electrolyzer (all claimed).    ADVANTAGE - The water vapor in the outbound path side-stream through-hole suppresses the leaking out in the inbound path side-stream through-hole with much hydrogen through the inside of the support structure in the boundary portion of the outbound trip side-stream through hole and the inbound path side-stream through-hole, and the electrolysis capability is improved effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view and cross sectional view of the electrolysis cell.    Porous support structure (2)    Cathode (3)    Solid electrolyte layer (4)    Anode (5)    Flow-hole (7)    Outbound path side stream through-hole (7a)    Inbound path side-stream through-hole (7b)    Electrolysis cells (22,25)
NOVELTY - Manufacture of fuel involves producing dewatered sludge by dehydrating organic sludge, mixing dewatered sludge and wooden fragment and/or sawdust, and producing wood material-mixed sludge.    USE - Manufacture of fuel used in sludge recycling system (all claimed).    ADVANTAGE - The fuel is manufactured quickly and economically without generating odor. The organic sludge is recycled efficiently. The wood material-mixed sludge is burned efficiently during processing of fuel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel containing dewatered sludge, wooden fragment and/or sawdust and plant-derived deodorizer; and    (2) sludge recycling system, which has fuel manufacturing plant and combustion unit, to which fuel is supplied.
NOVELTY - The cold plasma reforming chamber has vertical cavity that provides vertical path for chemical gas mixture to rise past the two or more electrodes and ground plane. The electrodes receive a control voltage large enough to produce electrical discharge for causing cold plasma reaction efficient to molecularly break down a portion of chemical gas mixture into hydrogen and unreacted chemical gas mixture heavier than hydrogen. A fan pulls unreacted chemical gas mixture into recycling cavity that directs unreacted chemical gas mixture toward reentry into vertical cavity.    USE - Cold plasma reforming chamber used in fuel cell for generating energy used in electronic apparatus. Uses include but are not limited to handheld device, consumer electronics, general-purpose computer, specialty computing device.    ADVANTAGE - The decrease in input voltage while current signature stays positive reduces the power necessary for hydrogen production in reforming chamber. The constant monitoring of current signature from the direct current-to-direct current (DC-to-DC) converter and corresponding adjustment of the input voltage ensures that electrical discharge is continually present and hydrogen is constantly being generated. Ensures more efficient production of hydrogen from the hydrocarbon-water mixture by allowing the molecules of reforming-chamber mixture to be excited and then relaxed. The use of just enough supply voltage to maintain the electrical discharge ensures that power is not wasted while plasma in reforming chamber is being produced.    DETAILED DESCRIPTION - The chemical gas mixture contains hydrocarbon-water mixture that is molecularly broken down into hydrogen and carbon dioxide. The hydrocarbon contains at least one member of a group consisting of methane, butane, propane, and ethanol.
NOVELTY - Fertilizer formed by reacting fossilized organic matter with waste saccharides, is claimed.    USE - The fertilizer is useful for fertilizing vegetation (claimed). The fertilizer activity was tested in broccoli plant by measuring number of cells sprouted and by measuring average height. The result showed that broccoli plant treated with fertilizer (1 table spoon liquid solution/gallon) showed 9 sprouted cells and an average height of 45.81 cm when compared to the broccoli plant treated with commercial fertilizer (1 table spoon dry powder/gallon) which showed 7 sprouted cells and an average height of 44.08 cm.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a fertilizer comprising a base material formed by reacting fossilized organic matter with saccharide, combined with at least one additional ingredient including phosphate, nitrate, mineral, pH balancer, additional organic matter and/or other soil builders; and    (2) fertilizing vegetation by applying a fertilizer made by reacting fossilized organic matter with saccharides.
NOVELTY - A chicken and pig manure fermentation composite bacteria comprises 20-30 pts. wt. Bacillus subtilis, 20-25 pts. wt. Bacillus licheniformis, 10-25 pts. wt. Bacillus coagulans, 10-20 pts. wt. Bacillus megaterium, and 8-15 pts. wt. Trichoderma viride.    USE - A chicken and pig manure fermentation composite bacteria for preparing organic fertilizer (claimed).    ADVANTAGE - Chicken and pig manure fermentation composite bacteria has low production cost, convenient use, no smell, and good fermenting effect.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) preparation of chicken and pig manure fermentation composite bacteria which involves performing high-density culturing on B. subtilis, B. licheniformis, B. coagulans, B. megaterium, and T. viride, performing activation culturing in shake flask containing 15-30 vol.% culture medium, inoculating in fermentation tank, performing expansion culturing, and dehydrating and drying single strain to obtain dormant microorganism dry powder, and mixing raw materials; and (2) use of chicken and pig manure fermentation composite bacteria which involves mixing chicken and pig manure with crushed straw, adding chicken and pig manure fermentation composite bacteria with addition amount of 1-2 kg/ton to obtain mixed material with moisture content of 50-65 wt.%, piling to form compost pile, starting fermenting at 55-65 degrees C, turning once 2 days after starting fermentation, turning once every 1-2 days while maintaining moisture content at 50-65 wt.%, and cooling to normal temperature to end fermentation and obtain organic fertilizer with moisture content of 20-30 wt.%.
NOVELTY - Regeol B is prepared by crushing Tripterygium wilfordii stems, performing ultrasonic extraction with ethanol, concentrating extract until dry to obtain crude extract, extracting, filtering, concentrating filtrate to obtain concentrated solution, mixing with silica gel sample, volatilizing solvent, performing dichloromethane-methanol gradient elution in silica gel column, monitoring with thin-layer chromatography (TLC), collecting regeol B eluate, concentrating, separating and purifying using high-speed countercurrent chromatography, and freeze-drying.    USE - Preparation of regeol B (claimed).    ADVANTAGE - Preparation of regeol B is simple and has high product purity and yield and small pollution, and regeol B has anti-tumor effect and improved biological utilization degree.
NOVELTY - Method for preparing sugar solution, involves (a) pretreating a first cellulose-containing biomass, (b) adding second cellulose-containing biomass to pretreated biomass, and performing hydrolyzation using a mold-derived cellulase, and (c) subjecting the hydrolyzate to solid-liquid separation to obtain a solution component and hydrolysis residue, and filtering the solution component through an ultrafiltration membrane to recover the mold-derived cellulase as a non-permeate and recover the sugar solution as a permeate.    USE - The method is useful for preparing sugar solution (claimed) which is used as fermentation ingredient of various chemical substances.    DETAILED DESCRIPTION - Method for preparing sugar solution, involves (a) pretreating a first cellulose-containing biomass, (b) adding 1-50 wt.% second cellulose-containing biomass with respect to the solid weight of the first cellulose-containing biomass pretreated substance of step (a), and performing hydrolyzation using a mold-derived cellulase, and (c) subjecting the hydrolyzate to solid-liquid separation to obtain a solution component and hydrolysis residue, and filtering the solution component through an ultrafiltration membrane to recover the mold-derived cellulase as a non-permeate and recover the sugar solution as a permeate. An INDEPENDENT CLAIM is included for method for preparing chemical substance, which involves preparing the sugar solution, and cultivating microorganisms in sugar solution.
NOVELTY - The method involves sending the food waste for crushing to removed the foreign substance, and mixing and agglomerating the precipitated dehydrate to the composting process. The neutralization processing supplies the effluent, in which the preprocess phase is sent to the aerobic biological processing. The solid material is sent to the settling tank for aerobic biological treatment, and supplies air from the blower.    USE - Method for processing a food waste.    ADVANTAGE - Solid material is removed in a simple and easy manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of a method for processing a food waste. (Drawing includes non-English language text).
NOVELTY - This utility new type claims a one family kitchen garbage treatment and recycling use of local processing device, comprising a rectangular box body by the clapboard of closeness, stainless steel basket, a food crusher, cloth water pipe compose. A multi-clapboard set with different height inside a box body of the box body dividing into kitchen garbage cutting area, oil removing and partition area, Anaerobic reaction area, the area is equipped with stainless steel basket and small food pulverizer in a kitchen garbage and a cover area, in Anaerobic reaction area upper part set with a multi-Anaerobic a a liquid adding wherein, inner cloth with water pipeline, and the precipitate area set with discharge tube and water , it also set with slag. This utility new type can place the kitchen garbage treatment and recycling use, reducing municipal pollution, energy-saving and environment-friendly, safe and convenient.
NOVELTY - A one open compost with a folding waterproof heat preservation device, wherein this a folding waterproof heat preservation device comprising: motor, switch, bracket, a transmission belt, a driven wheel, a winding drum, a bracket, a drum axial direction two end in a one set with a motor and a bracket one, the electric machine fixed mounted in the upper bracket, the bracket lower part is mounted with a roller, a motor capable of forward or reverse, the switch is set in a bracket at one side a motor a, a driven wheel set with a winding drum shaft a, the electric machine through conveyor driven wheel and set with and end up in the bracket is set with a flat plate in the lower part of the driven wheel, a drum upper, a flat plate, the first connecting rod, the first supporting pole, supporting pole in turn through second pin hinge, the first supporting pole, second supporting pole, the first connecting rod by a fixed sleeve, a stick, regulating bolt compose of a flexible cylindrical tube. This device has simple structure, convenient operation, because the two side winding of the electric machine are a use, the operator can work with high efficiency, with waterproof cover is not easy to be damaged, at the same time to save the storing space of a folding of the structure.
NOVELTY - This new utility model claims of a kind of organic fertile one bi-direction side Turning, comprising: box body and a main shaft, a turning bottom turning the main shaft box positive front of body, the middle part of main shaft turning and turning main shaft is set with dial material leaves the paddle rotate shaft, two side turning shaft is respectively provided with spiral stirring blade, dial material paddle leaf positive upper part of box inner set with material transporting blade, material transporting blade two side respectively set with transmission transporting device, box body of the material transport paddle leaf positive front is set with material input window. This new utility model the beneficial effect as follows: Turning walking one side head to pile the fertilizer, directly rotating to at once can be cut back fertilizer turning continue working without empty another one head can walk can start working turning, turning increase working efficiency and save working cost and consume side Turning, adopt this utility new type the organic fertile bi-direction side Turning can realize no strip-shaped stacking construction can at once, effective use of the land resource, which saves manual work strip-shaped stacking and construction cost.
NOVELTY - A one segment with combined aerobic compost reaction experiment device, comprising material mixed part, an aerobic compost part, circulation water part and air supply part, material mix part comprising material mixed chamber and transmission device, the aerobic compost part comprising aerobic compost bin body, aerobic compost bin body set with feeding and discharging wherein wherein, lower part set with circulation water outlet and air inlet, an aerobic compost bin body by stainless steel hole plate of the separating cabin is compost chamber of upper part and lower part of the pneuma bin, compost chamber top fixed with a scraper track, circulation water pump outlet and aerobic compost bin body top set with feed wherein a; air outlet and the air inlet of a leachate storage tank and entering into the pneuma of pipe. This utility new type is advantages as follows: a. mix material cabin can make material fully mix uniform and does not has a large area fertilizer agglomeration, porous channel cobblestone supporting layer is aerobic degradation supply;.. without need to stir, which can ensure that there is no agglomeration reaction in process, it will not produce local Anaerobic.
NOVELTY - This new type utility claims shell compost reaction room, including by four wall surface and the ground is composed of outside room, and reaction room through a transverse plate; and a room through a multi-separation vertical plate a, and grid plate set with b opposite a transverse plate, and a cover plate set with b of the top surface of the reaction room connecting with blast pipe, an atomizing pipe and heating pipe, the transverse upper side with multi-set with a through hole. This utility new type of shell compost reaction room, through reaction adjust room environment, satisfying fit microorganism growing of a temperature and humidity environment, after the fruit rapid compost reaction, compost, directly open gate plate the compost out can be effective to reduce environment pollution and at the same time a the fruit fertilizer as organic fertilizer auxiliary plant growing.
NOVELTY - The utility model is a new type claims a one droppings organic fertilizer fermenting pool, fermentation pool comprising a pool body (1), the pool body (1) by a two side wall and one bottom plate compose a; a bottom plate set with at least two of the length direction and a side wall in a trench (8), a trench (8) is mounted above the activity plate (6), the activity plate (6) are set with a through hole (7), the activity plate (6) is a plane are and pool body (1) is a plane bottom plate; the trench (8) of the lower part and the inner ditch (5) connect the inner (5) and outer (4) connect the outer ditch (4) and sewage processing system connection. A trench (8) in mounted high pressure pneuma pipe (2), high pressure pneuma pipe (2) mounting a plurality of pneuma nozzle (9), a high pressure pneuma pipe (2) and air compressor (4) connect. This utility new type structure is simple and reasonable, the fermentation speed is fast, sewage is contained a harmless treatment.
NOVELTY - An ecological agriculture recycling processing device comprises plant straw incineration tank (2), excrement and straw fermentation tank (1), and material storage tank (3).    USE - An ecological agriculture recycling processing device (claimed).    ADVANTAGE - Ecological agriculture recycling processing device is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of ecological agriculture recycling processing device.    Fermentation tank (1)    Incineration tank (2)    Material storage tank (3)    Material storage tank port (4)    Conical cavity (5)
NOVELTY - This utility new type provide the one a kitchen garbage processing production line, comprising a storing one of kitchen waste discharging pool, wherein the pool a discharging process in kitchen waste liquid one part of liquid fertilizer processing area and one in a solid part of kitchen waste processing area, further comprising the kitchen garbage in one solid part of conveying to treatment area of the pre-processing area, the pre-processing area comprising one processing auxiliary material auxiliary material processing area and a solid part in one of the kitchen garbage and auxiliary material mixed a mixed area. This utility new type of kitchen garbage processing production line aiming at the characteristics of kitchen garbage, the liquid part and solid part is separated from the kitchen garbage treatment and reasonable pipeline design structure, so the floor area is small, the pollution is small, efficient and so on, is one suitable b a kitchen garbage treatment system of industrial and environment-friendly.
NOVELTY - This utility new type provide the one application b a kitchen garbage processing production line of fermentation groove, comprising a plurality of mutually parallel of a concrete groove body, one side of the groove body set with a stacking area, wherein each said in a groove body are set with vent-pipe, one air blower through a pipe a groove body in the air, further comprising one the pneuma fan, the pneuma fan through a set of discharge pipe in the groove body upper part outside the pneuma to a whole the groove body area where atmospheric pressure is negative pressure, the groove body area where a closeness space. This utility new type has following advantages: automatic feeding, automatic discharging, increase production efficiency, air blower independent space, for a can after a process of recovery and reduce the energy consumption. Closeness space, negative pressure air conditioner design, reduces the smell, smell by a two channel processing only. And stacking operation controller, using a controller, reduces the operation risk and increase safety working environment.
NOVELTY - This utility new type claims a one aerobic excess sludge of automatic fermentation device, comprising a tower body, the top part of the fermentation the fermentation tower body set with feeding wherein the bottom set with hopper, the fermenting tower body internal through aeration component is outside set with a fan, a waste pneuma collecting cover set with the top part of a fermenting tower body inner cavity, a waste pneuma collecting cover is a hollow cone, the bottom of the inner cavity of the fermentation tower body connected the top through a pipeline connecting the waste pneuma inlet of three phase separator, used for the produce of sludge fermentation waste pneuma collecting process. This utility new type device through a control system realize automatic feeding, discharging, and can ensure the aerobic excess sludge feeding material uniform, fermenting process ventilation condition is good, residual sludge aerobic compost fermentation effect. fermentation process in a waste pneuma produce through a waste collecting system collecting after pneuma unified treatment to prevent the second pollution.
NOVELTY - This utility model belongs to the waste treatment technology field, and specifically relates to a garbage fermentation device. This utility model comprises a main body the fermentation, wherein the fermentation device main body set with upper end with a feeding port, the fermentation device main body lower end set with a discharge wherein the fermentation device main body intermediate a mounting with a marsh gas furnace, the furnace gas side is also mounted with a dryer. This utility model uses a heat dryer supply in fermentation jar body, fermentation; use in fermentation jar is garbage raise temperature fermentation marsh gas and a marsh gas supply combustion furnace, a save coal, it saves coal resource, protect environment, a rear gas-fired furnace combustion supply dryer heat supply, the organic fertilizer drying. In addition, this utility model has strong practicability, production cost is not high, social contribution are large, the product in the same type product fit in popularization and use.
NOVELTY - This utility new type is a device for transferring livestock and poultry excrement water to microorganism fertilizer belonging to the organic fertilizer production technology field. This device by livestock and poultry excrement water hydrolysis acidification groove, germ culture tank, a lactic acid culture tank, yeast culture tank, a mixed liquid culture tank, pneuma and culture tank, biological fluidization bed reactor a. After livestock and poultry excrement by water hydrolysis acidification treatment, the supernatant culture photosynthetic germ, then mixed nutrient solution to a culture the lactic acid and a yeast, at last a photosynthetic germ, lactic acid a, the three yeast a nutrient solution mix, by aerobic culture, fluidization bed reactor as futher treatment, into a microorganism fertilizer. The device fully using biological characteristic of photosynthetic germ, livestock and poultry excrement water for carrying out comprehensive use, production of a microorganism fertilizer, which is good for sustainable development of agriculture.
NOVELTY - This utility new type relates to marsh gas fermentation field, especially relates to a marsh gas production system. It comprising orderly arrangement of feeding tank, a c, hydrolyzing pool and Anaerobic fermentation jar, said transfer device comprising a main inclined conveyor and the main transmission part with the top end of two horizontal segment of secondary conveying belt, two section sub-belt type arrangement and in a main conveyor belt and vertical, hydrolyzing pool with two of which a the two side conveyor section of outside end, the main conveyor and the secondary conveyor belt mounted with two of following a compose by human is a hopper-shaped, the width of entrance of each lower hopper is greater than or equal to width of main conveyor, width of each exit of lower hopper is less than or equal to a width of the secondary belt, a stirrer of there are three, which are along the radial wall cloth and they are in the tank body wall of a height is not one. This utility new type has simple structure, high efficiency and convenient use.
NOVELTY - This utility new type relates to marsh gas fermentation field, especially relates to a marsh gas production system. It comprising orderly arrangement of feeding tank, a conveying device, hydrolyzing pool and Anaerobic fermentation jar, said conveying device comprising main conveyor is inclined and main conveyor is located below the top end of two horizontal segment of secondary conveying belt, two section sub-belt type arrangement and in a main conveyor belt and vertical, hydrolyzing pool with two of which a the two side conveyor section of outside end, between the main conveyor and secondary conveyor belt is mounted by two following a compose a human shape of a hopper, a hopper is entrance width is more than or equal to width of main conveyor, width of each exit of lower hopper is less than or equal to a width of the secondary belt, a stirrer of there are three, which are along the radial wall cloth and they are in the tank body wall of a height is not one. This utility new type has simple structure, high efficiency and convenient use.
NOVELTY - This utility new type claims a laboratory using one Anaerobic fermentation flask, the Anaerobic fermentation flask is sealed structure, comprising seal bottle plug, edulcoration device a fermentation bottle body, bottle plug seal tightly in setting a fermentation bottle body, bottle mouth edulcoration device set in lower part of seal bottle plug. This utility new type claims a laboratory with Anaerobic fermentation flask one, for the fermentation flask process is improved, a convenient using activity machinery stir device for a high concentration in fermentation flask material carry out stir monitoring experiment of different depth, to search rapid produce marsh gas is the best, is the actual marsh gas production provide a powerful scientific technology supporting, at the same time, the utility model is new type structure is simple, the practicability is strong.
NOVELTY - This new type utility claims one a multifunctional energy-saving environment-friendly toilet, comprising a toilet main body, set with a roller at the bottom, a toilet main body inner set with excrement processing system, urine processing system and cleaning system, the excrement is a processing system including one stay for a device, a biochemical treatment device comprising distillation kettle, pre-heating solar energy water tank, filter, a condensing water tank, the top part of the toilet main body is set with at least one a solar energy heater, solar energy heater and solar energy pre-heating water tank through a pipeline, collecting tank through a water pump one distillation kettle and a pipeline, and the connecting pipeline passes through the solar energy pre-heating water tank, distillation kettle with solid discharging port and gas discharging port, discharging the gas after filter and condensing water tank pipeline connecting the condensed water tank through water pump and connection to a ceiling water tank one. This utility new type of multifunctional energy-saving and environment-friendly mobile toilet excrement for a biological purification process and environment in a water recovery and use and water-saving.
NOVELTY - Low concentration aqueous ammonia carbonization recovery method comprises: (a) adding water softener into a synthetic air washing tower, then mixing the resultant liquid with low concentration aqueous ammonia mother liquor in a copper washing ammonia tower, passing the resultant liquid into a recovery tower for absorption of ammonia under constant pressure to obtain low concentration aqueous ammonia; and (b) passing the resultant low concentration aqueous ammonia into a carbonization section, simultaneously transforming gas to synthesize ammonia, then recovering ammonia gas.    USE - The method is useful as low concentration aqueous ammonia carbonization recovery method.    ADVANTAGE - The method is conducive to product structure adjustment, saves water resources and achieves cleaner production.    DETAILED DESCRIPTION - Low concentration aqueous ammonia carbonization recovery method comprises: (a) adding 0.4-0.6 ton/hour water softener into a synthetic air washing tower, then mixing the resultant liquid with low concentration aqueous ammonia mother liquor in a copper washing ammonia tower, passing the resultant liquid into a recovery tower for absorption of ammonia under constant pressure to obtain 130-140 ton/hour low concentration aqueous ammonia; and (b) passing the resultant low concentration aqueous ammonia into a carbonization section, simultaneously transforming gas to synthesize ammonia, where the reaction produces ammonium bicarbonate products and secondary low concentration aqueous ammonia mother liquor, continuously passing the secondary low concentration aqueous ammonia mother liquor back to ammonia gas recovery system.
NOVELTY - Sewage purification agent comprises cylindrical shaped activated carbon as a support material for composite microorganisms.    USE - Sewage purification agent.    ADVANTAGE - The sewage purification agent is capable of degrading pollutants in livestock and poultry wastewater in a highly efficient and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing sewage purification agent, which involves:    (A) culturing each strain of the composite microorganisms till the strain reaches logarithmic growth phase;    (B) collecting culture growth of each strain, and then centrifuging them to collect pellets;    (C) washing the collect pellets of each strain of composite microorganisms sterile saline, and then mixing them uniformly to prepare a suspension of composite strains;    (D) adding activated carbon carrier as a support material to the prepared suspension of composite strain, followed by incubation at 30-37 degrees C for 48-72 hours under shaking condition to obtain sewage purification agent; and    (E) drying the obtained sewage purification agent at 30-37 degrees C to obtain desired product.
NOVELTY - Preparing biological selenium-enriched fertilizer comprises: (a) drying chicken manure, mushroom residue and distillers to a moisture content of less than 20%; (b) grinding the dried mixture; (C) mixing; (d) adding fermentation agent to the mixture; (e) adjusting the moisture content of the mixture to 40-60%; (f) carrying out fermentation at a temperature of 40 degrees C and then at 60 degrees C for 3-7 days; (g) drying the fermented mixture; (h) testing the product for water content, heavy metals content, nitrogen-phosphorus-potassium (NPK) content; (i) packaging; and (j) storing the packaged product.    USE - The method is useful for preparing biological selenium-enriched fertilizer (claimed), which is useful for rice, wheat, soybean, and vegetable crops.    ADVANTAGE - The method is capable of simply, economically and environmental-friendly producing the selenium-enriched fertilizer.    DETAILED DESCRIPTION - Preparing biological selenium-enriched fertilizer comprises: (a) drying chicken manure, mushroom residue and distillers to a moisture content of less than 20%; (b) grinding the dried mixture; (C) mixing the mixture; (d) adding fermentation agent to the mixture; (e) adjusting the moisture content of the mixture to 40-60%; (f) carrying out fermentation at a temperature of 40 degrees C and then at 60 degrees C for 3-7 days; (g) drying the fermented mixture; (h) testing the product for water content, heavy metals content, nitrogen-phosphorus-potassium (NPK) content; (i) packaging the mixture; and (j) storing the packaged product in a well-ventilated, dry and cool environment.
NOVELTY - Auxiliary agent comprises 50-75 wt.% peanut bran, 20-50 wt.% plant ash, 3-8 wt.% calcium superphosphate, 0.2-0.5 wt.% sodium acetate, 0.01-0.03 wt.% zinc sulfate heptahydrate, 0.01-0.03 wt.% boric acid and 0.02-0.05 wt.% manganese sulfate tetrahydrate.    USE - Auxiliary agent used for culture medium useful for cultivating straw mushroom (all claimed).    ADVANTAGE - The auxiliary agent is convenient to use, provides straw mushroom with good growth vigor, strong stress resistance and increased weight at high yield, and promotes the use of sugarcane bagasse, manioc waste, straw and corn core as raw materials for straw mushroom cultivation culture medium, thus, developing the straw mushroom industry, providing inexpensive raw material sources, realizes recycling of waste materials, and protecting the ecological environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for straw mushroom cultivation comprising preparing straw mushroom culture medium by providing sugarcane bagasse, manioc waste, straw and/or corn core as raw materials, uniformly mixing corn core, lime and water by stirring and fermenting to obtain straw mushroom culture medium, preparing auxiliary agent by uniformly mixing zinc sulfate heptahydrate, boric acid, manganese sulfate tetrahydrate, sodium acetate and water to prepare mixed aqueous solution, uniformly mixing peanut bran, plant ash and calcium superphosphate to prepare solid mixture, adding the mixed aqueous solution into the solid mixture, uniformly stirring, drying to a water content of 15%, and obtaining auxiliary agent, uniformly mixing culture medium and auxiliary agent, bagging, sterilizing, inoculating and cultivating straw mushroom.
NOVELTY - Organic fertilizer comprises 50-60 pts. wt. peony leaf, 30-40 pts. wt. fresh livestock, 20-30 pts. wt. mushroom residue, 15-20 pts. wt. soybean meal, 5-10 pts. wt. starch, 2 pts. wt. microbial inoculant, 5-10 pts. wt. nitrogen phosphorus potassium compound fertilizer, and 5-10 pts. wt. polyacrylamide.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer can enhance the permeability and water retention properties of the soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the organic fertilizer comprising mixing peony leaf, mushroom residue, soybean meal and starch and then adjusting the water content and pH value to 7-8, fermenting the mixture for 15-20 days at a temperature of 40 degrees C, adding starch and zeolite in the fermented mixture, adding water to the mixture to adjust the moisture content to 60-65%, further fermenting the mixture for 510 days at 60-65 degrees C, reducing the temperature of the mixture to room temperature, drying the mixture, and uniformly mixing the mixture with nitrogen phosphorus potassium compound fertilizer and polyacrylamide and then granulating to obtain the organic fertilizer.
NOVELTY - Producing organic fertilizer comprises mixing Wedelia wallichii, 60-95 mass% of organic raw material, 5-40 mass% of composite fermentation yeast and soluble sugar, and carrying out anaerobic fermentation, aerobic fermentation and aging, then drying.    USE - The method is useful for producing organic fertilizer (claimed), which is useful for inhibiting and killing snail.    ADVANTAGE - The organic fertilizer reduces damage of crops, and effectively reduces the harmful germ and mildew harm for crops of root part.
NOVELTY - Biological organic fertilizer comprises 20-35 pts. wt. peat, 15-20 pts. wt. urea, 12-15 pts. wt. ammonium sulfate, 5-9 pts. wt. potassium metaphosphate, 1-3 pts. wt. potassium pyrophosphate, 4-8 pts. wt. phosphoric acid, 3-8 pts. wt. manganese phosphate, 0.01-0.02 pts. wt. silicate, 0.01-0.02 pts. wt. Bacillus cereus, 0.01-0.02 pts. wt. Bacillus thuringiensis, 25-30 pts. wt. chicken manure, 14-25 pts. wt. rice bran, and 10-16 pts. wt. wheat bran.    USE - Biological organic fertilizer.    ADVANTAGE - The fertilizer has good water absorption and water retention properties, provides nutrients required for plant overall growth, and improves soil physical properties and soil fertility restoration.
NOVELTY - Preparation of tofisopam intermediate comprises taking 1-(3,4-dimethoxyphenyl)-3-ethyl-5,6-dimethoxy-2-methyl-indene as a starting raw material, and reacting under acidic condition using copper compound as catalyst and hydrogen peroxide as oxidizing agent to obtain tofisopam intermediate i.e. 3-(2-(3 4-dimethoxybenzoyl)-4 5-dimethoxyphenyl)pentan-2-one.    USE - Preparation of tofisopam intermediate i.e. 3-(2-(3 4-dimethoxybenzoyl)-4 5-dimethoxyphenyl)pentan-2-one (claimed).    ADVANTAGE - The method greatly reduces the content of heavy metals in wastewater, avoids the use of carcinogenic chromium compound, and protects the environment.    DETAILED DESCRIPTION - Preparation of tofisopam intermediate comprises taking 1-(3,4-dimethoxyphenyl)-3-ethyl-5,6-dimethoxy-2-methyl-indene as a starting raw material, and reacting under acidic condition using copper compound as catalyst and hydrogen peroxide as oxidizing agent to obtain tofisopam intermediate i.e. 3-(2-(3 4-dimethoxybenzoyl)-4 5-dimethoxyphenyl)pentan-2-one. The 1-(3,4-dimethoxyphenyl)-3-ethyl-5,6-dimethoxy-2-methyl-indene is prepared by reacting esterification reacting isoeugenol and methanol in the presence of concentrated sulfuric acid, methylation reacting the esterified product with dimethylsulfate, and drying to obtain the target product.
NOVELTY - Alkaline extraction and acid precipitation of southernwood dihydroartemisinic acid from artemisinin production waste material includes concentrating artemisinin production waste material by vacuum evaporating the residual solvent, adding alkaline solution as extracting agent, ultrasonically extracting for 2 times, depositing, combining the two extraction liquids, room temperature precipitating, collecting the supernatant, clarifying to obtain clear extract solution, adding acid solution, continuously stirring, completely precipitating at room temperature and collecting the precipitates.    USE - Alkaline extraction and acid precipitation of southernwood dihydroartemisinic acid from artemisinin production waste material (claimed).    ADVANTAGE - The method has increased extraction efficiency and high recovery rate i.e. more than 90%, achieves product purity of more than 72%, and is easy for large-scale production.    DETAILED DESCRIPTION - Alkaline extraction and acid precipitation of southernwood dihydroartemisinic acid from artemisinin production waste material comprises concentrating artemisinin production waste material by vacuum evaporating the residual solvent to obtain concentrate, adding 1 ml of 0.2-0.6 mass/vol.% alkaline solution as extracting agent to 3-5 g concentrate, ultrasonically extracting for 2 times at ultrasonic power of 80-115 W and 30-50 degrees C for 40-60 minutes, depositing, combining the two extraction liquids, room temperature precipitating, collecting the supernatant, clarifying to obtain clear extract solution, adding 0.3-2 mol/L acid solution, continuously stirring until the solution pH is 1.0-4.5, completely precipitating at room temperature, collecting the precipitates, washing with distilled water for 2 times, each using 2 ml distilled water/g precipitate, pre-freezing at - 21 degrees C for 10-24 hours, and vacuum freeze drying until the product water content is less than 1%.
NOVELTY - Azithromycin is purified by dissolving crude azithromycin in non-water soluble organic solvent, quantitatively washing with aqueous acidic solution to water-soluble impurities, transferring to aqueous phase containing acid, washing with organic solvent and small amount of strong alkaline solution to obtain fat soluble impurities to obtain high purity azithromycin salt solution, adding water-soluble polar solvent, activated carbon, and drops of alkaline, filtering impurities, crystallizing azithromycin, filtering, washing, and drying.    USE - Purification of azithromycin for continuous extraction column (claimed).    ADVANTAGE - Process is low cost, reasonable, safe, environment-friendly, improves labor efficiency, yields uniform crystal size, and has easy to control crystallization rate, and high yield of high quality and stable material.
NOVELTY - Erythromycin thiocyanate is extracted by ultrafiltering erythromycin fermentation broth to obtain ultrafiltration permeate, concentrating by nanofiltration, extracting with organic solvent to obtain organic phase, ceramic membrane filtering, crystallizing, separating, and drying.    USE - Extraction of erythromycin thiocyanate (claimed).    ADVANTAGE - Process simple, environment-friendly, and has reduced solvent cost and high yield of high purity products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for erythromycin thiocyanate extraction device comprising ultrafiltration membrane (1) connected to retentate side inlet of erythromycin fermentation liquid and nanofiltration membrane (2) inlet and nanofiltration membrane outlet is connected to retentate side of extraction column (3) in which bottom of extraction column is connected to ceramic membrane (5) inlet, ceramic membrane is connected to permeate side of intermediate tank (6) provided with sodium thiocyanate tank (7), and intermediate tank is connected sequentially to crystallization kettle (8), solid-liquid separation tank (9), and drying apparatus (10).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of erythromycin thiocyanate extraction device.    Ultrafiltration membrane (1)    Nanofiltration membrane (2)    Extraction column (3)    Ceramic membrane (5)    Intermediate tank (6)    Thiocyanate tank (7)    Crystallization kettle (8)    Solid-liquid separation tank (9)    Drying apparatus (10)
NOVELTY - Glutathione is extracted from wheat germ by adding water to wheat germ, extracting, performing solid-liquid separation to obtain 1st extract, adding water, extracting, performing solid-liquid separation to obtain 2nd extract, combining extracts, eluting with buffer through metal chelating affinity chromatography medium, collecting eluate, concentrating, and drying.    USE - Extraction of glutathione from wheat germ (claimed).    ADVANTAGE - Process is simple, easy to control, environment-friendly, low cost, and uses standardized equipments.
NOVELTY - The tank comprises a tank body, a chain wheel provided with the tank body, a transmission chain, a control unit comprising a main controller. An upper part of the chain wheel is mounted with the transmission chain. The chain wheel is connected with a transmission mechanism and a motor transmission. A bottom part of the tank body is provided with a liquid inlet and a liquid outlet. The main controller is connected to a bottom part of temperature and a pressure control device. The main controller comprises a control motor. The tank body is provided with a stirring device.    USE - The tank is useful for controlling temperature and pressure during marsh gas fermentation (claimed).    ADVANTAGE - The tank is capable of controlling the temperature and pressure during marsh gas fermentation using crop straw and farm manure in an eco-friendly manner with reduced energy consumption.    DETAILED DESCRIPTION - The tank comprises a tank body, a chain wheel provided with the tank body, a transmission chain, a control unit comprising a main controller. An upper part of the chain wheel is mounted with the transmission chain. The chain wheel is connected with a transmission mechanism and a motor transmission. A bottom part of the tank body is provided with a liquid inlet and a liquid outlet. The main controller is connected to a bottom part of temperature and a pressure control device. The main controller comprises a control motor. The tank body is provided with a stirring device. A temperature-controlled water pipe is connected with a hot water valve and a cold water valve.
NOVELTY - Glucose aqueous solution is manufactured by performing 1st treatment process of heat-processing biomass in 0.01-7 wt.% of mineral acid aqueous solution and separating into process liquid and residue and performing 2nd treatment process of heat-processing residue obtained by 1st treatment process in 0.01-7 wt.% of mineral acid aqueous solution and separating into process liquid and residue. Biomass is hydrolyzed, and glucose aqueous solution is obtained.    USE - Manufacture of glucose aqueous solution for manufacture of bioethanol (claimed).    ADVANTAGE - Glucose aqueous solution can be easily and rapidly manufactured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of bioethanol which involves fermenting glucose aqueous solution and producing ethanol.
NOVELTY - Fertilizer comprises 10-30 pts. wt. traditional Chinese medicine residue, 5-25 pts. wt. rotten leaves, 5-10 pts. wt. eggshell, 10-20 pts. wt. melon skin, 30-50 pts. wt. poultry manure, 10-20 pts. wt. potash, 5-10 pts. wt. nitrogen and phosphorus fertilizer, 5-10 pts. wt. bone residue, 10-20 pts. wt. poultry wool and 50-70 pts. wt. tea residues.    USE - The fertilizer is useful for cultivating peony (claimed).    ADVANTAGE - The fertilizer is provided with balanced nutrition.
NOVELTY - The apparatus (100) has that fuel-supply and hydrogen recovery side cells (10,20) that are positioned mutually to be parallel so that a direction of going to a hydrogen-flow exit mutually opposes from a fuel intake. A connection unit (40) is provided between the fuel-supply and hydrogen recovery side cells so as to provide a flexibility to reduce a load originating in the heat elongation of fuel-supply and hydrogen recovery side cells, and is added to the fuel cell and hydrogen cell side connection units (41a,42a).    USE - Apparatus for producing hydrogen for fuel cell such as solid oxide fuel cell (SOFC) used as large-scale distributed power supply and household use power supply.    ADVANTAGE - The connection unit is provided between the fuel-supply and hydrogen recovery side cells by connecting the separated cells so as to provide a flexibility to reduce a load originating in the heat elongation of fuel-supply and hydrogen recovery side cells, and is added to the fuel cell and hydrogen cell side connection units so that the fuel-supply and hydrogen recovery side cells are thermally expanded. Thus, the thermal expansion of fuel-supply and hydrogen recovery side cells are tracked, and the length of connecting pipe between cells which is grade in which transformation of the connecting pipe between cells is possible is ensured. Hence, the strength and leak-proof property in hydrogen production apparatus are ensured effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the apparatus for producing hydrogen.    Fuel-supply side cell (10)    Hydrogen recovery side cell (20)    Connection unit (40)    Fuel cell side connection unit (41a)    Hydrogen cell side connection unit (42a)    Apparatus for producing hydrogen (100)
NOVELTY - This utility new type organic waste strengthening fermentation device of organic matter fermentation belongs to the auxiliary device, by a fermentation pool, the outlet pipeline of the air compressor passes through the fermenting pool and a lower part cloth is discharge tube body are connected, the upper part of a discharge tube body are cloth air outlet. Are cloth with the pneuma hole or nozzle in a discharge tube body, the diameter of the hole is 0.0001 to 200 mm. Coil set with fermentation pool in middle part, the two end disk pipe is connected and a water inlet pipe and a water outlet pipe passes through the fermenting pool side wall. The device, use air compressor compressing air, and air outlet use a organic waste transport a air compressing air form with a certain pressure of air flow inner in fermentation pool, a a fermentation device for oxygen supply, which ensures the fermentation process in the internal of a need for oxygen exchange so as to ensure the fermenting effect and fermentation time, it overcomes the fermentation is limited, energy-saving environment-friendly in environment with low temperature is low, the resource circulation use.
NOVELTY - This new type utility claims marsh gas pool stirrer, relating to Anaerobic fermentation of straw and livestock excrement Anaerobic fermentation process device technology field. Comprising rotating shaft and blade, rotating shaft transversely set in the inner reactor, a rotating shaft into spiral multi-set with a blade, the blade comprising a arm and paddle leaves head, one end arm of connecting and fixing a rotating shaft, and the other end connecting arm and a paddle leaves head fixing connection, paddle leaves a head plate of a cavity by a polyhedron, one side a polyhedral area maxinum is set into one end opening, a connecting arm and a fixing rotating mechanism driving the rotating shaft to rotate. Paddle rotating following rotation of a rotating shaft, a head set leaves one side is set with the opening downward and liquid surface of inner reactor first contact, following straw pulp leaves head is a floating in the liquid surface of a light such as a material to liquid surface, and other material fully mixed, increase production rate.
NOVELTY - The utility model claims a solar energy kitchen waste comprehensive treatment device, comprising solar energy greenhouse, pre-processing pool, material storage pool, the pool pre-processing a material storage pool, a material storage pool a solar energy greenhouse. Preferably, a set used for compost treatment of kitchen waste aerobic composting pool Anaerobic fermentation pool and a solar energy temperature in room, the Anaerobic fermentation pool connecting the material storage pool, the aerobic compost pool a. Anaerobic fermentation pool. This utility new type combine solar energy greenhouse, gradually increase material concentration, a rapid stable start of Anaerobic digestion device at the base of a conventional Anaerobic digestion technology. Anaerobic digestion generated biogas residue, according to the water according to the proportion after adding straw mixing uniformly carry out compost treatment, it not only effective absorptive reagent biogas residue, but also can form compost product for garden use. This comprehensive treatment method has operation energy consumption is low, the organic load high, digestive residue treatment cost is low, the raw material circulation use rate is high and so on.
NOVELTY - The utility model claims a fully-sealed marsh gas pool, comprising biogas pool, a feeding port, a groove, a pressure water tank, wherein the discharging guide pipe, switch, pneuma water separator, a tee joint, gas storage bag, purification regulator, a booster pump. pneuma and cooker, wherein said marsh gas pool is placed in ground up, the raw material groove through feed wherein and marsh gas pool is connected with the pressure water tank through discharge wherein marsh gas pool and is connected with a gas-guide tube through screw thread connecting mounting gas-guide tube of a switch after a left upper part of marsh gas pool, a water separator a pneuma, joint the fourth three-way joint mounted in guide pipe of pneuma, single vertical outlet of the three-way joint through the pneuma pipe and storage bag, the other one outlet through guide tube pneuma and purification regulator. This fully-sealed marsh gas pool which can increase effective marsh gas purity, increase effective use rate of marsh gas, simple, economical and reliable.
NOVELTY - Circulation photosynthetic reactor, including by circulation pipe after circulation main pipe, a circulation branch pipe, valve, suction pipe,,, wherein multi-spray head, bracket, a hydrolytic acidification compose. Circulation branch pipe from the circulation main pipe a, and b. hydrolyzing a size a acidification tank water connecting head, head size after a one section variable diameter after reducing a circulation branch pipe, the branch pipe end connecting multi-pipeline; wherein one end suction pipe and a straight pipe section of the upper size head connecting part, and the other one end extends into the hydrolysis acidification pool water in the upper layer. Utility new type can make the hydrolysis acidification pool water through inner circulation photosynthetic reactor realize internal circulation, regulating the function of buffering quality is degrading microorganism is relative stable supply of water amount fluctuation, acid-alkali condition, Degradation mechanisms concentration and temperature and so on, which is good for a biodegradable organic matter, at the same time, the hydrolysis acidification pool and a photosynthetic germ into the upper pool body, promote the biodegradation of organic pollutant in waste water.
NOVELTY - This utility new type claims a biological filler for repairing one of lake water body device, comprising a multi-biological filler through a connecting rope and into a processing unit, a multi-processing unit through the connection marker b horizontal rope, further comprising water quality real time monitoring device. Time to carry out, first for organic substance in lake, nitrogen, phosphorus and so on water quality index monitoring analysis process, for area of interest point of serious pollution, river lake bank select drain wherein lower end or pollutant serious standard area set with a section, then arranged suspended filler to a certain density, rear lake water and filler flow contact through one segment would form a biological film surface a filler, a germ biological film and each of a microorganism for the purification effect of water quality. This utility new type of device is simple, the operation and maintenance is convenient, operation cost is low, it has a good environment benefit and economic benefit.
NOVELTY - This utility model claims a device for separating propane from propylene through extractive distillation, to be solved technology problem is: aiming at low pressure of the separate propane and propylene fractionation, device investment and energy consumption are increased, separating high voltage rectification of propane and propylene, a further need of multi-theory plate number and technology problem of large return flow ratio. This utility model claims a device for separating propane from propylene through extractive distillation, comprising a light-constituent removing tower, a heavy component tower, extracting rectifying tower and extracting agent reclaiming tower, advantages of this utility new type device is simple, the investment is low, the separating effect is good, the extracting agent circulation use without second pollution, operation cost is low, and the polymeric by processing after a level of purity propane and propylene, it has a good social benefit and realize the efficient separating a propane-propylene.
NOVELTY - This utility new type provide a gas oxidizing one test device, comprising a bottom plate, a bottom plate set with gas proportion device, vacuum device happen, reaction container, a magnetic stir device, an ignition device, safety pressure relief device and sampling device, gas proportion device comprising nitrogen proportion device, gas to be detected proportion device and ethane gas proportion device, nitrogen proportion device, gas to be detected proportion and ethane gas proportion c. connecting and filling in a reaction container, a magnetic stir device set with a reaction container under vacuum happen device, an ignition device, safety pressure relief device and sampling device connection and a reaction container, a reaction container further a temperature measuring device and a pressure measuring device. This utility new type the to be detected and nitrogen mixed gas, oxidation ability of a gas to be detected whether is higher than air oxidation ability, so a gas oxidizing strength to be detected can be accurately the quantitative assessment of oxidizing gas, and the device test result is reliable, operation safety is high.
NOVELTY - Fungicide comprises 0.5-2 pts. wt. Stellera root, 3-5 pts. wt. water, 0.3-1 pts. wt. camphor, 1-3 pts. wt. tobacco leaves, 0.8-1.6 pts. wt. licorice, 1-3 pts. wt. salt bran, 3-5 pts. wt. gallnut, 0.5-2 pts. wt. radix sophorae flavescentis, and 0.2-0.6 pts. wt. synergistic agent.    USE - The fungicide is useful for treating and preventing Fusarium rot (claimed).    ADVANTAGE - The fungicide is non-toxic, has high selectivity towards fungi, and can be easily prepared with reduced amount of residue in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fungicide, comprising (a) mixing the above raw materials, adding 60% of ethyl alcohol to the mixture and extracting at 75 degrees C for 28 hours, followed by leaching with stirring at 210 revolutions per minute and then filtering, and (b) distilling the filtered liquid at a temperature of 130 degrees C and a pressure of 0.01 MPa, sterilizing at 100 degrees C for 21 minutes, adding azone and stirring the mixture uniformly.
NOVELTY - Fermentation apparatus comprises a high pressure air sending part (0202) to send out air from high pressure to low pressure in airflow path. Organic type material is not fixed, which is deposited on a deposition tank (0101) at irregular interval. The deposition tank is set with a low pressure air delivery part (0201) to send out air in order to make an aerobic fermentation with respect to organic type material deposited on the deposition tank.    USE - Fermentation apparatus used for processing organic type material for organic fertilizer and organic feed by fermentation (all claimed).    ADVANTAGE - The fermentation apparatus improves ventilation property in the deposition tank, and path of air is changeable.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of fermentation apparatus.    Deposition tank (0101)    Piping (0102)    Low pressure air delivery part (0201)    High pressure air sending part (0202)
NOVELTY - A composite biological filler livestock wastewater treatment method is performed by soaking composite biological filler in livestock and poultry wastewater for 3-10 hours in which volume ratio composite biological filler:livestock and poultry wastewater is 1:(10-20), removing filler, stacking, covering surface layer with wheat straw or corn stalk, composting at high temperature, and controlling daily composting temperature, T, at 0-45 degrees C in which composting time, t, is defined as 240 (T-10)x 2.4 and unit of t is hours, h.    USE - A composite biological filler livestock wastewater treatment method (claimed).    ADVANTAGE - The biological composite filler has high mechanical strength, large adsorption capacity of phytate, veterinary drug residues, urea, suspended solids, and macromolecules i.e. copper, iron, and zinc, and kills pathogens in wastewater.
NOVELTY - A municipal sewage treatment and sludge decrement system is performed by hydrolysis acidifying, anaerobic releasing of phosphorus, anoxic denitrifying using microorganism lysate, aerobic decomposing, culturing microorganism, three-level biological predating, and depositing in which phosphorus-rich liquid is treated by integrating solid phosphorus as sidestream, and device system consists of hydrolysis pool, anaerobic pool, aerobic pool, biological contact oxidation pool, sludge anaerobic pool, sludge pool, sludge aerobic pool, and sludge biological contact oxidation pool.    USE - Municipal sewage treatment and sludge decrement system (claimed).    ADVANTAGE - The system has no secondary pollution, convenient reconstruction, small difficulty coefficient, high reduction degree, and low cost, does not add chemical medicine, and reduces sludge and energy consumption.    DETAILED DESCRIPTION - A municipal sewage treatment and sludge decrement system is performed by hydrolysis acidifying, anaerobic releasing of phosphorus, anoxic denitrifying using microorganism lysate, aerobic decomposing, culturing microorganism, three-level biological predating, and depositing in which phosphorus-rich liquid is treated by integrating solid phosphorus as sidestream, and device system comprises hydrolysis pool, anaerobic pool, aerobic pool, biological contact oxidation pool consisting of activated sludge area set with micropore aeration device, and inner filling area having 30-45 vol.% per pool, sludge anaerobic pool, sludge pool, sludge aerobic pool, sludge biological contact oxidation pool having 30-50 vol.% filling area, and chemical dephosphorizing pool.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of municipal sewage treatment and sludge decrement system. (Drawing includes non-English language text).
NOVELTY - Organic fertilizer comprises 4-10 pts. wt. edible waste, 1-5 pts. wt. chicken manure, 1-5 pts. wt. furnace ash and 2-5 pts. wt. auxiliary material.    USE - The organic fertilizer is useful for fruit tree and flower planting.    ADVANTAGE - The organic fertilizer can be prepared with wide raw material source, less cost, less energy consumption and less labor intensive, and without environment pollution.
NOVELTY - Use of Stevia rebaudiana waste in preparation of biogas and soil conditioner is claimed. The biogas is prepared by separating wastewater from S.rebaudiana waste, pre-treating wastewater, separating residue and liquid, subjecting residue to anaerobic fermentation, separating solid residue and liquid from fermented broth and collecting biogas produced in fermentation tank. The soil conditioner is prepared by fermenting solid residue separated from fermented broth using bentonite and shell powder, and drying fermented mixture to obtain product.    USE - The S.rebaudiana waste is useful for preparing biogas and soil conditioner (claimed).    ADVANTAGE - The biogas and soil conditioner are prepared from S.rebaudiana waste by simple, energy-saving, convenient and cost-effective method.    DETAILED DESCRIPTION - Use of Stevia rebaudiana waste in preparation of biogas and soil conditioner is claimed. The biogas is prepared by (a) collecting S.rebaudiana waste in semi-closed container and separating wastewater from the waste using leachate collection system, (b) transferring separated wastewater into the wastewater pretreatment pool, separating residue and liquid, then subjecting to micro-aeration at 1-3 m3/(m3 water.day) and removing scum from the wastewater surface, (c) performing anaerobic fermentation at 30-55 degrees C for 25-35 days using the residue obtained in step (b), separating solid residue and liquid in the fermented mixture, collecting biogas produced in the fermentation tank and drying collected biogas, until the moisture content becomes 40-60%. The soil conditioner is prepared by mixing 50-60 pts. wt. solid residue separated in step (c), 30-40 pts. wt. bentonite and 10 pts. wt. shell powder uniformly, fermenting mixture at 50-60 degrees C for 10-15 days and drying fermented mixture, until the moisture content becomes 20% to obtain the product.
NOVELTY - Complex compound preparation involves utilizing fatty alcohol polyethenoxy ether, usnic acid and citric acid.    USE - Method for preparing complex compound used for preparing dandruff and hair washing liquid, medicated mouthwash, and fungicides and bactericidal intermediates for preventing Staphylococcus aureus, Escherichia coli, fungi, mold and microorganisms infection (all claimed).    ADVANTAGE - The method is simple and enables to prepare complex compound that is environment-friendly and cost-effective.
NOVELTY - A metal complex comprises polyhydric carboxylic acid compound, metal ion chosen from metal ion which belongs to groups 2-13 of periodic table, and 4-14C aromatic monocarboxylic-acid compound.    USE - Metal complex is used for occlusion material for gas storage apparatus for gas motor vehicle, separation material used for separating separates the carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, 1-4C hydrocarbon, noble gas, hydrogen sulfide, ammonia, sulfur oxide, nitrogen oxide, siloxane, and water vapor, and adsorbent used in canister (all claimed) of or hybrid vehicles.    ADVANTAGE - The metal complex has excellent gas-adsorption characteristics, gas-occlusion capacity, and gas-separation characteristics.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gas storage apparatus, which comprises gas occlusion space inside pressure-resistant airtight container having entrance and exit of gas, and occlusion material inside the gas occlusion space;    (2) gas motor vehicle, which comprises internal combustion engine which obtains driving force with the fuel gas supplied from the gas storage apparatus;    (3) separation method, which involves using separation material and contacting the metal complex and mixed gas at 0.01-10 MPa; and    (4) manufacture of metal complex, which involves depositing metal complex by reacting and stirring polyhydric carboxylic acid compound, metal ion chosen from metal ion which belongs to group(s) 2-13 of periodic table, and 4-14C aromatic monocarboxylic-acid compound in solvent.
NOVELTY - Treating used crackling oil, comprises performing a tangential ultrafiltration step.    USE - The method is useful for treating used crackling oil, which is useful as a biolubricant for a chainsaw (all claimed), preferably chainsaw loggers, where the oil is useful for the production of biofuels (preferably ethanol and biodiesel), biomaterials (preferably bioplastics and composites) and biomolecules (preferably surfactants, solvents, bio-lubricants and catalysts).    ADVANTAGE - The used crackling oil can be prepared with good biodegradability and low ecotoxicity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for oil obtained by the method, comprising triglycerides and 3-5% of polar compounds.
NOVELTY - A soil improvement agent comprises 10-30 wt.% yellow phosphorus slag, 3-20 wt.% humic acid, 6-12 wt.% nitrogen-fixing bacteria and its culture medium, 6-12 wt.% cellulose-decomposing bacteria and its culture medium, 3-6 wt.% vermiculite, 2-5 wt.% limestone, 6-10 wt.% perlite and 100 wt.% filler, and has pH of 9-11.    USE - Soil improvement agent is used for improving compaction and fertility of soil (all claimed) for improving crop production.    ADVANTAGE - The agent improves crop production by economical, rapid and simple method.
NOVELTY - Fungicidal composition comprises fluazinam and thiophanate-methyl at a mass ratio of 3:5.    USE - The fungicidal composition is useful for preventing and treating blight disease in crop comprising potato (all claimed).    ADVANTAGE - The fungicidal composition can be prepared with improved synergistic effect, good storage stability and without dust pollution in an eco-friendly manner, and treats blight disease with good drug resistance profile and curative effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fungicidal composition comprising adding fluazinam, thiophanate-methyl, a dispersing agent, a wetting agent, an antifreezing agent, a preservative, a defoaming agent and deionized water into a reaction container, uniformly mixing to obtain a base material, grinding the base material, adding a stabilizer to the grinded material, adjusting pH value to 5.5-6, adding a thickening agent to the mixture, and uniformly stirring.
NOVELTY - Alkannin-fatty alcohol ethoxylate complex is prepared using fatty alcohol ethoxylate, alkannin and citric acid.    USE - The alkannin-fatty alcohol ethoxylate complex is useful for preparing medicine, which is useful for treating eczema, hyperkeratosis, fungal infections of the skin, burns and hemorrhoids (all claimed).    ADVANTAGE - The alkannin-fatty alcohol ethoxylate complex is prepared by simple and convenient method. The complex preparation method is environmentally-friendly and suitable for large scale production, and reduces resource wastage.
NOVELTY - Producing alkannin polyoxyethylenesorbitan monolaurate complex using polyoxyethylenesorbitan monolaurate, alkannin and citric acid, is claimed.    USE - The method is useful for producing alkannin polyoxyethylenesorbitan monolaurate complex, which is useful for: manufacturing medicine, chemicals and intermediates to treat eczema, skin keratosis, epiphyte survival on skin, burn and hemorrhoids; and restraining malignant tumor cell in human skin (all claimed).    ADVANTAGE - The method easily produces the alkannin polyoxyethylenesorbitan monolaurate complex with high yield and reduced pollution in an eco-friendly manner, and treats eczema with good curative effect and proximity.
NOVELTY - Organic vegetable fertilizer composition comprises 30-45% maotai lees, 25-35% quail manure, 15-25% beer grain powder, 5-10% cow dung and 1-3% bioactive fungus. The organic vegetable fertilizer composition is prepared by mixing raw materials, and then bioactive fungus is added to the obtained mixture. The obtained material is fermented for 10 days, and then performing aerobic fermentation for 12 days. The obtained material is crushed, and then sieved. The obtained material is granulated to obtain the finished product.    USE - Organic vegetable fertilizer.    ADVANTAGE - The organic vegetable fertilizer is odorless.
NOVELTY - Fertilizer for Berberis virgetorum comprises 33-37 pts. wt. urea, 10-15 pts. wt. wood waste, 40-50 pts. wt. peat, 3-5 pts. wt. potato starch, 8-10 pts. wt. peanut shell, 15-17 pts. wt. calcium magnesium silicate powder, 4-6 pts. wt. lime powder, 6-8 pts. wt. lotus root starch, 12-14 pts. wt. tea waste, 2-3 pts. wt. pupa, 3.5-4.5 pts. wt. polyvinyl alcohol, 2-3 pts. wt. Celastrus powder, 0.5-0.6 pts. wt. ferrous sulfate, 0.2-0.5 pts. wt. zinc sulfate and 0.3-0.4 pts. wt. microbial fertilizer.    USE - As B.virgetorum fertilizer.    ADVANTAGE - The fertilizer is nutritious and cost-effective, and has excellent bactericidal and pesticidal activities, and reduces usage amount of fertilizer, improves soil quality and survival rate of B.virgetorum to 10.5%, and promotes yield and quality of B.virgetorum.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the B.virgetorum fertilizer which involves (a) mixing wood waste, peat, peanut shell, lime powder and calcium magnesium silicate, adding suitable amount of water, maintaining 20-35% moisture content, adding mixture into a furnace, subjecting to primary heat treatment at 120-150 degrees C for 20-30 minutes, performing calcination at 300-380 degrees C for 3-5 minutes, cooling mixture, then subjecting to secondary heat treatment at 330-350 degrees C for 5-6 minutes, cooling and grinding cooled mixture using palm oil solution containing 10-15% polyvinyl alcohol; (b) mixing potato starch and product obtained in step (a), then adding Celastrus powder, lotus root starch and tea waste, mixing uniformly and maintaining for 4-6 days, in sealed container; and (c) adding remaining raw materials in the product obtained in step (b), mixing uniformly, granulating mixture, drying granules and sieving product.
NOVELTY - Preparation of 4-(4-aminophenyl)morpholin-3-one (I) involves reducing 4-(4-nitrophenyl)morpholin-3-one (II) using anhydrous ammonium formate as a reducing agent in presence of palladium carbon catalyst.    USE - Preparation of 4-aminophenyl-morpholin-3-one used as intermediate of rivaroxaban for treating thrombotic diseases.    ADVANTAGE - The method enables preparation of 4-aminophenyl-morpholin-3-one with high purity, under mild reaction conditions, by safe, simple and environmentally-friendly process.    DETAILED DESCRIPTION - Preparation of 4-(4-aminophenyl)morpholin-3-one of formula (I) involves reducing 4-(4-nitrophenyl)morpholin-3-one of formula (II) using anhydrous ammonium formate as a reducing agent in presence of palladium carbon catalyst.
NOVELTY - Complex comprises propylene glycol polyether, alkannin and citric acid.    USE - Complex used for preparing medicine for treating eczema, skin keratinocytes, skin epiphyte, burn and hemorrhoids (claimed).    ADVANTAGE - The complex is prepared in eco-friendly manner without producing waste, and has industry application.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a complex by using a device with temperature control jacket, which is made of stainless steel or glass.
NOVELTY - Thermochemical conversion of a carbonaceous feedstock into synthesis gas mainly containing hydrogen and carbon monoxide comprises: (a) oxycombustion of carbonaceous feedstock to cogenerate electricity and heat; and (b) simultaneously co-electrolyzing water and carbon dioxide at high temperature using the generated electricity and heat.    USE - The method is useful for the thermochemical conversion of a carbonaceous feedstock, preferably lignocellulosic biomass with a moisture content of less than 50%, into synthesis gas mainly containing hydrogen and carbon monoxide (all claimed), where the synthesis gas is useful to produce liquid fuels such as Fischer-Tropsch diesel, dimethyl ether and methanol or gas such as synthetic natural gas.    ADVANTAGE - The method is capable of effectively converting carbonaceous feedstock into synthesis gas with improved energy efficiency in a cost-effective manner.
NOVELTY - A catalyst comprises metal component.    USE - Catalyst for use in composition for converting synthesis gas to carbon dioxide, methane and olefin such as ethylene, propene, 1-butene, 1-pentene, 1-hexene, 1-heptene, 2-ethyl-hexylene, 2-ethyl-heptene, 1-octene, 1-nonene and/or 1-decene (all claimed).    ADVANTAGE - The catalyst has high activity and/or conversion of syngas, and high total hydrocarbon formation yield.    DETAILED DESCRIPTION - A catalyst comprises metal component (CACBOx), where CA is cobalt-manganese component (COaMnbXd), X comprises silicon, titanium, copper, zinc, palladium or lanthanum, a is 0.8-12, b is 0.1-1 and d is 0-0.5, CB is nickel-copper-magnesium-silicon component (NieCufMghSim), e is 0.8-1.2, f is 0-1, h is 0-0.5, and m is 0-0.5, and Ox is determined by the valence requirements of the other elements present. INDEPENDENT CLAIMS are also included for the following:    (1) a catalyst composition    (2) a method for utilizing catalyst or catalyst composition.
NOVELTY - Algae are combined with a medium to form algae-containing medium, and a free-fatty acid-containing feedstock is combined with the algae-containing medium to form algae-treated feedstock. Algae are allowed to reduce the free-fatty-acid content of the algae-treated feedstock, and product is produced from the algae-treated feedstock.    USE - Method for reducing free-fatty acid content of feedstock used for producing biodiesel (claimed). The algal products include algal biomass, dry algal cells, algal proteins, algal lipids and algal carbohydrates, nutritional products, pharmaceuticals, and cosmetics.    ADVANTAGE - The method efficiently reduces free-fatty acid content of feedstock and economically produces biodiesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing biodiesel, which involves providing free-fatty acid-containing feedstock, treating the feedstock by combining algae and/or coagulant with the feedstock, separating into upper oil phase, middle phase and lower aqueous phase, collecting the upper oil phase, and producing biodiesel product from the upper oil phase.
NOVELTY - The system has an entrained gas flow gasification plant that is configured for operating under pressure up to 10 Mpa and temperatures up to 1900 degrees C. A washing column (11) follows a quencher in a path of crude gas coarsely purified in quencher. The washing column is configured to cause the crude gas to flow through a water bath (13). A washing water separator is configured for separating washing water (26) from the crude gas flow. A high-pressure injection nozzle (18,20) is configured for finely-dispersed injection of washing water that is free of solid material into crude gas.    USE - Multistage crude gas washing system for high degree separation of dust during production of crude gas rich in carbon monoxide and hydrogen for entrained flow gasification plant for reaction of ash and slag forming fuels.    ADVANTAGE - The gas purification system for an entrained flow gasification plant having the high separation rate of particles in particular fine dust with a reliable operating mode is provided. The availability of the system is improved. The erosion in the Venturi washers can be reduced.    DETAILED DESCRIPTION - The crude gas washing stage is provided with a quencher, and is configured for coarsely purifying crude gas. An injecting device (10) is provided for injecting water into the crude gas generated for coarsely purifying the crude gas, and for cooling the crude gas to a temperature between 150 and 250 degrees C and saturating the crude gas with water vapor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multistage crude gas washing system.    Injecting device (10)    Washing column (11)    Water bath (13)    High-pressure injection nozzles (18,20)    Washing water (26)
NOVELTY - The method involves adding synthesis gas with the hydrogen by electrolysis. The electrolysis is carried out as high pressure electrolysis. The electrolysis-generated oxygen is employed in the gasification to produce the synthesis gas. The hydrogen-enriched synthesis gas is subjected to the provision of liquid hydrocarbons. The liquid hydrocarbons are converted using a combustion turbine into electrical energy.    USE - Method for enriching synthesis gas generated by gasification of forest residue e.g. wood chip and agricultural residue such as straw or chaff with hydrogen using solid organic as feedstock.    ADVANTAGE - The efficiency of the high pressure electrolysis process is improved. The measurement usually made for gasification air separation for oxygen generation can be made smaller or eliminated. The synthesis can be stably operated even during power shortage. The grid stabilization is achieved. The higher degree of utilization of carbon from biomass fuels such as wood in the synthesis can be achieved. The hydrocarbon products are significantly increased in the subsequent process for processing of synthesis gas over solutions with shift process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gasification system for enriching synthesis gas generated by gasification with hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the gasification system for enriching synthesis gas generated by gasification with hydrogen.    Gasification system (100)    Gasification device (110)    Gas purification system (120)    Refining device (140)    Storage facility (150)
NOVELTY - Biomass pellet fertilizer comprises 5-10 pts. wt. bacterial enzyme preparations, 85-95 pts. wt. monosodium glutamate sludge, 25-35 pts. wt. soybean skin, 35-45 pts. wt. soybean powder, 10-15 pts. wt. potassium dihydrogen phosphate, 28-40 pts. wt. crop straw (fermented), 5-10 pts. wt. mushroom, 20-25 pts. wt. wheat bran, 15-20 pts. wt. southernwood powder, 10-15 pts. wt. cystine, 15-20 pts. wt. alginate, 5-8 pts. wt. bentonite, 5-8 pts. wt. humic acid, 2-5 pts. wt. bioregulators, 5-8 pts. wt. phytase, 5-10 pts. wt. stone powder and water.    USE - Biomass pellet fertilizer.    ADVANTAGE - The biomass pellet fertilizer can be prepared with high nutritional content in a cost-effective manner.
NOVELTY - Preparing biodiesel, comprises adding preheated oil in a first twin-screw extruder, vacuum degassing the oil in a three to four stage heating system and removing oil from water, passing obtained oil into a two to three stage heating system, dispersing obtained product, homogeneously passing oil and hydrogen into a catalytic hydrogenation interface, adding obtained product into a second twin-screw extruder, vacuum degassing the product in a nine to ten stage heating system, removing volatile gas, and passing obtained reaction product into a polyvinyl alcohol filtration membrane.    USE - The method is useful for preparing biodiesel (claimed).    ADVANTAGE - The method is capable of efficiently producing the biodiesel with improved cold flow properties, high purity and stable quality.    DETAILED DESCRIPTION - Preparing biodiesel, comprises adding preheated oil in a first twin-screw extruder at a temperature of 80-100 degrees C, 100-120 degrees C, 100-110 degrees C, 90-100 degrees C or 90-80 degrees C, a pressure of 0.5-2 MPa and a rotating speed of 200-300 revolutions per minute, vacuum degassing the oil in a three to four stage heating system and removing oil from water, passing obtained oil into a two to three stage heating system provided with a hydrogen pump and a machine head provided with a porous plate containing hydrogenation catalyst, dispersing obtained product at constant pressure, homogeneously passing oil and hydrogen into a catalytic hydrogenation interface, adding obtained product into a second twin-screw extruder at a temperature of 100-120 degrees C, 120-130 degrees C, 80-110 degrees C or 80-100 degrees C, a pressure of 2-5 MPa and a rotating speed of 50-100 revolutions per minute, vacuum degassing the product in a nine to ten stage heating system, removing volatile gas, and passing obtained reaction product into a polyvinyl alcohol filtration membrane to remove trace impurities.
NOVELTY - Bio-processing fresh tobacco leaves into organic fertilizer and biological protein using Megacephala larvae, comprises (i) taking out waste from fresh tobacco leaves, adding auxiliary material to a culture medium, adding Megacephala eggs, bio-transforming Megacephala larvae, converting tobacco leaves and auxiliary materials into organic fertilizer, allowing Megacephala larvae to grow into mature maggots, and collecting biological protein, where culture material includes fresh tobacco leaves, wheat bran, bran powder, sawdust and fish meal.    USE - The method is useful for bio-processing fresh tobacco leaves into organic fertilizer and biological protein using Megacephala larvae (claimed).    ADVANTAGE - The method produces nicotine-free products; has high utilization rate of resources, low energy consumption, and less emissions; converts waste into useful materials; occupies less working area; does not change the property of the working land, and thus it can be re-utilized; and reduces the cost of crushing process.    DETAILED DESCRIPTION - Bio-processing fresh tobacco leaves into organic fertilizer and biological protein using Megacephala larvae, comprises (i) taking out waste from fresh tobacco leaves, and adding an auxiliary material into a culture medium, then adding Megacephala eggs, allowing the eggs to hatch into Megacephala larvae, and subjecting to biotransformation, converting tobacco leaves and auxiliary materials into organic fertilizer, allowing Megacephala larvae to grow into mature maggots, and collecting biological protein, where the culture material includes 60-85 wt.% fresh tobacco leaves, 0-25 wt.% wheat bran, 5 wt.% bran powder, 5 wt.% sawdust and 5 wt.% fish meal, and the tobacco leaves are chopped into granules of diameter 2-3 cm. INDEPENDENT CLAIMS are also included for:    (1) biological proteins prepared by using fresh tobacco leaves; and    (2) organic fertilizer prepared by using fresh leaves of tobacco.
NOVELTY - A silkworm sand preparing method involves hydrolyzing silkworm dropping with hydrolysis liquid that is acetic acid-sodium acetate buffer solution, or disodium hydrogen phosphate-monosodium orthophosphate buffer solution, adding aluminum oxide and silicon dioxide to the hydrolyzed silkworm dropping, and blending mixture. The obtained dropping is dried, and biomass waste is pyrolyzed and dry distilled. The residues are collected and are mixed with the hydrolyzed silkworm dropping. Biogas is added to the obtained mixture followed by fermented and drying mixture.    USE - Method for preparing silkworm sand that is utilized as moisture absorbent.    ADVANTAGE - The method enables preparing the silkworm sand in a simple and rapid manner with easy operation, low energy consumption, high efficiency, strong adaptability and biodegradable property, controlling insects, avoiding discharge of pollutants and secondary pollution, and realizing utilization of waste resources.    DETAILED DESCRIPTION - A silkworm sand preparing method involves hydrolyzing silkworm dropping with hydrolysis liquid, where the hydrolysis liquid is acetic acid-sodium acetate buffer solution, or disodium hydrogen phosphate-monosodium orthophosphate buffer solution, adding 10-20 mass% aluminum oxide and silicon dioxide to the hydrolyzed silkworm dropping and blending the mixture at 50 degrees C. The obtained dropping is dried at 100-130 degrees C for 1-2 hours and biomass waste is pyrolyzed and dry distilled at 300-600 degrees C. The residues are collected and the residues are mixed with the hydrolyzed silkworm dropping in mass ratio of 1:1. Biogas is added to the obtained mixture and fermented anaerobically at normal temperature for 10-15 days followed by drying the mixture at 130-180 degrees C for 8-12 hours.
NOVELTY - A sodium chloride strengthened alkaline sludge fermentation method involves taking sludge SBR pilot sludge fermentation system, after water washing sludge index for sludge concentration of 9000-10000 mg/L, and pH of 7-8, applying remaining sludge to a small cast after washing SBR unit, setting small one-time dosing SBR device after sludge reaches the preset volume control reactor of 0.1-25 g/l, start agitator stirring, adding 2-4 mol/l sodium hydroxide solution in alkali agent tank, stirring in a small SBR device for 30-60 minutes, and maintaining temperature to 25 plus minus 1 degrees C and pH of 10 plus minus 0.1.    USE - Method for fermentation of sodium chloride strengthened alkaline sludge.
NOVELTY - An alcohol biodiesel contains 10-30 wt.% methanol, 15-30 wt.% methanol modifier, 10-30 wt.% fatty acid methyl ester, 0.1-1 wt.% fatty acid methyl ester modifier, and 35-50 wt.% diesel oil.    USE - Alcohol biodiesel (claimed).    ADVANTAGE - Biodiesel is clean, environment-friendly, energy-saving, and has high energy, corrosion resistance, high cetane number, good solubility, and high calorific energy. Preparation is simple, easy, and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of alcohol biodiesel which involves uniformly mixing methanol and methanol modifier at room temperature and pressure to obtain 1st mixed solution, uniformly mixing fatty acid methyl ester and fatty acid methyl ester modifier to obtain 2nd mixed solution, uniformly mixing 1st and 2nd mixed solution and diesel oil, and static aging. An INDEPENDENT CLAIM is included for preparation of alcohol biodiesel which involves uniformly mixing methanol and methanol modifier at room temperature and pressure to obtain 1st mixed solution, uniformly mixing fatty acid methyl ester and fatty acid methyl ester modifier to obtain 2nd mixed solution, uniformly mixing 1st and 2nd mixed solution and diesel oil, and static aging.
NOVELTY - An energy material is prepared by crushing coal and household waste, mixing, storing, adding sludge and oxidation bactericide, uniformly mixing, performing compression molding, stacking, and naturally drying.    USE - Preparation of energy material for coal-fired power plants.    ADVANTAGE - The method reduces coal resource depletion, and municipal solid waste disposal problem.
NOVELTY - A straw coal is prepared by collecting corn straw, weeding in soil, crushing single straw in grinder, mixing corn straw powder, peanut shell, and rice husk, milling, carbonizing in oxygen-free carbonizing furnace, adding additive, cooling, adding loess, coal slime, curing agent, and paraffin four additive mixture, mixing in mixer, extruding in molding machine having spiral blade, cooling, packaging, and air cooling.    USE - Preparation of straw coal (claimed).    ADVANTAGE - The carbonization time is short, product has good quality and purity, strong plasticity, and high calorific value, and method does not produce waste emissions.    DETAILED DESCRIPTION - A straw coal is prepared by collecting corn straw, weeding in soil at not greater than 5% processing rate, crushing single straw in grinder to obtain 200 meshes corn straw powder, mixing corn straw powder, peanut shell, and rice husk at ratio corn straw powder:peanut shell:rice husk of 8:2:1, milling to obtain 180-170 mu m meshes mixed powder, carbonizing in oxygen-free carbonizing furnace at 1000-1350 degrees C for 25-35 minutes until moisture content is 3-4.5%, adding additive, cooling to 250-300 degrees C, adding loess, coal slime, curing agent, and paraffin four additive mixture, mixing in mixer, extruding in molding machine having spiral blade at not less than 520 MPa, 380-420 degrees C, and 1.6-1.8 ton/m3 extrusion mass density, cooling, packaging, and air cooling.
NOVELTY - A garbage molding fuel is prepared by collecting garbage, removing inorganic substances to prevent possible explosion, removing garbage with high volume and length, compact rolling, crushing, drying in baking furnace, heating at high temperature, continuously heating to 200-300 to melt plastic components, uniformly stirring, molding at high temperature, and hardening to obtain fixed shape while using molding trash section as fuel in baking furnace.    USE - Preparation of garbage molding fuel (claimed).    ADVANTAGE - The method has automatic mechanical processing thus preventing human injury, and conserves external energy supply.
NOVELTY - Biodiesel production involves mixing high acid number oils with glycerol as reactant feedstock, and ionic liquid as catalyst for esterification reaction in a container. The esterification reaction is performed in the sealed container to obtain glycerol product. The obtained glycerol product is separated by adding a basic catalyst, and then treated with a mixture of methanol, isopropanol and isobutanol to perform transesterification reaction to give a fatty acid ester product. The obtained fatty acid ester product is separated by distillation to obtain the biodiesel.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method produces biodiesel has low acid value, low condensation point in a simple and eco-friendly manner.
NOVELTY - Method of treating non-human animal infested with biting lice, involves internally administering neonicotinoid to the animal such that the neonicotinoid is present systemically within the animal.    USE - The method is useful for treating non-human animal infested with biting lice, preferably Bovicola ovis in animal, preferably sheep (all claimed).    ADVANTAGE - The method reduces mortality rate of the sheep, does not cause detrimental effects on host animal, is cost-effective, less labor intensive, environmentally-friendly and safe for persons, and minimizes insecticide residues in fleece which reduces risks in wool processing.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) applicator designed for internal administration comprising 2-89 weight/volume% neonicotinoid; and    (2) dosage regime for treating non-human animal infested with the biting lice, involves administering neonicotinoid internally at a dose of 40 mg/kg or less of the animal.
NOVELTY - Fuel composition (208) comprises: a fuel component; an alcohol component; a water component; a microemulsion blend (206) comprising at least one of lower grade fatty acid derivatives that are present in an amount effective for the fuel, alcohol and water components to form the microemulsion blend; and a cetane-enhancer component.    USE - The fuel composition is useful in internal-combustion engines (claimed).    ADVANTAGE - The fuel composition: exhibits high purity; and can be prepared in a cost effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for formulating (200) the fuel composition for use in internal-combustion engines, comprising: providing the fuel; and forming the fuel composition by adding the microemulsion blend to the fuel, where the microemulsion blend includes mixture of oleic acid, ethanol, ammonia, water and cetane enhancer.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a method for formulating a fuel composition.    Formulating fuel composition (200)    Crude oil (202)    Straight run diesel (204)    Micro- emulsion blend (206)    Fuel composition (208)
NOVELTY - Carp feed comprises 40-50 pts. wt. soybean meal, 3-5 pts. wt. full cream rice bran, 10-15 pts. wt. distillers dried grains (DDG), 5-8 pts. wt. peanut cake, 3-5 pts. wt. corn meal, 10-15 pts. wt. rapeseed meal, 3-5 pts. wt. fish meal, 1-1.5 pts. wt. monocalcium phosphate, 0.15-0.2 pts. wt. L-lysine, 0.01-0.02 pts. wt. allicin, 1-3 pts. wt. active enzyme, and 1-2 pts. wt. salt.    USE - The carp feed is useful for improving fish immunity.    ADVANTAGE - The carp feed: is balanced with nutritional components; and reduces the plant diseases and insect pests. The method is clean and environmentally friendly, which does not produce any pollutants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the carp feed, comprising (i) pre-mixing the soybean meal, full-cream rice bran, DDG, peanut cake, corn meal, rapeseed meal, fish meal and salt, and stirring at room temperature for 20-30 minutes under stirring speed of 1500-2000 rotations/minute (rpm) to obtain a premix; (ii) subjecting the premix to superfine crushing to obtain superfine premix having particle size of 80-100 meshes; and (iii) adding the superfine premix with the monocalcium phosphate, L-lysine, allicin and active enzyme, and stirring for 20-30 minutes under stirring speed of 1500-2000 rpm.
NOVELTY - Methanation catalyst comprises 10-80 wt.% nickel active ingredient, 0.1-15 wt.% modified additive, 20-75 wt.% carrier, and 0.01-10 wt.% template.    USE - The methanation catalyst is useful for converting coal to substitute natural gas (claimed).    ADVANTAGE - The catalyst has mesoporous pore structure, large specific surface area and low resistance gas diffusion, low activity, high-temperature hydrothermal stability, anti-coking properties, reaction temperature zone width (220-700 degrees C) and raw gas adaptability characteristics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the methanation catalyst, comprising (a) formulating nickel active ingredient and modified additives soluble salt into a mixed solution, then co-precipitating using sodium hydroxide, sodium bicarbonate, sodium carbonate, potassium carbonate or ammonia as the precipitating agent, and washing to obtain parent catalyst; (b) mixing alumina, magnesia, silica, calcium oxide, zirconia, pseudo-boehmite and/or aluminum magnesium spinel, and ball milling; (c) mixing the templating agent ethylene diamine, n-butylamine, pyrrolidine, cellulose, P123, cetyl trimethyl ammonium bromide (CTAB), triisopropylbenzen and/or trimethylbenzene into a mixed solution, and fully dissolving it completely; and (d) adding the powder component of (b) and mixed solution of step (c) into parent catalyst, beating, filtering, drying, roasting, and compression molding.
NOVELTY - High-flash point alcohol ether diesel oil comprises 5-15 %mass mixed alcohol, 1-18 %mass polyoxymethylene dimethyl ether, 0.03-1 %mass glycol ether, 0.05-0.3 %mass additive and remainder of diesel oil. The mixed alcohol is formed by uniformly mixing 20-25 pts. wt. 2-pentanol, 5-8 pts. wt. n-butanol, 15-20 pts. wt. 2-methyl butanol, 8-12 pts. wt. cyclopentanol, 27-32 pts. wt. n-pentanol and 10-15 pts. wt. 2-hexyl alcohol. The additive includes mixture of acetamide, 1,2,3-triazole and berberine in mass ratio 0.75-1:1:0.25-0.5.    USE - High-flash point alcohol ether diesel oil (claimed).    ADVANTAGE - The high-flash point alcohol ether diesel oil has excellent storage stability, reduces emission, and is safe and environmentally-friendly.    DETAILED DESCRIPTION - High-flash point alcohol ether diesel oil comprises 5-15 %mass mixed alcohol, 1-18 %mass polyoxymethylene dimethyl ether (DMMn, where n is 3-8), 0.03-1 %mass glycol ether, 0.05-0.3 %mass additive and remainder of diesel oil. The mixed alcohol is formed by uniformly mixing 20-25 pts. wt. 2-pentanol, 5-8 pts. wt. n-butanol, 15-20 pts. wt. 2-methyl butanol, 8-12 pts. wt. cyclopentanol, 27-32 pts. wt. n-pentanol and 10-15 pts. wt. 2-hexyl alcohol. The additive includes mixture of acetamide, 1,2,3-triazole and berberine in mass ratio 0.75-1:1:0.25-0.5. The high-flash point alcohol ether diesel oil has flash point of 55 degrees C or more.
NOVELTY - M5-M25 methanol gasoline fuel complex additive comprises 22-36% alcohol mixture, 12-24% ester mixture, 14-28% ether mixture, 13-24% aromatic hydrocarbon mixture, 4-8% dimethoxytetrahydrofuran, 2-6% alkenyl succinic acid, 2-6% polylysine, 3-6% 2,4-dimethyl-6-tert-butylphenol, 1-8% tetraethylenepentamine and 2-5% 2-methyl benzothiazole.    USE - Used as M5-M25 methanol gasoline fuel complex additive.    ADVANTAGE - The additive: can be used at high temperature conditions without air resistance phenomenon; can maintain transparent clarified state and non-stratified state; and is stable, and convenient to store and use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for M5-M25 methanol gasoline comprising the complex additive as mentioned above.
NOVELTY - A compression granulator comprises a packing auger (1), an auger mounting cylinder, and a granulation gear (3). The packing auger is mounted in an inner packing auger mounting cylinder end side wall set with a feeding port (21) and a discharge bracket (32). The discharge bracket is set with two elastic pressing plates (4), and a rotating shaft (11).    USE - A compression granulator used for hay and straw powder.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the compression granulator.    Packing auger (1)    Granulation gear (3)    Elastic pressing plates (4)    Rotating shaft (11)    Feeding port (21)    Discharge bracket (32)
NOVELTY - Sustained- or controlled-release capsule material comprises first component and second component. The first component comprises 38-42 %mass soybean oil, 28-32 %mass cashew nutshell liquid, 18-22 %mass calcium stearate and 8-12 %mass alcohol. The second component comprises 48-52 %mass epoxidized soybean oil, 28-32 %mass methanol, 13-17 %mass brightening agent and 3-7 %mass ethyl acetate.    USE - The sustained- or controlled-release capsule material is useful in preparation of sustained- or controlled-release fertilizers (claimed) which are used for crops.    ADVANTAGE - The sustained- or controlled-release capsule material prolongs effect of fertilizer, and increases yield of crops. The method is environmentally-friendly, and performed simply and cost-effectively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) for preparing the sustained- or controlled-release capsule material, involves (a) sequentially adding the soybean oil, calcium stearate, alcohol and cashew nutshell liquid to a first reaction kettle, and reacting obtained mixture to obtain first component, and (b) sequentially adding the epoxidized soybean oil, methanol, brightening agent and ethyl acetate to a second reaction kettle, and reacting obtained mixture to obtain second component; and    (2) method (M2) for preparing the sustained- and controlled-release fertilizers using the sustained- and controlled-release capsule material, involves adding the fertilizer to the sustained- and controlled-release capsule material, uniformly stirring obtained mixture, canning the mixture, and solidifying the mixture.
NOVELTY - Co-producing natural gas and methanol involves removing impurities from coal coke furnace and then compressing the mixed gas for synthesizing methanol. The methanol synthesis gas mixture is entered into systemic circulation system and then the obtained material is entered into methanol separator. The obtained material is flash evaporated in methanol rectifying system and then the separated material is entered into recycle compressor cycle. The small part of methanol is entered into methanol synthesis purge system and then the obtained material is not discharged directly in the methanation.    USE - Method for co-producing natural gas and methanol (claimed).    ADVANTAGE - The method enables to co-produce natural gas and methanol has achieved best utilization of carbon and hydrogen gas.    DETAILED DESCRIPTION - Co-producing natural gas and methanol involves removing impurities from coal coke furnace and then compressing the mixed gas for synthesizing methanol. The methanol synthesis gas mixture is entered into systemic circulation system and then the obtained material is entered into methanol separator. The obtained material is flash evaporated in methanol rectifying system and then the separated material is entered into recycle compressor cycle. The small part of methanol is entered into methanol synthesis purge system and then the obtained material is not discharged directly in the methanation device. The first-stage methanation reactor is connected with level circulation compressor and the methanation device for performing the reaction of carbon monoxide and carbon dioxide. The deflated main component is methane, carbon, hydrocarbons, hydrogen and nitrogen and then the released gas is dehydrated. The dehydrated material is subjected to membrane separation to obtain respectively liquefied natural gas or compressed natural gas.
NOVELTY - An expression carrier comprises (i) a protein comprising a defined sequence of 411 or 445 amino acids (SEQ ID NO. 1 or 2), given in the specification, and (ii) a protein comprising an amino acid sequence of SEQ ID NO. 1 or 2 having one or more amino acid substitution, deletion or addition, is new.    USE - The expression carrier, host cell and protein are useful for producing biofuel. The biofuel is ethanol, acetone or butanol (all claimed).    ADVANTAGE - The expression carrier, host cell and protein are used for rapid biofuel production with high yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a host cell comprising the expression carrier above;    (2) a protein for producing biofuel, selected from (i) a protein comprising an amino acid sequence of SEQ ID NO. 1 or 2, and (ii) a protein comprising an amino acid sequence of SEQ ID NO. 1 or 2 having one or more amino acid substitution, deletion or addition; and    (3) a method for producing biofuel by culturing the host cell of (1) and obtaining the biofuel.
NOVELTY - Use of dead animal fats for producing biodiesel by adding acid or alkaline substance and dead animal fat solution into a closed container, uniformly mixing, performing acidolysis method, adding dead animal protein and amino acid compound to the mixture, completely hydrolyzing the mixture, collecting supernatant, adding low molecular weight aliphatic diol compounds and fatty acid to the supernatant, uniformly mixing, adding catalyst to the mixture, heating the mixture at 65 degrees C for 1.5 hours, and uniformly stirring, is claimed.    USE - The dead animal fats are useful for producing biodiesel and for preparing amino acid fertilizer (all claimed).    ADVANTAGE - The dead animal fats are capable of producing biodiesel with high efficiency, with a conversion rate of more than 97%.    DETAILED DESCRIPTION - Use of dead animal fats for producing biodiesel by adding acid or alkaline substance and dead animal fat solution into a closed container, uniformly mixing, performing acidolysis, adding dead animal protein to the mixture, completely hydrolyzing the mixture, collecting supernatant, adding low molecular weight aliphatic diol compounds to the resulting fatty acid at a molar ratio of 1: 7 and a volume ratio of 4:1 to the supernatant, uniformly mixing, adding 1 wt.% of a catalyst to the mixture, heating the mixture at 65 degrees C for 1.5 hours and uniformly stirring the heated mixture.
NOVELTY - Preparing wild rape seed biological diesel oil comprises mixing wild rape seed oil and methanol with a mass ratio of 1:0.436-0.546, adding 7-9 wt.% of solid sodium bisulfate as catalyst to the wild rape seed oil, placing the mixture in an oil bath at 110-130 degrees C under stirring to react for 12-15 hours.    USE - The method is useful for producing wild rape seed biological diesel oil (claimed).    ADVANTAGE - The method produces biological diesel oil with yield of 98.06%, in a simple, cost-effective and eco-friendly manner, and can satisfy diesel fuel blend with biological diesel oil (BD100) national standard.
NOVELTY - Cellulosic biomass pyrolysis using eutectic solvent involves (a) mixing highly polar polyol and alkali metal carbonate, in molar ratio of 5:1-10:1, and heating mixture at 80-100 degrees C for 0.5-2 hours to obtain a uniform clear solution, and (b) adding the clear solution with processed cellulosic biomass, heating at 130-180 degrees C for 1-6 hours, and separating glucose-polyol solution for producing ethanol by fermentation.    USE - The cellulosic biomass pyrolysis method using eutectic solvent is useful for producing ethanol (claimed).    ADVANTAGE - The method is simple, cost-effective and suitable for large scale ethanol production, and significantly degrades cellulosic biomass.
NOVELTY - This utility new type provide the a one a biological diesel oil leftovers glycerol of rear processing device, comprising glycerol tank, the glycerol tank rear quantitative pump through a treatment reaction tank, concentrated sulfuric acid tank rear sulphuric acid metering pump through a treatment reaction tank, a reaction tank through second rear quantitative pump a glycerol neutralizing tank, a rear reaction tank at the same time a acidification tank, neutralizing tank set with alkali liquor device, vacuum dewatering device, neutralizing tank through third quantitative pump a crude glycerine tank, rear reaction tank is set with a stir motor in rear reaction tank set with a sulphuric acid distributor, neutralizing tank top part set with a second stir motor, rear treatment reaction tank lower part set with a air device. It fills the rear in lower foot material without glycerol in biological diesel production process, use rear glycerol treatment device, a biological diesel oil in a link process, increase yield and purity glycerine, increase yield, reduce the production cost and the purpose of benefit.
NOVELTY - Composition comprises zeolite, active carbon, aluminum oxide and graphite powder.    USE - The composition is useful for micro-porous material to absorb natural gas (claimed).    ADVANTAGE - The micro-porous material has high surface area utilization ratio, two-dimensional plane structure, excellent physical and chemical properties, and high natural gas absorbing rate.
NOVELTY - Alcohol based biofuel comprises 30-50 vol.% methanol or ethanol, 0.1-0.3 vol.% corrosion inhibitor, 6-17 vol.% plant oleic acid, 5-24 vol.% higher alcohol mixture, 10-20 vol.% waste oil, 1-7 vol.% ethyl acetate, and additive (balance).    USE - Used as alcohol based biofuel.    ADVANTAGE - The biofuel solves physical and chemical property index which does not completely meet requirements for engine use, thus having large physical and chemical property index difference of vehicle diesel oil; saves the national petroleum resource; is environmentally friendly; saves energy; increases calorific value of methanol; solves the pollution problem; avoids discharging of gas harmful to human body; has good lubricating property and prolongs the use life of engine fuel injection system; has high reproducibility; does not need to be changed in the original device working state, thus directly replacing petroleum oil; does not get layered on long-term storage; and does not deteriorate and cause turbidity.
NOVELTY - An additive contains 50-80 wt.% ammonium polyphosphate salt, 0-50 wt.% magnesium residue, 0-50 wt.% carbide residue, 0-50 wt.% red mud, and 0-50 wt.% blast furnace residue in which ammonium polyphosphate salt is ammonium polyphosphate, ammonium dihydrogen phosphate, or diammonium phosphate, magnesium residue contains calcium oxide, silicon dioxide, aluminum oxide, magnesium oxide, and ferric oxide, carbide residue contains calcium oxide, silicon dioxide, aluminum oxide, and ferric oxide, and red mud contains calcium oxide, silicon dioxide, and aluminum oxide.    USE - Additive for biomass solid fuel (claimed).    ADVANTAGE - Additive has improved ash fusibility and low cost.    DETAILED DESCRIPTION - An additive contains 50-80 wt.% ammonium polyphosphate salt, 0-50 wt.% magnesium residue, 0-50 wt.% carbide residue, 0-50 wt.% red mud, and 0-50 wt.% blast furnace residue in which ammonium polyphosphate salt is ammonium polyphosphate, ammonium dihydrogen phosphate, or diammonium phosphate, magnesium residue contains calcium oxide, silicon dioxide, aluminum oxide, magnesium oxide, and ferric oxide, carbide residue contains calcium oxide, silicon dioxide, aluminum oxide, and ferric oxide, red mud contains calcium oxide, silicon dioxide, aluminum oxide, magnesium oxide, ferric oxide, and titanium dioxide, and blast furnace residue contains calcium oxide, silicon dioxide, aluminum oxide, magnesium oxide, manganese oxide, and iron(II) oxide. An INDEPENDENT CLAIM is included for application for biomass solid fuel which involves grinding additive into 200-400 mesh powder and mixing in biomass raw material in which added amount of additive is 0.5-9 wt.%.
NOVELTY - Method for purification of amino acids, polypeptides and other water-soluble substances involves adjusting pH of crude aqueous solution comprising amino acids and/or polypeptides to a predetermined value, and allowing precipitation of target amino acids and/or polypeptides in the solution in presence of organic solvent and conversion of impurity substances with similar solubility to different products.    USE - The method is useful for purification of amino acids, preferably water-soluble amino acids chosen from natural and non natural amino acids, and polypeptides chosen from soluble glycyl-L-glutamine dipeptide, N-glycyl-L-tyrosine dipeptide, L-alanyl-L-glutamine dipeptide, and other water-soluble substances (all claimed).    ADVANTAGE - The method is simple to operate, cost-effective, environmentally-friendly and suitable for large-scale industrial production, enables efficient separation of high purity water-soluble amino acids and peptides and other substances from the crude solution without affecting their physical properties, consumes less time, and requires organic solvent in lesser amount.
NOVELTY - The machine comprises a cylindrical cylinder, a pressing block and biomass fuel. The biomass fuel comprises 20-30 wt.% of waste mushroom, 12-18 wt.% of walnut, 12-18 wt.% of dogwood seed, 15-25 wt.% of peanut shell, 10-15 wt.% of almond shell, 1-5 wt.% of sawdust, 1-5 wt.% of wood and 3-8 wt.% of forest waste material.    USE - The machine is useful for thermally cracking and gasifying biomass fuel (claimed).    ADVANTAGE - The machine greatly increases the production speed and production rate, increases the intensity of biomass fuel and reduces the molding pressure of fuel, thus avoiding unnecessary energy loss, and saves the production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the biomass fuel.
NOVELTY - Special fertilizer comprises 25-35 pts. wt. chicken manure, 8-12 pts. wt. plant ash, 4-6 pts. wt. oil cake fertilizer, 9-12 pts. wt. calcium magnesium phosphate fertilizer, 0.01-0.05 pts. wt. boron fertilizer, 0.04-0.08 pts. wt. zinc fertilizer and 40-50 pts. wt. crop straw.    USE - The special fertilizer is useful for promoting crop growth and increasing photosynthetic utilization rate.    ADVANTAGE - The special fertilizer reduces dosage of pesticides and is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves cutting rice straw into 3 cm long pieces and mixing with chicken manure, plant ash, oil cake fertilizer, calcium magnesium phosphate fertilizer, boron fertilizer and zinc fertilizer, forming pile like structure of the mixture and fermenting mixture for 6 months by turning pile once in every 2 months.
NOVELTY - The system has a pre-processor (18) connected with an outlet anaerobic fermentation tank (2) and a sludge conveying part of a sludge pump (1). A biogas outlet connecting tank (17) is connected with a rear combustion engine (16). A smoke outlet of the combustion engine is connected with a waste heat boiler (14). The anaerobic fermentation tank is connected with a dehydration machine (3). A level drying machine (6) is connected with a dryer heat supply source that is connected with the biogas outlet connecting tank.    USE - Two-level sludge drying system.    ADVANTAGE - The system reduces energy consumption and sludge treatment defects, satisfies power grid electric power requirements, realizes two-level sludge drying process, increases sludge drying speed and occupies less space.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a two-level sludge drying system.    Sludge pump (1)    Outlet anaerobic fermentation tank (2)    Dehydration machine (3)    Level drying machine (6)    Waste heat boiler (14)    Rear combustion engine (16)    Biogas outlet connecting tank (17)    Pre-processor (18)
NOVELTY - A bromine sodium diclofenac sesquihydrate is prepared by adding bromfenac sodium and antioxidant in mixed solvent of water and organic alcohol, heating, dissolving, adding pH adjusting agent to adjust pH to 7-10.5, adding anti-solvent, cooling at 30-35 degrees C, adding bromfenac sodium monohydrate, bromfenac sodium sesquihydrate, or their mixtures as seed crystal, stirring, cooling, crystallizing, collecting crystals, and drying.    USE - Preparation of bromine sodium diclofenac sesquihydrate (claimed).    ADVANTAGE - Preparation process is simple, easy, and environment-friendly and has mild reaction conditions and low discharge. Product has high purity.    DESCRIPTION OF DRAWING(S) - The drawing shows a high-performance liquid chromatography graph of a bromine sodium diclofenac sesquihydrate. (Drawing includes non-English text).
NOVELTY - The method involves carrying out dehydration treatment by biomass raw material to reduce total water content for 30 percentage in normal pressure, where the biomass raw material includes firewood, marsh gas, hull, straw, wheat straw and organic waste. Pyrolysis reaction is carried out by the biomass raw material such that is raw material is converted into gas product and solid product that are separated by using a reaction system. Decomposing is carried out by gas reaction product to reduce heat of the product. The gas reaction product is converted into first catalyst and second catalyst.    USE - Air-cooled biomass catalytic pyrolysis reaction method.    ADVANTAGE - The method enables performing solution reaction process by first catalyst and second catalyst, so that tar accumulation can be eliminated, thus increasing yield of hydrogen in gas product. The method enables reducing pollution and smoke dust in a cost-effective manner so as to increase energy utilization rate, thus realizing catalytic pyrolysis reaction process with wide market prospect.    DETAILED DESCRIPTION - The gas reaction product comprises hydrogen, lower carbon monoxide and carbon dioxide.
NOVELTY - Biodiesel additive comprises 18-28 pts. polymethylmethacrylate, 3-8 pts. polydecene, 5-10 pts. dodecyl trimethyl ammonium chloride, 2-5 pts. maleic anhydride, 3-6 pts. dodecyl methacrylate, 2-5 pts. diethyl phthalate and 15-18 pts. dialkyl naphthalene.    USE - Used as biodiesel additive.    ADVANTAGE - The additives is environmentally-friendly, reduces the cold filter plugging point of biodiesel, improves flowability, inhibits the breeding of germs and bacteria during long-term storage of biodiesel under hot and humid environment, and does not require condensing-separation, crystalline distillation and other treatments.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing biodiesel additive, comprising adding polymethylmethacrylate, polydecene, dodecyl trimethyl ammonium chloride and maleic anhydride into a reactor, stirring, heating to 80 degrees C under ultrasonic environment for 95 minutes, naturally cooling, sequentially and slowly adding sodium dodecyl methacrylate, diethyl phthalate and dialkyl naphthalene, heating to 65 degrees C with a pressure of 0.9 MP under ultrasonic environment for 30 minutes, naturally cooling, allowing to stand and collecting the supernatant.
NOVELTY - An alcohol base gasoline solubilizer comprises 13-16 wt.% toluene, 13-18 wt.% sec-butyl acetate, 10-15 wt.% isopropanol, 15-20 wt.% tert-butanol, 0.3-0.8 wt.% ethanolamine, 5-10 wt.% methylal, 5-8 wt.% glycol, 15-20 wt.% 2-methyl-2-pentanol, 0.5-1 wt.% phthalate ester and 15-20 wt.% oleic acid.    USE - Alcohol base gasoline solubilizer.
NOVELTY - Carbon-dioxide enrichment and methanation of confined space, comprises converting carbon-dioxide to methane by carrying out methanation of carbon-dioxide in presence of hydrogen, and supplying hydrogen and oxygen into the confined space which is produced by electrolysis of water, and periodically carrying out carbon-dioxide enrichment and carbon-dioxide methanation, after complete conversion of carbon-dioxide.    USE - The method and reactor are useful for underwater diving device or space station (chamber) in effective removal of carbon-dioxide in low gas concentration (claimed).    ADVANTAGE - The method effectively controls the carbon-dioxide content in the confined space; provides required oxygen to survive; carries out the process in a single step so as to simplify the carbon-dioxide removal process in the confined space; and protects human life in space station or underwater diving device while working, and thus it guarantees security of life and property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a methanation reactor to carry out the above process, comprising a reactor integrated with carbon-dioxide enrichment process and methanation reaction process, where the reactor includes a heat exchange chamber, a carbon-dioxide enrichment chamber, an electric heating start chamber, and a methanation reaction chamber provide with multi-cavity layer, and the heat exchange chamber, carbon-dioxide enrichment chamber, electric heating start chamber and methanation reaction chamber, used for continuously purifying the gas, by alternately feeding gas into different cavity while pre-heating the raw materials, and cooling the gas product to carry out carbon-dioxide enrichment and dissociation processes.
NOVELTY - Anaerobic fermentation involves crushing pole. The crushed product is added with inoculant strain. The mixture is fermented at 60-70 degrees C for 48-72 hours. the fermented mixture is added with livestock excrement. The mixture is stirred to obtain desired product.    USE - Method for anaerobic fermentation for producing biogas using straw pole (claimed).    ADVANTAGE - The method is stable and efficient.
NOVELTY - A biomass pyrolysis gasification multifunctional iron-based catalyst comprises 5-15 pts. wt. ferric oxide, 8-13 pts. wt. cerium oxide, 7-12 pts. wt. zirconium oxide, and 60-80 pts. wt. calcium oxide.    USE - Biomass pyrolysis gasification multifunctional iron-based catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of iron-based catalyst comprising adding calcium oxide into muffle furnace, calcining, grinding, and screening to obtain 10-200 meshes carrier; mixing with ferric nitrate nonahydrate solution, drying to remove water, calcining, cooling, grinding, and screening; mixing with cerium nitrate hexahydrate solution, stirring, drying to remove water, calcining, cooling, grinding, mixing with zirconium nitrate pentahydrate, drying to remove water, calcining, cooling, molding, and grinding; and molding and sieving through 30-40 meshes.
NOVELTY - The kettle (14) has horizontal cylindrical casing (10) whose outer wall is sleeved with the circumference gear (9) and small gear (5) which is connected to relative speed regulating motor (6). The small gear is configured to drive the circumferential gear, so as to rotate the casing. A feeding cabin (15) is attached to one end of casing, while the material discharging chamber (18) is attached to other end of casing. A thermometer (22) is attached to discharging chamber, while pressure sensor (23) is attached to the feeding cabin.    USE - Coal pyrolysis organic waste or garbage rotating reaction kettle.    ADVANTAGE - The coal pyrolysis organic waste or garbage can be rotated and treated efficiently in the reaction kettle. The stir conveyor can efficiently convey the waste material from feeding cabin to discharging chamber. The deformation of kettle can be avoided and the sealing property of the kettle can be improved.    DETAILED DESCRIPTION - A stir conveyor (24) arranged inside the casing, is configured to connect the feeding cabin and material discharging chamber. The top side of discharging chamber is provided with a gas phase product exit (13). The center of discharging chamber is provided with horizontal spiral discharging machine containing discharge hole.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the coal pyrolysis organic waste or garbage rotating reaction kettle. (Drawing includes non-English language text)    Small gear (5)    Relative speed regulating motor (6)    Circumference gear (9)    Horizontal cylindrical casing (10)    Gas phase product exit (13)    Coal pyrolysis organic waste or garbage rotating reaction kettle (14)    Feeding cabin (15)    Material discharging chamber (18)    Thermometer (22)    Pressure sensor (23)    Stir conveyor (24)
NOVELTY - Preparation of aryl or heteroaryl tert-butyl ester compounds comprises adding aryl- or heteroaryl-boric acid compound to solvent. Palladium catalyst and ligand are added to resulting mixture to obtain mixture (A). Mixture (A) is heated to 60-110 degrees C, reacted, and the resulting mixture is cooled to room temperature for 13-17 hours to obtain mixture (B). The resulting mixture (B) is diluted with ethyl acetate, filtered, filtrate is collected, concentrated and spin-dried.    USE - Preparation of aryl- or heteroaryl tert-butyl ester compound (claimed).    ADVANTAGE - The method provides non-toxic aryl- or heteroaryl tert-butyl ester compounds having excellent stability and high safety under mild reaction conditions by a simple, economical and environmentally-friendly process.
NOVELTY - The device has a low temperature condenser that is installed at a top of a thermal regeneration tower (1). A gas outlet at a top of the tower is communicated with a gas phase separator (5) through a water cooler (2). A gas phase outlet of the separator is communicated with a methanol water scrubber, and liquid phase outlets (103,104) are communicated with a liquid phase delivery pipe. A gas phase outlet is formed in the top of an alcohol amine-separating tower, and a liquid phase outlet is formed in the bottom of the alcohol amine-separating tower.    USE - Device for treating low temperature methanol washing ammonium crystallization and purifying barren liquor methanol.    ADVANTAGE - The condenser and the pipe at the top of the thermal regeneration tower are blocked due to ammonium bicarbonate crystallization, and the treatment of methanol discharged intermittently, thus the barren liquor methanol is purified, and the methanol consumption is reduced. The safety, reliability and stability of the low temperature methanol-washing device are improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for treating low temperature methanol washing ammonium crystallization and purifying barren liquor methanol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic explanatory view illustrating the process for treating low temperature methanol washing ammonium crystallization and purifying barren liquor methanol.    Thermal regeneration tower (1)    Water cooler (2)    Gas phase separator (5)    Primary liquid phase outlet (103)    Secondary liquid phase outlet (104)
NOVELTY - This utility new type claims a one biomass gasification tar catalytic splitting reactor, comprising reactor shell and set on a catalyst reactor shell, reactor shell inner end set with two corresponding to the air inlet pipe and the pneuma of pipe, a catalyst comprising a cylindrical catalyst carrier, catalyst carrier has a multi-interval arrangement along the length direction in parallel set with a through hole, a tar splitting catalyst up the hole of inner wall of each through hole, the inner tar catalytic splitting reactor in high temperature gas through the air inlet pipe entering into reactor shell, high temperature gas with a tar time of the catalyst carrier of inner through hole through the upper hole wall of the effect of splitting catalyst low tar, tar splitting is small molecule and other combustible fuel a small molecule, and a tube through the outlet, makes full use of a tar-containing a heat, increase biomass gasification efficiency.
NOVELTY - This utility new type claims a one application directly on the ozone ditch sewage river wetland of water source water treatment system, which is mainly composed by a one or a multi-carrier platform, a carrier platform comprising building structure (1), deposition pool (2), filter carrier (3) and discharge space (4) and the water outlet (5), a building structure (1) composed of a deposition pool (2) filter carrier (3) and discharge space (4) and the water outlet (5). Deposition pool (2) is located in the water inlet at the upstream carrier platform of front half part, a water space (4) and the water outlet (5) is located in the carrier platform rear semi-part of a filter carrier (3) of middle part. This utility new type simple and efficient, saving energy and water, it is easy to maintain, have less investment and take effect fast, which ensures , benefiting the nation and the people, the nation, son, like the water well of modified the stand is lying down for people water the water of descendant we can be from in.
NOVELTY - This new utility model claims of one of more gallery channel embedded filtering wall biological film sewage processor, this processor is of water collecting system, one level gallery channel, second level gallery channel, the third level gallery channel connected in series in turn, one level gallery channel and the third level gallery comprises biological filtering wall, upper wall of filter hole, the aperture of hole from upper to lower gradually change large, two of biological filtering wall and hole in all filling ceramic ring filler, and the third one gallery and cloth with biological suspension ball filler and micro-pore aerator. The utility model use new micro-pore aeration, baffle plate and installation using water flow slow line flow, which is good for slow growing nitration fungus growth and breeding, forming biological film, using biological filtering wall is set with transition zone of different function, avoid of microorganism is different variety, especially autotrophic microorganism is eliminated and on competing. This new utility model embedded biological filtering wall is set with micro-aeration system before and in denitrification gallery channel, microorganism can effective increase the biological membrane and nitrification-denitrification ability.
NOVELTY - This utility new type relates to a one cultivation sewage treatment of biological fermentation separate device. The existing cultivation excrement is not processing, directly discharging pollution environment affect health of people, the utility model is a new target for cultivation waste is one prepared using a multi-stage biological treatment container (3), (6), (10) and stir the fermentation container (20) a sedimentation purification, fermentation of water separate rear processing, processing a circulation, feces into biological organic fertilizer, changes waste into valuable, reduces the pollution and reduces the cultivation cost benefit, which is good for promoting the sustainable development of animal husbandry.
NOVELTY - This utility new type relates to a microorganism one electrolysis pool with the duckweed culture is combine resources processing organic waste water of device, comprising the electrolytic pool and microorganism light biological reactor a two unit, microorganism electrolytic pool comprising microorganism electrolysis pool shell, set with said organic sewage flow change of baffle plate, an anode electrode and a cathode electrode on the microorganism electrolysis pool inner shell, a microorganism cell pool and light biological reactor connected, a rear organic sewage by a microorganism electrolytic pool enters the light biological reactor, inner said light biological reactor with culture. This utility new type at the same time overcomes a time by using a microorganism electrolytic pool and processing organic waste water the duckweed, it not only increase the treatment effect of sewage, and obtaining a biological fuel and biomass can be a compensation sewage treatment cost, and is a valid processing organic sewage supply the new way for energy saving and emission reduction and environment of important significance.
NOVELTY - An agent is obtained by mixing and culturing 150-250 pts. wt. yeast, 400-600 pts. wt. photosynthetic bacteria, 1-5 pts. wt. Bacillus natto, 1-5 pts. wt. B.licheniformis, 1-5 pts. wt. Actinomycetes and 1-5 pts. wt. Lactobacillus at 36-38 degrees C for 6-8 days.    USE - Agent for use in deodorizing microorganism inoculum in municipal garbage and water source (claimed).    ADVANTAGE - The agent has mutual synergistic effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the above-mentioned agent, which involves preparing culture tank, adding culture medium to the tank, stirring the culture medium with pure water at 37-38 degrees C for 10 minutes to obtain culture liquid, and taking some culture liquid as nutrition liquid. The nutrition liquid is activated by adding yeast, photosynthetic bacteria, B.natto, B.licheniformis, Actinomycetes and Lactobacillus to culture tank, stirring the mixture for 10-20 minutes and culturing the mixture at 36-38 degrees C for 6-8 days.
NOVELTY - Invention relates to electrolysis installation for space purposes, including electrolysis module with output pneumatic mains of oxygen and hydrogen, provided with vapour condensers, made of porous hydrophilic material and having water discharge into the environment, reservoir with water, provided with temperature sensor and hydraulically connected with electrolysis module and working under excess pressure, gas balloon system of oxygen and hydrogen storage with pneumatic mains of said gases output with lock elements, which has, at least two successively balloons for each of gases connected to each other via pneumatic mains, with pressure sensors, installed on balloons; as well as system for control of parameters, connected to said sensors, sensor of external pressure and temperature sensor. Vapour condensers are connected with reservoir with water via hydromains with lock elements, and inserts of porous hydrophilic material for accumulation of condensate, are placed inside balloons, with balloons themselves being provided with hydromains to control accumulated in inserts condensate, and said hydromains are provided with lock elements and are connected with respective vapour condensers. Invention also relates to method.    USE - Chemistry.    ADVANTAGE - Application of claimed invention makes it possible to reduce water-content of produced gases, increase energy efficiency and reliability of device operation.4 cl, 1 dwg
NOVELTY - Method of partial natural gas liquefaction under option 1 switches on the pre-cooling of direct HP gas flow. After cooling the direct flow is throttled and separated in the rectifier to liquid phase and steam phase. The steam phase is supplied for re-condensation with further supply of part of re-condensed product flow to the rectifier as reflux, and throttling of the other part of the re-condensed product and separation to the liquid phase being finished product, and steam phase sent as back flow for the direct flow cooling. The liquid phase from the rectifier is expanded and due to re-condensation of the steam phase from the rectifier it is evaporated, then it is heated by the direct flow, and after re-throttling is sent to the back flow. In contrast to the option 1 during the partial natural gas liquefaction method under option 2 part of the direct flow after cooling is expanded and mixed with back flow.    USE - Machine building.    ADVANTAGE - Suggested group of inventions ensures production of the liquefied natural gas with low content of high boiling components, including carbon dioxide having increased operation characteristics, upon power consumption decreasing for its production.2 cl, 2 dwg
NOVELTY - This utility model claims a dimethyl sulfoxide waste salt of a treatment device, and including oxidation reaction jar, dimethyl sulfone crystal reaction jar, dimethyl sulfone centrifuge, evaporation concentrate a, sodium nitrate crystal reaction jar, methyl sulfonic acid sodium separating device and separating device and a sodium nitrate. This utility new type can be used for a for a multi-effective component in dimethyl sulfoxide waste salt is a process using the waste is valuable, green environment-friendly effect is effect, at the same time it has simple structure, a green and environment-friendly, waste water, the energy consumption is low, and a high efficiency and so on.
NOVELTY - Producing functional organic fertilizer comprises carrying out composting aerobic fermentation until fermentation temperature is less than 50 degrees C, when the water content is less than 40%, adding 10-50% Allium spp. raw material, aging at least for 15 days, during each 5-7 days turning one time, when the temperature is less than 45 degrees C, when water content is less than 40%, entering into a finished product packing stage processing.    USE - The method is useful for producing functional organic fertilizer (claimed), which is used for preventing nematodes, bacteria, and virus.    ADVANTAGE - The method converts waste material into useful material, and reduces agricultural wastes causing environmental pollution. The organic fertilizer reduces pesticidal pollution and damages caused to the farm, does not produce harm for human body.
NOVELTY - An organic fertilizer composition is manufactured using kitchen waste comprises 20-95% kitchen waste powder, 3.5-50% straw powder, 1-30% humic acid fungus powder and 0.5-1.5% lactic acid powder.    USE - Method for manufacturing organic fertilizer composition using kitchen waste (claimed).    ADVANTAGE - The method solves kitchen waste treatment, high transportation cost and environment pollution. The product absorbs by crop.
NOVELTY - Preparation of salicylate guanidine comprises under a water bath condition, dissolving salicylic acid in an organic solvent, slowly stirring while adding guanidine carbonate, reacting at 25-75 degrees C, preferably 45-65 degrees C for 0.5-10 hours, preferably 0.5-2 hours continuously stirring, cooling, filtering, concentrating filtered liquid to dryness, and oven drying at 60 degrees C, where the mol ratio of guanidine carbonate and salicylic acid is 1:1-1:5.    USE - Method for the preparation of salicylate guanidine (claimed).    ADVANTAGE - The method is easy, uses less organic solvent to avoid excessive residua organic solvents to ensure drug safety, and is inexpensive.
NOVELTY - Idelalisib is synthesized by subjecting R-2-hydroxybutyrate and 6-amino-9H-purine to nucleophilic substitution reaction in presence of leaving reagent and acid-binding agent in solvent to obtain intermediate S-2-(N-9H-purin-6-yl) aminobutyric acid ester; subjecting intermediate and 2-carboxylic acid-3-fluroaniline to amidation reaction in presence of catalyst to obtain second intermediate S-2-(N-9H-purin-6-yl) amino-N-(2-carboxylic acid-3-fluorophenyl) butanamide; and performing cyclization reaction in acetic anhydride, followed by substitution reaction with aniline.    USE - Method for synthesizing idelalisib (claimed).    ADVANTAGE - The method utilizes easy to obtain raw material, has simple technique, and is economical, environment-friendly and suitable for industrial production.
NOVELTY - Glufosinate ammonium is produced by performing addition reaction on methyl phosphonite compound and acrolein to form methyl phosphonite derivative compound , reacting with cyanide to form methyl phosphonite cyanohydrin compound, reacting with ammonia to obtain aminonitrile derivative, performing alkaline hydrolysis to obtain glufosinate disalt aqueous solution, performing bipolar membrane electrodialysis treatment on with salt chamber pH of 2.5-3.5 to obtain glufosinate and glufosinate salt mixed solution and alkaline solution from alkali chamber, concentrating mixed solution, and cooling.    USE - Production of glufosinate ammonium (claimed).    ADVANTAGE - Production of glufosinate ammonium is environment-friendly, has high yield product purity, use rate, and improved electric current efficiency, saves energy, and reduces production cost and consumption.    DETAILED DESCRIPTION - Glufosinate ammonium is produced by performing addition reaction on methyl phosphonite compound of formula (I) and acrolein to form methyl phosphonite derivative compound of formula (IV), reacting with cyanide to form methyl phosphonite cyanohydrin compound of formula (V), reacting with ammonia to obtain aminonitrile derivative of formula (VI), performing alkaline hydrolysis to obtain glufosinate disalt aqueous solution, performing bipolar membrane electrodialysis treatment on with salt chamber pH of 2.5-3.5 to obtain glufosinate and glufosinate salt mixed solution and alkaline solution from alkali chamber, concentrating mixed solution, cooling, crystallizing to obtain glufosinate and crystallization mother liquor, returning mother liquor to bipolar membrane electrodialysis treatment, and reacting glufosinate with ammonia.    R=undefined.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart for the production of glufosinate ammonium. (Drawing includes non-English language text).
NOVELTY - A glyphosate is produced by oxidizing hydrogen peroxide, air or oxygen-rich gas as oxidizing agent, activated carbon as catalyst, and N-phosphonomethyliminodiacetic acid (PMIDA) glyphosate salt in water to obtain glyphosate salt solution and activated carbon mixture, solid-liquid separating mixture in which solid is activated carbon and filtered liquid is glyphosate salt solution, feeding glyphosate salt solution in bipolar film electro-dialysis device, treating solution, controlling pH to 2-3 to obtain glyphosate solution, and treating in alkali chamber containing alkali solution.    USE - Production of glyphosate (claimed).    ADVANTAGE - The production is energy-saving and clean, increases PMIDA and glyphosate solubility in water, shortens reaction time, overcomes double-residue of glyphosate due to wrapping, separates glyphosate salt solution and activated carbon at low temperature, avoids formaldehyde by-product in mother liquid and repeated heating and cooling, does not need acid to neutralize, eliminates sulfate or hydrochloride coagulant salt by-product, reduces salt-containing wastewater and three-waste pollution, and has good product quality and high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for glyphosate production device comprising oxidation reaction device, solid-liquid separating device, bipolar film electro-dialysis device, and crystallizing device in which oxidation device material outlet is connected to solid-liquid separating device material inlet, filtered liquid outlet of solid-liquid separating device is connected to salt room of bipolar film electro-dialysis device, solid outlet of solid-liquid separating device is connected to oxidation device, and salt room of bipolar film electro-dialysis device is connected to crystallizing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow chart of Energy-saving glyphosate production and device. (Drawing includes non-English language text).
NOVELTY - The device comprises a shaft that is rotatable about an axis of rotation. A stirring element (106) having a recess (108) is attached to shaft. The recess including surface portion (114) and an edge (116) defining an opening that provides access to surface portion. The recess is spaced from shaft. The rotation of the shaft is adapted to define a moving direction (120) of recess in which the edge forms a leading edge of the recess. The surface portion is configured for defining a depth of the recess with regard to edge and depth of recess is decreased in a radially inwardly direction.    USE - Stirring device for stirring fermentation material in biogas fermenter.    ADVANTAGE - Since the depth of the recess is inwardly decreased with regard to opening edge, the removal of fermentation material contained in the recess is facilitated and the resistance against radially inward emptying of the recess is reduced. As tetragonal shape of recess provides a large area transverse to the moving direction, the ease of manufacturing is ensured. Since the surface portion and the further surface portion are flat surface portions, the cost efficient manufacture of the stirring element is ensured. The accumulation of sediment in the recess is eliminated by flow of fermentation material in the recess. The flow of fermentation material within the recess is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of stirring element of a stirring device for a biogas fermenter.    Stirring element (106)    Recess (108)    Surface portion of recess (114)    Edge of recess (116)    Moving direction of recess (120)
NOVELTY - An electrochemical reaction device (10,20) has an anode electrode (11,21) containing iron and gadolinium-doped ceria, cathode electrode (12,22) containing cobalt and gadolinium-doped ceria, and porous electrolytic membrane (13,23) provided between the anode electrode and the cathode electrode, and containing gadolinium-doped ceria.    USE - Electrochemical reaction device is used in composite electrochemical reaction device used in manufacture of hydrogen (all claimed) used as fuel in fuel cell.    ADVANTAGE - The device manufactures hydrogen and carbon dioxide from carbon monoxide and water vapor at high efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) composite electrochemical reaction device (1); and    (2) manufacture of hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrochemical reaction device. (Drawing includes non-English language text)    Composite electrochemical reaction device (1)    Electrochemical reaction devices (10,20)    Anode electrodes (11,21)    Cathode electrodes (12,22)    Electrolytic membranes (13,23)
NOVELTY - The system has a process gas line passed through a heat exchanger for supplying process gas to a condenser. The condenser supplies process gas emitted in a regenerator. An absorbent supply line faces the regenerator and supplies absorbent absorbing acidic gas in an absorptive tower. An exhaust gas supply line faces the absorptive tower. A condensed water supply line supplies rough condensed water to an upper end of the regenerator. Another heat exchanger exchanges condensed water heat with dilute solution in the regenerator by using the condensed water.    USE - System for sampling energy reduction-type acidic gas e.g. carbon dioxide, methane, hydrogen sulfide, carbonylsulfide and mercapto.    ADVANTAGE - The system reduces reboiler demand calorie of the condensed water and pre-heats high temperature process gas by selectively using low temperature condensed water in a dust scrubber with dilute solution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an energy reduction-type acidic gas collecting method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for sampling energy reduction-type acidic gas.
NOVELTY - This new type utility claims kitchen garbage treatment system, in turn comprising a the feeding bin, a pre-crushing device, the press filter, solid-liquid separating device, the oil water separating device, a magnetic sorting device, depth crushing device, a squeezing device, collecting the sterilizing device, a fermentation device, a use device. This utility new type is kind of kitchen garbage processing system aiming at special ingredient of domestic kitchen garbage, through extrusion, solid liquid separating device, a magnetic sorting device effective for the containing of the various inorganic object is gradually separated by, and to separate out the inorganic object taking full use. At the same time, to the organic object in process of kitchen garbage crushing and purifying equal depth process, using the organic object particle size after crushing can well satisfy inoculating ferment and process condition, increase of yield of marsh gas, gain of the good environmental benefit and economic benefit.
NOVELTY - This utility new type relates to a water electrolysis hydrogen one double-film gas balance device, wherein this device include one for U-shaped shell, between the one for U-shaped shell set with middle ring (7), a middle ring (7) and two side of U-shaped shell through each one piece thin film piece (6); the one for U-shaped shell and each corresponding to a thin film piece (6) is composed two pneuma cavity a, a is with hydrogen entrance (1) and gas outlet (4) of gas cavity, and oxygen entrance (12) and oxygen outlet of oxygen cavity, two pieces of film piece (6) is inner space set with a film (8), a middle ring (7) is set with at least one side a the pneuma hole. Once side cavity of film piece happen damage, leakage of a gas from the middle ring up the pneuma hole is a, and a is a gas and the other side inner cavity mixed, which avoids the safety hidden trouble.
NOVELTY - This utility model relates to a production device of biomass absolute ethyl alcohol, belonging to the organic solvent dehydration technology field. After at least one of pressurizing rectifying tower (1), at least one of more pressure rectifying tower (2), at least one of pressure reducing rectifying tower (3), a permeation vaporized membrane (4), a pressurizing rectifying tower (1), the more pressure rectifying tower (2) and pressure reducing rectifying tower (3) and tower top respectively and permeation vaporizing membrane (4) is connected with entrance of ferment liquid raw material pipeline (6) respectively and permeation vaporizing membrane (4) and material liquid side of discharging pipeline and rectifying tower bottoms of discharging pipeline for heat exchange connection, respectively entering into rectifying tower to inside. The production device considering of each grade energy optimizing configuration in the system, to realize energy saving and target system, steam consumption and the traditional process of whole system of comparison can save steam is 30 to 50% more than.
NOVELTY - Preparing phosphomolybdate crystal catalyst, comprises adding ammonium molybdate tetrahydrate, 1,3-bis(4-pyridyl)propane and phosphoric acid to 15 ml of distilled water, stirring for 1-12 hours to obtain a mixed liquid, adding the resulting mixture in a Teflon (RTM: PTFE) lined stainless steel autoclave and then sealing the autoclave at a fill rate of 60%, placing the autoclave inside an oven and then performing heating crystallization, and cooling at a room temperature to obtain phosphomolybdate crystal catalyst.    USE - The process is useful for preparing phosphomolybdate crystal catalyst (claimed), which is useful for the synthesis of aspirin.    ADVANTAGE - The process is capable of simply and economically preparing phosphomolybdate crystal catalyst with high catalytic activity and yield and without environmental pollution under mild reaction conditions.    DETAILED DESCRIPTION - Preparing phosphomolybdate crystal catalyst, comprises adding ammonium molybdate tetrahydrate ((NH4)6Mo7O24.4H2O), 1,3-bis(4-pyridyl)propane and phosphoric acid at a molar ratio of 1:1:8.6 to 15 ml of distilled water, stirring for 1-12 hours to obtain a mixed liquid, adding the resulting mixture in a Teflon (RTM: PTFE) lined stainless steel autoclave and then sealing the autoclave at a fill rate of 60%, placing the autoclave inside an oven and then performing heating crystallization at a temperature of 100-200 degrees C for 100-200 hours, and cooling at a room temperature to obtain phosphomolybdate crystal catalyst.
NOVELTY - Biocomplex comprises a livestock complex 1 communicated with a storage hopper of organic wastes 2; a pyrolysis furnace 4 with nozzles of discharge of char, crude pyrolysis gas, waste heat and flue gases; a gasholder 16; microalgae cultivation unit consisting of the block of culture liquid 23 and a photoreactor 24, microalgae processing unit 26 communicated with the feed-preparation device 27, the carbon dioxide production unit 19, consisting of the absorber 20 and the desorber 21, provided with a carbon dioxide discharge pipe to the block of production of microalgae, the carbon dioxide liquefaction unit 25; the cogeneration unit 18 provided with the flue gases discharge system to the carbon dioxide production unit. The pyrolysis furnace is connected with the preparation unit of furnace fuel, a unit of purification of pyrolysis gas, with livestock complex and the production unit of carbon dioxide. The unit of purification of pyrolysis gas 9 is connected with the preparation unit of furnace fuel 12 and with the gas holder 16 connected to the cogeneration unit 18.    USE - Agriculture.    ADVANTAGE - Biocomplex enables to obtain year-round the pyrolysis gas for processing it into heat and electricity, char, pyrolysis distillate, to reprocess animal wastes, to increase the intensity of growth of microalgae.3 cl, 1 dwg
NOVELTY - Recombinant microorganism comprising: (a) one or more native and/or heterologous proteins that function to import glycerol into the recombinant microorganism, where the native and/or heterologous proteins are activated, upregulated, or overexpressed; and (b) one or more native and/or heterologous enzymes that function in one or more engineered metabolic pathways to convert a carbohydrate source to an alcohol, is new, where the native and/or heterologous enzymes are activated, upregulated, overexpressed, or down-regulated.    USE - The recombinant microorganism is useful for: decreasing cellular-produced glycerol; and converting biomass e.g. corn mash or corn starch, to alcohol, such as ethanol or isopropanol (all claimed).    ADVANTAGE - The method allows effective production of alcohol from lignocellulosic feedstocks, which are cheaper, can be grown more densely, show lower life cycle carbon dioxide emissions, and can be cultivated on marginal lands, so that the time and cost of the process can be reduced.
NOVELTY - N-methylmorpholine hydrochloride is recovered from valnemulin synthesis wastewater by quenching wastewater and adjusting pH value to 9-11, then extracting with organic solvent, collecting organic phase, drying organic phase using desiccant, heating dried material to 115-116 degrees C and performing fractional distillation, and collecting product.    USE - Method for recovering N-methylmorpholine hydrochloride from valnemulin synthesis wastewater (claimed).    ADVANTAGE - The method is simple to carry out, has reduced cost, can reduce pollutant in sewage discharge to reduce environment pollution. The N-methylmorpholine hydrochloride recovery rate is higher than 95% with N-methylmorpholine content of more than 98%.
NOVELTY - The system has a control unit (800) for controlling the two flow control valves (931,932). A presser portion (400) refines pressurized source gas. A buffer tank (600) stores supplied source gas and refinery gas. The three refining units (100-300) refine refinery gases by controlling flow rate using specific flow control valve of sub return line (720), so as to purity refinery gas and waste gas. The refining unit has a bed which repeatedly executes multiple processing stages and sorbing step. The control unit is made to control operation time of processing stage.    USE - Gas separation system for producing refined methane.    ADVANTAGE - The control unit controls operation time of processing stage which is repeatedly executed by bed of refining unit which refines refinery gases by controlling flow rate, so that the component of the gas is monitored by the real-time and the methane gas of the high purity can be steadily produced. The consumed energy is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of gas separation system.    Refining units (100-300)    Presser portion (400)    Buffer tank (600)    Sub return line (720)    Control unit (800)    Flow control valves (931,932)
NOVELTY - A catalyst comprises metal nitride (I). The metal nitride contains hexagonal lattice having four-layered stacking sequence comprising mixed close packed structure having alternating layers of metal (M') and metal (M") in trigonal prismatic coordination or octahedral coordination. The metal (M') is silver, aluminum, calcium, cobalt, chromium, copper, iron, gallium, indium, lithium, magnesium, manganese, sodium, nickel, scandium, titanium, vanadium, yttrium, and/or zinc. The metal (M") is hafnium, molybdenum, niobium, rhenium, ruthenium, tantalum, tungsten, and/or zirconium.    USE - Catalyst is used in production of hydrogen (claimed).    ADVANTAGE - The catalyst has excellent catalytic activity, and enables efficient production of hydrogen by economical process.    DETAILED DESCRIPTION - A catalyst comprises metal nitride of formula: M'xM"yNz (I). The metal nitride contains hexagonal lattice having four-layered stacking sequence comprising mixed close packed structure having alternating layers of metal (M') and metal (M") in trigonal prismatic coordination or octahedral coordination. The metal (M') is silver, aluminum, calcium, cobalt, chromium, copper, iron, gallium, indium, lithium, magnesium, manganese, sodium, nickel, scandium, titanium, vanadium, yttrium, and/or zinc. The metal (M") is hafnium, molybdenum, niobium, rhenium, ruthenium, tantalum, tungsten, and/or zirconium. The catalyst is capable of promoting hydrogen evolution reaction.    x=0-1;    y=1-2;and    z=1.8-2.2.    An INDEPENDENT CLAIM is included for production of hydrogen, which involves providing one-chambered electrochemical cell having an anode, supporting electrolytes and reagent solution, and a cathode comprising hydrogen-evolution reaction catalyst, applying current with respect to the electrochemical cell, and producing hydrogen at the cathode.
NOVELTY - Aniline compound (I) and 5-chloro-pentanoyl chloride (II) are reacted in presence of inorganic base and inert solvent to obtain apixaban intermediate (III).    USE - Synthesis of apixaban intermediate (claimed).    ADVANTAGE - The method provides apixaban intermediate with high purity, under mild reaction conditions, by simple, economical and environmentally-friendly process.    DETAILED DESCRIPTION - Aniline compound of formula (I) and 5-chloro-pentanoyl chloride of formula (II) are reacted in presence of inorganic base and inert solvent to obtain apixaban intermediate (phenyl piperidinone) of formula (III).    R=nitro, or 3-morpholin-4-yl-5,6-dihydro-1H-pyridinyl.
NOVELTY - Preparing complex microemulsion comprises adding methylene chloride in high-speed stirring tank and then stirring, adding ethanol, cyhalofop butyl, and Starane (RTM: Herbicide) to tank, allowing mixture to react in tank, adding water into tank and then stirring, adding sodium dodecylbenzenesulfonate to mixture and then stirring until alkyl sodium is completely dissolved, and slowly adding methylene chloride and cyhalofop butyl to obtained mixture and then allowing to react.    USE - The method is useful for preparing complex microemulsion (claimed), which is useful for controlling broadleaf weeds.    ADVANTAGE - The method is capable of easily preparing the complex microemulsion with improved quality under mild reaction conditions in an eco-friendly manner.    DETAILED DESCRIPTION - Preparing complex microemulsion comprises adding 5-6 wt.% of methylene chloride in a high-speed stirring tank and then stirring at room temperature and a speed rate of 35-40 revolutions per minute, adding 13-14 wt.% of ethanol, 10-11 wt.% of cyhalofop butyl, and 2-3 wt.% of Starane (RTM: Herbicide) to the tank, allowing the mixture to react in the tank for 0.8-10 hours, adding water into the tank and then stirring at a speed rate of 50-60 revolutions per minute at room temperature, adding sodium dodecylbenzenesulfonate to the mixture and then stirring at a speed rate of 210-220 revolutions per minute until alkyl sodium is completely dissolved, and slowly adding methylene chloride and cyhalofop butyl to the obtained mixture and then allowing to react for 0 9-1.1 hours.
NOVELTY - Water-soluble granule comprises paraquat as an active ingredient in the form of paraquat concentrated liquid.    USE - Water-soluble granule.    ADVANTAGE - The water-soluble granule can be simply prepared with high yield and without producing waste residue in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the water-soluble granule, comprising taking paraquat and distillating under a pressure of -0.08 MPa to -0.095 MPa to reach a moisture content of 27-33 wt.% and to obtain a paraquat concentrated liquid, and (b) uniformly mixing the paraquat concentrated liquid with adsorbent, surfactant and binder, granulating and then drying.
NOVELTY - Sewage treatment agent comprises 100-200 pts. wt. activated sludge, 20-40 pts. wt. submarine mud (mineral), 10-20 pts. wt. coagulant, 10-20 pts. wt. deactivator, 10-20 pts. wt. plant ash, 10-30 pts. wt. 1,3,5-triazine-2,4,6-trithiol trisodium salt, 5-10 pts. wt. bleaching agent, 5-10 pts. wt. biological enzyme, and 20-40 pts. wt. microbial mixture, where the microbial mixture comprises Arthrobacter, yeast and wood-decay fungus, and the above-mentioned microorganisms are not less than 200 million activated cells.    USE - The sewage treatment agent is useful for treating waste water containing heavy metal (claimed).    ADVANTAGE - The agent is cost-effective and prevents pollution.
NOVELTY - Method for processing biomass involves mixing carboxylic acid and hydrogen peroxide in a molar ratio of 0.5-7:1, adding mixture to biomass, heating mixture at 60-100 degrees C for 2-3 hours, filtering heated mixture, and adding 3 wt.% lignin to obtained filtered solid.    USE - The method is useful for processing biomass (claimed).    ADVANTAGE - The method enables to process biomass in an environmentally-friendly manner.
NOVELTY - A municipal river water pollution treatment microbial agent comprises 40-60 pts. wt. Lactobacillus acidophilus preparation, 20-30 pts. wt. Candida tropicalis preparation, and 10-20 pts. wt. Bacillus subtilis preparation, where the concentration of the Lactobacillus acidophilus preparations cell is not less than 5.0x 109 CFU/mL, Candida tropicalis is not less than 1.0x 109 CFU/mL, and Bacillus subtilis is not less than 1.0x 1011 CFU/ml.    USE - Municipal river water pollution treatment microbial agent.    ADVANTAGE - The agent repairs and treats river water dirty, odor pollution, repairs water ecological environment and prevents water pollution, and can fast recovery of water from a purification, digestion river sludge, in efficient, rapid, low cost manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing municipal river water pollution treatment microbial agent, which involves taking Lactobacillus acidophilus in solid culture medium to obtain the activate Lactobacillus acidophilus, placing activate the Lactobacillus acidophilus inoculating liquid culture medium into expanding culture, inoculating fermentation culture medium I in b, fermenting culture to obtain Lactobacillus acidophilus preparation, taking Candida tropicalis in solid culture medium to obtain the activated Candida tropicalis, placing activated Candida tropicalis in liquid culture medium II expanding culture, inoculating fermentation culture medium II, fermenting culture to obtain Candida tropicalis preparation, taking Bacillus subtilis, in solid culture medium to obtain activated Bacillus subtilis, inoculating bacillus subtilis liquid culture medium III in expanding culture, inoculating fermentation culture medium III, fermenting culture to obtain Bacillus subtilis preparation, mixing the preparations according to the proportion to obtain finished product.
NOVELTY - Preparing ginsenoside Rg2 comprises extracting ginseng using solvent including weak acid, organic acid, water and/or 50-80% of ethanol (preferred), adjusting pH value of the extract to 3-5, concentrating the extract, processing the extract by dissolving it in a mixture of water and ethanol and then filtering, centrifuging to remove supernatant from the filtrate and then concentrating, performing column chromatography using methacrylate based resin to separate fractions containing ethanol and water, and eluting the obtained product using an eluent.    USE - The method is useful for preparing ginsenoside Rg2 (claimed), which is useful in cosmetics, health functional food, and drugs.    ADVANTAGE - The method is capable of easily and economically preparing the ginsenoside Rg2 with improved yield and purity, and without using organic solvent in an efficient and environmentally-friendly manner.
NOVELTY - A fuel treating apparatus (1) comprises source gas and modification part (20) which produces hydrogen-containing-gas from water vapor and combustion part (50) which burns fuel gas and generates combustion gas in which combustion gas flow path of combustion part may surround along flow path of modification part.    USE - A fuel treating apparatus for fuel cell system.    ADVANTAGE - Apparatus has small temperature distribution of modification catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the fuel treating apparatus. (Drawing includes non-English language text).    Fuel treating apparatus (1)    Source gas inlet port (3)    Fuel gas inlet (4)    Modification part (20)    Combustion part (50)
NOVELTY - A visible-light-responsive composition comprises 30-45 mol% tantalum, 20-40 mol% copper, 30-38 mol% bismuth, and oxygen.    USE - Visible-light-responsive composition is used for photosensors, and photoelectrodes and photocatalysts used for hydrolysis (all claimed) to produce hydrogen. Can also be used for removal and deodorization of environmental pollutants, and for providing antimicrobial, antiviral, antifungal, antifouling and antifogging effects in building interiors and motor vehicles.    ADVANTAGE - The visible-light-responsive composition has high photoelectric current responsiveness with respect to visible light irradiation, and the degree of charge separation for photocatalytic function. The composition provides photoelectrodes which efficiently utilize sunlight.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrolysis using photoelectrode and/or photocatalyst using the visible-light-responsive composition.
NOVELTY - A fluid separation material (20) comprises porous silica substrate (21) produced by chemical vapor deposition method, silica separation membrane (23) having fluid separability formed on the porous silica substrate, and intermediate layer (22) provided between the porous silica substrate and the silica separation membrane. The intermediate layer is formed using silica particles having average particle diameter of 100-500 nm, and product of BET specific-surface-area (m2/g) and average particle diameter (nm) of 7000 or less.    USE - Material is used for separating hydrogen from hydrogen-containing mixed gas generated by fuel modification.    ADVANTAGE - The fluid separation material prevents permeation of fluid other than fluid to be separated, and reduction in fluid separation property at high temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of fluid separation material, which involves forming intermediate layer between the porous silica substrate and the silica separation membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the fluid separation material.    Fluid separation material (20)    Porous silica substrate (21)    Intermediate layer (22)    Silica separation membrane (23)    Center hole (24)
NOVELTY - Method for processing organic wastewater, involves adjusting chemical oxygen demand (COD) concentration and pH of organic wastewater, obtaining adjustment wastewater, supplying ozone microbubble to the adjustment wastewater, rendering decomposable organic substance in adjustment wastewater, obtaining pre-processed wastewater, performing microbial treatment of the pre-processed wastewater using bacteria, removing phosphorus, measuring mixed liquor suspended solids (MLSS) concentration, adjusting the MLSS concentration of the mixture, and adjusting pH.    USE - The method is useful for processing organic wastewater including rice processed wastewater and rice bran processed wastewater (all claimed).    ADVANTAGE - The method maintains wastewater treatment performance in stable manner.    DETAILED DESCRIPTION - Method for processing organic wastewater, involves adjusting chemical oxygen demand (COD) concentration and pH of organic wastewater, obtaining adjustment wastewater, supplying ozone microbubble to the adjustment wastewater, rendering decomposable organic substance in adjustment wastewater, obtaining pre-processed wastewater, performing microbial treatment including anaerobic process, aerobic treatment, and anoxic treatment of the pre-processed wastewater using phosphorus accumulating bacteria and denitrifying phosphorus accumulating bacteria, removing phosphorus, measuring mixed liquor suspended solids (MLSS) concentration of microorganisms treated wastewater, adjusting the MLSS concentration of the mixture until the threshold value and COD concentration reaches 2000 mg/l or less, and adjusting pH of the mixture to 5-8. An INDEPENDENT CLAIM is included for organic wastewater processing device.
NOVELTY - Methane fermentation processing apparatus comprises grinder (14), reaction tank (16), filter (18) and fermenter (20). The grinder is provided to pulverize organic waste which is heat-processed such that the melting point of the organic waste reaches melting point of sulfur. The reaction tank is provided to generate solution containing mixture of substrate for methane fermentation, pulverized organic waste and acidic electrolyzed water which is processed at predetermined temperature. The filter is provided to remove sulfur from the solution.    USE - As methane fermentation processing apparatus.    ADVANTAGE - The apparatus enables to perform methane fermentation simply and stably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for methane fermentation processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of methane fermentation processing apparatus.    Grinder (14)    Reaction tank (16)    Filter (18)    Fermenter (20)
NOVELTY - The apparatus has a cell stack that is formed by arranging outbound path side cell (1a) and inbound path side cell (1b). A communication element (32) connects the upper end portion of the outbound path side cell, and the upper end portion of the inbound path side cell. The inbound path side cell is connected with the upper end portion of the outbound path side cell located in the sequence direction both ends of the cell stack unit (30a) in the cell stack. The outlet tube (37) derives the gas containing hydrogen and the inlet tube (35) introduces the gas containing water vapor.    USE - Electrolysis cell stack apparatus for electrolyzer (claimed).    ADVANTAGE - The electrolysis cell stack apparatus can reduce the stress concentration in the connection portion of an inlet tube, an outlet tube, and a cell stack. The long-term reliability of the electrolyzer is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the electrolysis cell stack apparatus.    Outbound path side cell (1a)    Inbound path side cell (1b)    Cell stack unit (30a)    Communication element (32)    Inlet tube (35)    Outlet tube (37)
NOVELTY - Visible-light responsive composition comprises 30-50 mol% tin, 30-40 mol% iron, 20-60 mol% vanadium, and oxygen.    USE - Visible-light responsive composition is used for photocatalyst, photosensor and photoelectrode for hydrolysis (all claimed) for hydrogen production. The photocatalyst is used for interior of building and motor vehicle.    ADVANTAGE - The composition has high photoelectric current responsiveness with respect to visible light irradiation, and visible light absorption property. The photocatalyst containing the composition removes and deodorizes environmental pollutant, and has high antimicrobial property, antiviral property, antifungal property, antifouling property and anti-fogging property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrolysis method.
NOVELTY - Microbial electrolysis cell generates hydrogen from glucose and acetate using immobilized microorganisms as anode, and modified carbon electrode having hydrogen generating catalytic activity as cathode.    USE - The microbial electrolysis cell is useful for producing hydrogen using hydrogen using biomass, preferably woody biomass (all claimed).    ADVANTAGE - The microbial electrolysis cell is reliable, ensures high yield of hydrogen and has high energy-conversion efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of producing hydrogen, which involves (a) extracting hemicellulose and cellulose components from woody biomass, (b) carrying out first and second fermentation process of woody biomass using microorganisms to obtain fermentation broth, and (c) producing hydrogen from the resulting fermentation broth using the microbial electrolysis cell by supplying electric current.
NOVELTY - A diatomaceous earth sintered compact comprises 1 mu m open cell and is mixed with 0.5-20% methane fermentation liquid and improves biogas productivity to 5-10%.    USE - A diatomaceous earth sintered compact for soil improvement materials (claimed).    ADVANTAGE - Improvement of biogas production rate and shortening of induction time of biogas generation are acquired by absorbing microorganisms in methane fermentation. Moisture retention and productivity of agricultural products are improved when using digestive liquid as liquid fertilizer. Sintered compact can be recycled by putting into nylon bag.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the change of generation amount of methane in methane fermentation with inorganic additive. (Drawing includes non-English language text).
NOVELTY - A solid fuel is manufactured by baking wood-type biomass within a kiln inner cylinder (1) of an external heating type rotary kiln in which temperature of wood-type biomass in kiln inner cylinder is 250-350 degrees C, oxygen concentration in kiln inner cylinder is less than or equal to 10%, and temperature of kiln outer cylinder (7) is 400-800 degrees C.    USE - Manufacture of solid fuel for powdered coal boiler.    ADVANTAGE - Even if the residence time within a kiln is short, solid fuel can be manufactured efficiently by baking wood-type biomass with external heating type rotary kiln. Substance yield and heat amount yield are high, and manufactured solid fuel has grindability equivalent to coal and high density.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the external heating type rotary kiln.    Kiln inner cylinder (1)    Supply side hood (2)    Discharge side hood (3)    Supply part (4)    Kiln outer cylinder (7)
NOVELTY - The system has a fuel cell (1) for providing a solid polymer electrolyte membrane (7) between an anode (8) and a cathode (9). A fuel gas supply unit (2) supplies fuel gas to the anode. An oxidizing agent gas supply unit (3) supplies oxidizing agent gas to the cathode. A power generation reaction inhibitor addition unit (4) temporarily adds a power generation reaction inhibitor in which adsorption and desorption of the oxidizing agent gas are reversibly carried out to a catalyst layer of the cathode such that output voltage in electric power generation of the fuel cell is temporarily declined.    USE - Fuel cell system i.e. solid high polymer type household use fuel cell system.    ADVANTAGE - The power generation reaction inhibitor addition unit temporarily adds the power generation reaction inhibitor such that the output voltage in electric power generation of the fuel cell is temporarily declined, so that an electrolytic membrane and catalyst can be activated in a downstream part that is not contributed to the electric power generation by fastening addition of the power generation reaction inhibitor, thus suppressing drying of the electrolytic membrane with increase of electric current and improving electric power generation performance of the fuel cell.    DETAILED DESCRIPTION - The fuel gas is hydrogen. The power generation reaction inhibitor is nitrogen oxide contained in combustion exhaust gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel cell system.'(Drawing includes non-English language text)'    Fuel cell (1)    Fuel gas supply unit (2)    Oxidizing agent gas supply unit (3)    Power generation reaction inhibitor addition unit (4)    Solid polymer electrolyte membrane (7)    Anode (8)    Cathode (9)
NOVELTY - Cultivating star anise having high oil content and high-quality comprises (i) placing full star anise seeds on ground, tedding, and stirring; (ii) soaking in clean water, then soaking in cold water, and drying; (iii) sowing the star anise; (iv) crushing ceramsite, adding with distilled water, and uniformly mixing; (v) adding the resulting aqueous solution with chicken manure, straw, Camellia, alfalfa, cassava residue, soybean residue and organic selenium, fermenting, drying, and crushing to obtain organic fertilizer; and (vi) combining the organic fertilizer with inorganic fertilizer.    USE - The method is useful for cultivating star anise having high oil content and high-quality (claimed).    ADVANTAGE - The method: is suitable to grow seedlings of star anise; and improves the yield and quality of the star anise.    DETAILED DESCRIPTION - Cultivating star anise having high oil content and high-quality comprises (i) selecting full star anise seeds, placing on ground, continuously tedding for 2-3 days, and stirring once at an interval of 4-6 hours; (ii) soaking in clean water, then soaking in cold water for 12-24 hours, and placing in room to dry for 2-4 hours; (iii) sowing the star anise by maintaining V-shaped single planting density, where row spacing is 40-50 cm, and spacing range is 35-40 cm; (iv) preparing aqueous nano ceramic solution by crushing ceramsite into particle diameter of 600-800 mu m, adding the material with distilled water according to ratio of 1:5-10, uniformly mixing and stirring; (v) adding the resulting aqueous solution with chicken manure, straw, Camellia, alfalfa, cassava residue, soybean residue and organic selenium, placing in a fermenting tank to ferment for 10-20 days, drying, and crushing to obtain organic fertilizer; and (vi) combining the base fertilizer of organic fertilizer with inorganic fertilizer comprising 0.5-0.8% urea, 0.2-0.4% monopotassium phosphate, 0.5-1% calcium superphosphate, and 0.02-0.05% zinc molybdate.
NOVELTY - Bio-organic nutritional liquid fertilizer comprises 1-2 pts. wt. pollen, 0.2-0.5 pts. wt. honey, 2-5 pts. wt. white sugar, 10-20 pts. wt. water and 0.01-0.05 pts. wt. effective microorganisms (EM).    USE - The bio-organic nutritional liquid fertilizer is useful in fruit tree planting (claimed).    ADVANTAGE - The fertilizer: is stable; can be preserved for a long time; is convenient to use; prolongs the flowering period; increases the proportion of female flowers; increases fruit yield; increases fruit tree leaf thickness, fruit weight and yield; can be prepared in a simple manner; and is suitable for easy industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the fertilizer, comprising (a) introducing the raw materials as mentioned above into a fermentation container and stirring uniformly to obtain a mixture, (b) fermenting the mixture at 20-35 degrees C to obtain fermentation broth, and (c) diluting the broth with water for 100-500 times.
NOVELTY - Agricultural solid waste aerobic compost processing comprises regulating moisture content of the agricultural solid waste to 50%-90%, where the solid waste contains 20-30% rotten compost; adjusting carbon to nitrogen ratio to 10:1-30:1, preferably 15:1-25:1; and inserting the solid waste stack material in a vertical ventilation tube, and treating.    USE - Method for agricultural solid waste aerobic compost processing (claimed).    ADVANTAGE - The method is operated without power consumption, is simple and easy, shortens aerobic time for 1-2 days, and shortens compost time for 5-15 days.
NOVELTY - Gel controlled-release bio-fertilizer comprises 1-3 pts. ammonium nitrate, 2-6 pts. calcium nitrate, 1-3 pts. potassium ore powder, 7-13 pts. stone powder, 25-35 pts. carbon powder, 0.1-0.2 pts. caterpillar fungus powder, 0.1-0.2 pts. Japanese scarab Bacillus powder, 0.1-0.2 pts. Bacillus sphaericus powder, 35-45 pts. rice straw, 30-40 pts. corn straw, 0.1-0.2 pts. avermectin mixture, 1-6 pts. arrow root powder, 2-6 pts. potassium dihydrogen phosphate, 1-2 pts. sodium nitrophenolate, 1-2 pts. naphthalene acetic acid and 1-2 pts. humic acid.    USE - Used as gel controlled-release bio-fertilizer.    ADVANTAGE - The bio-fertilizer: is less soluble in water with slow release of nutrition element into the soil, thus reduces the loss of nutritional element; is stable; has long-term fertilizer effect; and supply nutrients to the plant continuously.
NOVELTY - Preparing 4-methyl guaiacol by vanillin catalytic hydrodeoxygenation comprises under the action of catalyst molybdenum carbide/activated carbon (AC), reacting vanillin and hydrogen under the pressure of 0.5-2.5 MPa, under the reaction temperature of 80-220 degrees C, carrying out hydrodeoxygenation reaction, after reaction, obtaining 4-methyl guaiacol.    USE - The method is useful for preparing 4-methyl guaiacol by vanillin catalytic hydrodeoxygenation (claimed).    ADVANTAGE - The method is simple, is environmentally friendly, uses economical catalyst with good stability, and is good for large scale industrial popularization and application.
NOVELTY - A phosphorus removal Pseudomonas fluorescens (D6) strain preserved in China center for Type Culture Collection under preservation number (CCTCC No: M2014140), is new.    USE - For phosphorus removal in waste waters (Claimed), natural water etc.    ADVANTAGE - The strain has wide temperature suitability and shows a good phosphorus removal effect even at low temperature of 8-30 degrees C, in winter or waste water under low temperature condition. It shows a very high phosphorus removal activity of upto 94.5%, in natural water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for screening phosphorus removal effect of Pseudomonas fluorescens (D6) strain at low temperature involving 1) preparing a culture medium A comprising 10 g of peptone, 5 g of beef extract, 5 g of sodium chloride, 19 g of agar and water (balance) with a pH value of 7.0-7.2; preparing a pre-culture medium B comprising 2 g of sodium acetate, 46 mg of Na2HPO4, 152.8 mg of NH4Cl, 8.3 mg of CaCl2, 82 mg of MgSO4, 17.83 mg of K2SO4, 7 g of HEPES, 2% of microelement and water (balance) with a pH value of 7.0-7.2; and preparing a rich-culture medium C comprising sodium acetate, 82 mg of MgSO4, 3.7 mg of FeSO4, 60 mg of CaCl2, 0.2 g of (NH4)2SO4, 0.22 g of beef extract, 74 mg of K2HPO4, 2 ml of trace element and water (balance) with a pH value of 7.0-7.2; incubating enriched culture of the Pseudomonas fluorescens (D6) strain with activated sludge in presence of the above culture mediums and subjecting it to separation, purification and screening under low temperature conditions.
NOVELTY - Method comprises adding to the feed mixture of growth promoting additive. The growth promoting additive is used as paunch manure with lactic acid bacteria Enterococus durans and Lactobacillus gallinarum added at 20 degrees -25 degrees C. At that the components are taken in the following ratio: barley - 9%-21%, triticale - 24%-26%, wheat bran - 3%-5%, chalk - 1%, paunch manure - 49%-51%.    USE - Agriculture.    ADVANTAGE - Use of the invention enables to increase the growth-promoting effect, to reduce feed costs.1 tbl
NOVELTY - An organic material composting apparatus comprises a unitary system comprising inlet (5), outlet (17), homogenizer tank(s) (6) and rotary digester(s) (11). The inlet inputs fluid undigested organic material to the homogenizer. The homogenizer includes a stirrer, preferably paddle stirrer (7), and an air supply. A conveying mechanism transfers material from the tank to the rotary digester. The digester includes a circulator for circulating heated air and inputting fresh heated air. The outlet discharges digested material from the drum.    USE - Apparatus for composting and digesting biodegradable organic waste to produce fertilizer.    ADVANTAGE - The apparatus enables production of good quality stable fertilizer in a continuous process using aerobic digestion in single rotary digestion, together with homogenizer tank. Use of heaters, e.g. microwave guns, is not required because the air is warmed enough to increase temperature of digesting material to 40-65 degrees C during digestion and more than 70 degrees C for 1 hour during the subsequent pasteurization phase. The risk of human error is reduced and there is less need for skilled management of digestion process. The efficiency of thermophilic processing conditions in the rotary digester is optimized, and the speed of digestion is also improved. The digestion time is shorter compared with standard anaerobic digestion, i.e. 1 day for manure, 3-4 days for food waste and 10-14 days for wood, as compared to 30 days for food waste in conventional digester. The digested material is stable and does not produce methane.    DESCRIPTION OF DRAWING(S) - The drawing is a side elevational view of composting apparatus.    Inlet (5)    Homogenizer tank (6)    Paddle stirrer (7)    Rotary digester (11)    Outlet (17)
NOVELTY - The device (200) has a shaft (102) that is rotatable about an axis of rotation. A mounting structure is attached to the shaft. The mounting structure has a first connection surface (112) and a second connection surface (114). A stirring element (116) is attached to the first and second connection surfaces. The first connection surface and the second connection surface are located at opposite sides of the shaft with the shaft being located between the first connection surface and a second connection surface.    USE - Stirring device for biogas fermenter.    ADVANTAGE - The improved technique is provided that enables to provide a stirring device for a biogas fermenter which provides for an efficient and reliable mounting of stirring elements to a rotatable shaft of the stirring device, while avoiding or reducing the problems. Spacing the connection surfaces from the shaft allows designing force transfer elements, which are configured for transferring the force between the stirring element and the shaft, independently from the connection surfaces. The circumferentially extended portion increases the mechanical stability of the mounting structure without increasing the surface of the mounting structure transverse to the circumferential direction. Due to the weight of the shaft, is not avoided but rather the deflection is taken into account by a reduced length of the stirring elements, thus avoiding a contact between the stirring elements and the biogas fermenter.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of mounting a stirring element to a shaft of a stirring device.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the stirring device.    Shaft (102)    First connection surface (112)    Second connection surface (114)    Stirring element (116)    Stirring device (200)
NOVELTY - Transitmycin (I) is new.    USE - (I) is useful as antibacterial and antiviral agents, where: the bacteria include Mycobacterium tuberculosis, Bacillus subtilis, Bacillus pumilus, Bacillus cereus, Staphylococcus aureus, and Acinetobacter baumannii , such as multiple drug resistant and extensively drug resistant strains of Mycobacterium tuberculosis, preferably streptomycin, isoniazid, rifampicin, and ethambutol (SHRE) sensitive and SHRE resistant strains of Mycobacterium tuberculosis; and the virus includes HIV (all claimed). The antibacterial activity of (I) was tested against Mycobacterium tuberculosis. The result showed that diethyl ether extract of (I) exhibited a percentage reduction in relative light units (RLU) of 83.4.    ADVANTAGE - The process of producing (I) is a simple process and does not require complex laboratory set-up, hence economical. (I) is a natural product and produced through naturally occurring microorganisms, hence eco-friendly. (I) shows very poor cytotoxic activity, hence used to manufacture pharmaceutical formulations against bacterial and viral pathogens.    DETAILED DESCRIPTION - Transitmycin of formula (I) is new. INDEPENDENT CLAIMS are included for:    (1) the preparation of (I);    (2) an Actinomycete strain with accession no MTCC 5597 useful for producing (I); and    (3) a kit comprising (I) along with an instruction manual.
NOVELTY - The fuel cell (300) comprises an anode side separator (320) and multiple frame gaskets that are formed between the anode side separator and cathode side separator. A membrane electrode assembly is provided with transmitted film, anode catalyst and cathode catalyst. A convex unit (350) is combined in a recess (360) among multiple frame gaskets. The cross section of the convex unit is provided in the convex shape and polygonal cross section.    USE - Fuel cell for generating electricity according to the chemical reaction with the hydrogen.    ADVANTAGE - The fuel cell comprises an anode side separator and multiple frame gaskets that are formed between the anode side separator and cathode side separator, and thus enables preventing the membrane electrode assembly misalignment at the existing fuel cell stack process. The handling of the membrane electrode assembly is improved without the rigidity. The positional accuracy between the gas diffusion layer and the membrane electrode assembly is improved. The distributivity of the reactive gases is improved. The effectiveness of the process is improved by decreasing the failure rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell.    Fuel cell (300)    Anode side separator (320)    Anode side gasket (330)    Convex unit (350)    Recess (360)
NOVELTY - Invention relates to agriculture. The method of environmentally friendly bioconversion of superfine metallurgical industry wastes containing heavy metals comprises creation of mixtures based on sand, metallurgical sludge, peat and calcium carbonate for growing plants, and for bioconversion the plants of fodder beet (Beta vulgaris L.), large-flowered flax (Linum grandiflorum), sweet corn (Zea Mays) and rapeseed (Brassica napus) are used.    USE - Agriculture.    ADVANTAGE - Invention enables to simplify the technology of obtaining organo-mineral fertilisers for agriculture in the process of biological recovery of metal production wastes.4 ex
NOVELTY - Preparing N-(3-ethynylphenyl)-6,7-bis(2-methoxyethoxy)- quinazolin-4-amine from 6,7-bis(2-methoxyethoxy)quinazolin-4(3H)-one, comprises treating starting compound with 3-aminophenylacetylene in the presence of titanium(IV) chloride and anisole in a solvent.    USE - The process is useful for preparing N-(3-ethynylphenyl)-6,7-bis(2-methoxyethoxy)-quinazolin-4-amine (claimed), which is useful for treating non-small cell lung cancer, pancreatic cancer, and several other types of cancer. No biological data given.    ADVANTAGE - The process is capable of preparing N-(3-ethynylphenyl)-6,7-bis(2-methoxyethoxy)-quinazolin-4-amine with good yield and purity (99%) and without using toxic reagents and isolating 4-chloroquinazoline intermediate in an environmental-friendly manner.
NOVELTY - A sintered compact for hydrogen production comprises lithium zirconate (Li2ZrO3) or lithium orthosilicate (Li4SiO4) as main component and has Brunauer-Emmett-Teller (BET) specific surface areas of 0.2-3 m2/g.    USE - A sintered compact used as powder for hydrogen production apparatus (claimed).    ADVANTAGE - Hydrogen production capability is excellent.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) powder for hydrogen production comprising lithium zirconate or lithium orthosilicate with BET specific surface areas of 0.2-3 m2/g; and    (2) hydrogen purification apparatus (1) comprising hydrogen production material (11) containing sintered compact and powder, reaction container (12) which accommodates hydrogen production material, pressure reduction unit (13) pressure-reduces the inside of reaction container, heater (14) which heats hydrogen production material in reaction container, purge gas supply unit which supplies purge gas (P) in reaction container, and hydrogen-permeable membrane (15) which selectively permeates hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the structure of hydrogen purification apparatuses. (Drawing includes non-English language text).    Hydrogen purification apparatus (1)    Hydrogen production material (11)    Reaction container (12)    Pressure reduction unit (13)    Heater (14)    Hydrogen-permeable membrane (15)    Purge gas (P)
NOVELTY - This utility new type claims a one high efficiency heat preservation marsh gas pool, wherein, a fermentation pool (10) two side is set with a feeding port (11) and discharging wherein (6), fermentation pool (10) inner wall is set with an annular oil storage tank (9), oil container (9) is set with the oil wherein (2), a fermentation pool (10) is inside set with U-type heating pipe (5) and humidity sensor (3), heating pipe (5) and humidity sensor (3) a connection controller (4), a fermentation pool (10) upper part is set with gas storage room (1), the gas storage room (1) on the top end set with pneuma collecting pipe (7), a fermentation pool (10) side is set with water pump (8), water pump (8) and controller (4) through lead. The biogas slurry is always in the most suitable gas temperature, which can reduce heat loss, so as to save electric energy consumption, marsh gas pool not affect of external environment, a automatic regulating temperature and humidity, of a content is a good organic fertilizer.
NOVELTY - Preparation of biogas fermented feed comprises mixing Lophatherum gracile, rhizoma cibotii, and keel, crushing, extracting with water to obtain medicine liquid, repeatedly purifying, and adding starch powder to obtain purified powder; mixing biogas residue, corn, fructus aurantii, amino acid, malt, and garlic oil, adding lipase while stirring, and plastic film sealing for 3 days, and fermenting at 60 degrees C; mixing the fermented material with peptide and calcium powder, adding Kudzu root, and sealing for 2 days at 45 degrees C; and uniformly mixing with the purified powder, and packaging.    USE - Method for the preparation of biogas fermented feed (claimed) used for increasing immunity of fowl.    ADVANTAGE - The method is simple and convenient, and increases egg production.
NOVELTY - This utility new type belongs to the sewage treatment device technology field, especially claims a sewage low frequency resonance mineral water, a the technology characteristic is: water storage tank comprising a in a pool and this in a water storage tank is connected, with a mineral layer set below the energy in a pool, a filter screen set up in the mineral layer, the floating frame set up in the filter network, set with at least one a table is provided with a vertical through hole a in the floating frame, set with a low frequency resonance head of low frequency resonator in in the vertical through hole, a low frequency resonance head is inserted into the vertical through hole inner. The water in a process after entering into a in a pool, a mineral substance layer in the low frequency resonator processing and can rapidly enter in to water, forming stable is rich in mineral substance is water, which is good for plant for absorption of minerals, increase disease resistance of plant, anti-pest ability, increase the crop yield, and can effective increase in soil mineral matter content, soil is not easy to plate, root system breathing effect enhance.
NOVELTY - This utility new type relates to a nursery stock one biological fermenting device of liquid fertilizer device, the first fermentation jar comprises material pool according to sequence a set of side by side, second fermentation jar, third fermentation jar, fourth fermentation jar four common a fermentation jar, a four fermenting jar through a corresponding of a connecting auger, material after a first fermentation jar for entering into a second fermentation jar continuously fermenting, turning. b the first times, after a second fermentation jar for entering into a third fermentation jar continuously fermenting, turning b. second times, after a third fermentation jar for entering into a fourth fermentation jar continuously fermenting, b. third time, after the material after the fourth fermentation jar for a Tool a fertilizer output after entering into the discharging pool use process. This utility new type is a four fermentation jar at the same time carry out a fermentation of different stage for biological fertilizer, and through a material between the fermentation jar for a material process, the fermentation effect is good, and material capacity is large, is suitable for mass production.
NOVELTY - This utility new type relates to compost technology field, especially a one compost fermenting device, comprising fermentation jar, the fermenting jar lower end mounted with a blast device, the top of the fermentation jar mounted with a waste gas processing device, the bottom of the fermenting jar mounted with a water outlet in the fermentation jar mounted with circulation cooling water pipeline, the water inlet of said cooling water pipeline below the fermentation jar end, the water outlet of said cooling water pipeline fermentation jar is located at upper end, the top of the fermentation jar mounted with spray pipe, a fermentation jar close to the inner bottom mounted with a filtering plate. The beneficial effect is: in a fermentation jar mounted with a temperature and humidity sensor, a pH detector and a fermenting jar inner mounted circulation water cooling pipeline and spraying pipe, it can regulate the fermentation condition of the fermentation jar inner a most suitable condition of growing a microorganism so as to obtain fertilizer effect is good, the nutrition component, high content of fermentation.
NOVELTY - This utility model claims a heating energy-saving marsh gas fermentation device, belonging to agricultural energy-saving environment-friendly technology. Comprising marsh gas fermentation tank 1, solar energy hot water device 2 and boiler 3 of the third main body part, the boiler is set inside of metal coil 3-4, and metal plate tube heating generation of water as the marsh gas fermentation tank is hot water supplying source. This new utility model or modify manufacturing is simple and economical, use of stove and combustion generation of heat, preventing or reducing of energy by the body absorb, at the same time then that of the sky and the marsh gas fermentation tank heat can supply not sufficient then generate efficiency reducing problem is.
NOVELTY - This utility new type claims a straw and pig manure one mix of Anaerobic digestion processing system, comprising straw crusher, pig manure sieving device and collecting pig manure domestication and reaction of Anaerobic digestion integrated reactor, a straw crusher and pig manure sieving device is connected and a Anaerobic digestion reactor, feeding wherein a set with an air outlet in the top part of a Anaerobic digestion reactor, the bottom set with material wherein the inner set with electric stirrer, at the same time a gas outlet with a gas collecting device. The use of straw and pig manure a. mix Anaerobic fermentation, it not only can process crop straw and pig manure the two a pollutant, but also can obtain clean energy. A whole treatment process in a substantially stable operation, average per day in 869-3232ml; yield a volume fraction of the maximum is 55.2%.
NOVELTY - This new utility model provide a kind of preparing one Promptly, wherein as one main body, the main body is one box, inner box has at least one electrolytic groove, outside main body has at least one water input pipe, a gas pipe and electric source wire, water pipe input electrolytic slot, power supply wire and electric power supply electrolytic slot, and with one gas tube for electrolytic production of hydrogen oxygen transporting groove main body to outside, wherein the outside main body has at least one group main switch shunt, in main body has at least one group before switching shunt, converter and rear conversion splitter, power source wire connected with main switch shunt, again input before switch shunt, again connected with transformer, after switching current and electrolytic groove in, before switching current divider, converter and rear conversion current divider can lap joint in electrolytic groove is multi-group, and can reach before switching shunt, converter and rear conversion current as unit, use before conversion and after conversion current divider assembly more electrolytic groove group, but can fast manufacture of hydrogen oxygen.
NOVELTY - This utility new type relates to a environment-friendly livestock and poultry without one harmless processing system, by housing the fermentation pool, crushing device, a conveyor, a smoke, pneuma collecting tank, a tank, second level filter, one filter level, a draught fan, a heating furnace compose, set with fermentation pool, shell body upper end of the fermentation pool and a cover corresponding to the set with a crushing device, the fermentation pool inner shell in lower end is set with a heating furnace, the fermentation pool is a side wall set with a sensor, a discharge wherein a fermentation pool is set with conveyor; side of fermentation pool is set with a first-stage filter and smoke, pneuma collecting tank, upper end of first-stage filter set with a level filter, wherein smoke discharge wherein a heating furnace is a fermentation pool are connected and smoke, pneuma collecting tank, smoke, pneuma collecting tank through a draught fan and fan pipeline and one level filter is a, first-stage filter and the second level filter through a conduit is connected with the set with a tank in a side wall of shell.
NOVELTY - This utility new type provide a silkworm dropping one vertical continuous solid compound fertilizer production device, set with solid mixer A continuous solid fermentation device, a packing, a solid mixer pump B, solid mixer A continuous solid fermentation device, a packing, a solid mixer B pump connect in turn, the a continuous solid fermentation device using the applicant the same day according to a continuous solid fermentation device, this device set with a vertical square structure, set with solid-liquid mixed unit, fermenting unit and drying unit, solid-liquid mixed unit setting a tower body upper section, lower fermentation unit setting in middle section of tower body, drying unit setting a tower section. The device material inlet is smooth, effective use energy, the fertilizer is fermentation time, increase solid fermentation efficiency, the device structure is simple, the operation is easy, the product quality stable, a little investment, can realize industrial production and has a good economic benefit, social benefit and ecological benefit.
NOVELTY - This utility new type claims a biological organic fertilizer and stacking one, belonging to the biological organic fertilizer production machinery device field, this biological organic fertilizer stack turning machine comprising supporting frame, a rotating disk and turning device, this rotating disk including a plate and motor, supporting frame mutually between the connection is set with rotating shaft of a electric machine base, motor set with a motor base up, this turning device comprising a bracket, a rotary motor and turn pile head, wherein bottom edge of two end a two end supporting frame and a rotating connection, a bracket and support frame of rotating connection and rotating connection of motor base and supporting frame are located on the same one straight line strip, and the other end and the electric machine base fixing connection, this end part is further set with a rotating rod, a rotating electrical machine set with 3 a, a center position, the angle is set with a mounting plate, rotating electrical machine rotating shaft is set with a mounting plate a, turn stack head set with a rotating shaft of rotating electrical machine a can for biological organic fertilizer turning process.
NOVELTY - This utility new one provide a vertical continuous solid fermentation device, set with a vertical square structure, set with solid-liquid mixed unit, fermenting unit and drying unit, solid-liquid mixed unit setting a tower body upper section, the fermentation unit setting in middle section of tower body, drying unit setting a section lower tower body; the fermenting unit set with supporting plate, circulation fan, an atomizing pipe, and temperature and humidity probe. The device set with uniform small holes is inclined bearing material plate, scraping plate and scraping plate, inlet and outlet material; set with heater, a fan, a circulation fan, a temperature and humidity probe, the drying and the fermentation condition of the fermentation time effective energy, the use of fertilizer, increase solid fermentation efficiency.. solid-liquid mixed room and sprinkle liquid pipe, it can ensure a mixed fermentation material, the continuous solid fermentation device structure is simple, the operation is easy, the product quality stable, a little investment, can realize industrial production, in particular granular agricultural products processing for febrile fertilizer effect, it has a good economic benefit, social benefit and ecological benefit.
NOVELTY - This utility model relates to a chemical fertilizer production device, specifically relating to a humic acid activation treatment urea humic acid reaction groove. Comprising shell, stir shaft set in inner shell is in a fixed mounting of a stir shaft upper blade, shell wall is set with heating coil, lower end is set with discharging housing wherein, upper end of shell body set with end cover, stir shaft through bearing is inserted in end cover up, stir shaft and driving motor transmission connection, upper end cover fixed install the first and a second hopper, the first hopper and the second hopper are set in a feeding spiral shaft, a feeding spiral shaft of upper end through bearing and bracket mounted at a centre of a through transmission device and a stir shaft transmission connection, wherein a discharge end of the feeding spiral shaft positoin b a is in, the feeding spiral shaft by shaft and fixed in a column in a shaft in a spiral piece. This reaction groove structure is reasonable, the energy consumption is low, the reaction raw materials according to the ratio, reaction process;
NOVELTY - This utility new type claims a submerged one filler type ammonia nitrogen degradation device, comprising a tank, a lower tank from bottom to top in turn a set with a water distribution room, a, filler layer and the water groove, a lower water distribution room from bottom to top in turn set with an emptying pipe, a water inlet pipe, pneuma reverse flushing system and distribution water distribution pneuma., one end the emptying pipe and the water distribution room is connected, and the other end extending to the outside of the water distribution room and set with an emptying valve, one end the inlet pipe is inserted into the inner of the water distribution room, and the other end extending to the outside of the water distribution room and set with water inlet valve, the water outlet groove and the water tube connected one, and this the up water pipe set with a water valve. This utility new type is submerged filler type ammonia nitrogen degradation device using the specific gravity is light, than the plastic filler table with a larger area of traditional water of reverse flushing system, reduces the operation energy consumption, simplify the operation program, the reverse flushing water processing system.
NOVELTY - This utility new type claims a one o-benzene dimethyl amine waste water processing system, comprising regulating pool and a phase of sedimentation pool, oxygen consumption pool inner set with a sedimentation pool, and oxygen consumption pool is set with a connected inner and a oxygen consumption pool, and is also set with concentrate pool is connected is, a concentrate pool lower end and sludge pool, the concentrate pool and nutrition liquid regulating pool is connected in inner pool, nutrition liquid pool and regulating the pH value regulating pool, pH value regulating pool and blowing system, stir. inner set with a regulating pool, adding a set with a regulating pool, aeration device rings in oxygen consumption pool section and facultative section, rotary table set with aeration device above a concentrate pool, clean water reflowing system set with a upper pool and oxygen consumption and . This utility new type is the purpose is provide a one simple structure, sewage treatment ability is strong, the processing effect is good, the production cost is low o-benzene dimethylamine waste water processing system.
NOVELTY - This utility model relates to a dewatered sludge aerobic fermentation device, comprising mixing crusher and fermenting unit, wherein, the fermentation unit by two rows of ferment groove group compose, set with two bar conveyor and arranged in the upper of a distributing machine and a machine in two rows fermentation groove. Using the utility model new the dewatered sludge aerobic ferment device, effective to avoid diffusion of odour in fermentation process, improving working environment and floor ferment site to accelerate fermentation speed of material.
NOVELTY - This utility new type relates to a organic fertilizer one turner, comprising machine frame, a machine frame set at the bottom of bottom disk walking device mounting a control device and a machine frame, wherein it further comprising the crushing mechanism, the crushing mechanism including a driving motor, driving shaft, supporting plate, left and right small bevel gear, a large bevel gear, left and right left and right driving chain wheel, left and right driven chain wheel group and the left and right two group combination . This utility new type turner with, crushing, mix and a multi function, it has good applicability and universality, and inlet device, it has simple structure, low cost, fit condition, high cost performance advantages and so on, it has good market prospect. This machine a greatly reduces labour requirement, increase production rate and reduces the work cost. In addition, organic fertilizer production field work environment comparing, odour smell bad, for body health of the worker working damage. Using remote control, which greatly reduces the worker directly entering into a probability of a field and improves the work environment.
NOVELTY - The utility model claims a new fermentation compost technology area, and claims of a kind of used for ferment compost is one taking device. The used for the trolley slide rail and taking ferment compost device set on two side wall of ferment groove to be taking and the upper edge of the trolley along the truss slide way moving, the mobile tower frame slide rail along vertical direction of said trolley is slide rail set up on the truss at, the mobile tower frame pulley along the mobile tower frame slide rail moving, the mobile tower frame of the pulley is set with with from the ferment groove for taking material of grab bucket, the car and the mobile tower frame corresponding to is set with pulley, and the unloading and moving tower frame pulley along direction of the mobile tower frame slide rail synchronous moving, the lower part of the car equipped with the transmission belt. This new utility model supply is used for fermentation compost is taking device not again by means of driver and loading machine equal manpower and material resources, greatly increase automation level and compost process, save manpower and material resources cost.
NOVELTY - One for hydrogen-oxygen generator is a plate pole piece, this utility new type relates to one used for hydrogen-oxygen generator is a plate pole piece, this utility new type in order to solve the existing technology in a hydrogen-oxygen gas generating efficiency low, safe stability, electrolytic groove volume is too high, in the existing technology when the adjacent pole piece distance is very close to happen short circuit, a liquid level inner piece processing technique is complex, the electrolytic groove is not stable, a pole piece including a pole piece plate, sealing element and one group baffle plate component, the plate piece is, pole piece plate close to one side of a periphery edge fixed mounted with a sealing element, group one plate component fixed in the mounting plate a piece close to the upper end of pole piece plate processing the pneuma hole close to the pole piece plate of lower end processing with electrolyte circulation pump outlet hole, liquid level balance hole and electrolyte circulation pump entrance hole, piece plate middle part processing with one group separating column mounting hole, the utility model is new type with the hydrogen in the field.
NOVELTY - This utility model claims a marsh gas storage cabinet pneuma and gas storage cabinet comprises marsh gas pool of this pneuma storage cabinet, a marsh gas storage cabinet comprising pneuma sludge pool and the sludge pool is connected at the bottom of the cabinet a pneuma connected at a sludge pool and a storage cabinet pneuma downward, and a sludge pool to the water outlet of the side wall, the cross section of the bottom of the cabinet is inner concave semi pneuma; between a marsh gas pool of this pneuma storage cabinet comprising main pool and water pressure, one side main pool is set with between the manure wherein the fermentation pool and water pressure chamber set with the excrement wherein, this the manure at the other side wall wherein the fermentation pool is up, the excrement is wherein a and the top end of the manure wherein are located on the same one horizontal line up, the bottom of fermentation pool from the manure wherein the side wall to a hydraulic pressure in a downward inclined and extending to overflow flow wherein water pressure between the side wall of the pool fermentation pool is set with a bottom is inner concave semi feces guide flow channel is spherical, the purpose is to supply a structure one is simple, the cost is low and use life of gas storage cabinet, and a gas pressure constant one, it is not easy to crust and marsh gas pool gas amount is larger.
NOVELTY - Two-jar supercharger comprises an upper and lower seal jars and funnel type water basket at the middle.    USE - Used as two-jar supercharger.    ADVANTAGE - The supercharger realizes pressurization, and high efficiency energy saving by mutual exchange of water vapor (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the two-jar supercharger.
NOVELTY - The method involves providing water vapor, a converging-diverging nozzle (24), and a combustion chamber (10). The molecules of water vapor are processed in an electric field, by passing molecules through an electric circuit (22) adapted to produce plasma. The water vapor is subjected to rapid thermal quench processing, by passing water vapor through the converging-diverging nozzle. The water vapor is subjected to a heat exposure by injecting water vapor into the combustion chamber at a temperature of 800 degrees C.    USE - Method for producing combustible gas. Uses include but are not limited to combustion- based device e.g. heaters, furnaces, incinerators, power generator, vehicle e.g. auto, aircraft, watercraft, aerospace propulsion system, and coal/waste gasification system.    ADVANTAGE - By the higher quench rates and subsequent exposure to heat, the water molecules are efficiently ruptured with minimum energy expenditures, and the hazard of explosion of the highly explosive gasses such as hydrogen and oxygen is eliminated. The fuel consumption required during the production of combustible gas is reduced. The issue of harmful gases in the air and low consumption of electric power supply are reduced. The high energy efficiency is obtained, by the utilization of plain water at room temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the method for producing combustible gas.    Combustion chamber (10)    Boiler (14)    Pump (16)    Electric circuit (22)    Converging-diverging nozzle (24)
NOVELTY - The method involves manufacturing first and second components including first and second gas channel structures. The first and second components are stacked with mutually facing gas channel structures with interposition of an electrolyte unit (7). The first and the second gas channel structures are manufactured by generative process preferably by laser, electron beam or steam jet sintering process. The first and second components are connected to one another preferably by material-fit or welding or soldering process or by the generative process.    USE - Method for manufacturing a fuel cell stack of a fuel cell or electrolyzer (all claimed).    ADVANTAGE - The first and second components are connected to one another preferably by material-fit or welding or soldering process or by the generative process, thus avoiding leakage problems, reducing manufacturing cost of the fuel cell stack in a simple manner and providing an optimized fuel cell stack.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a fuel cell stack    (2) a fuel cell or electrolyzer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining process of manufacturing a fuel cell stack.    Electrolyte unit (7)
NOVELTY - Method of disposal and decontamination of poultry manure comprises separation of biomass by separation into liquid and solid fractions, decontamination of liquid fraction by processing in the device with insoluble electrodes. The liquid fraction passed through the separator is mixed with lime milk in an amount of m Ca(OH)2=3.7.10-6 g/L (to remove ions of ammonium and phosphates). Then it is poured into a horizontal settler with an electrode system mounted throughout its volume and consisting of 7 flat carbon and graphite plates with the length of 30 m, the width of 2-3 mm with the distance of 5 cm between the plates where it is kept for seven and a half hours, affecting with nano-current of 40 nA.    USE - Agriculture.    ADVANTAGE - Invention enables to increase the efficiency of technology of disposal and decontamination of poultry manure, to reduce energy consumption and to reduce harmful emissions into the environment.1 dwg, 4 tbl
NOVELTY - Use of cow dung and straw for preparing organic fertilizer additive, is claimed, where the application method comprises cutting wheat straw into 8-12 cm, uniformly mixing cow dung and straw, fermenting the mixed material in a fermenting tank, raising the temperature to 50 degrees C, then stacking, inoculating bacteria into 400 ml of plate count agar culture medium comprising peptone, sodium chloride, calcium carbonate, yeast powder, tetracycline, cow dung and straw according to an inoculum size of 5%, then culturing in a culture flask, and filtering the seed culture liquid using a filter paper.    USE - The cow dung and straw are useful for preparing organic fertilizer additive (claimed).    ADVANTAGE - The cow dung and straw are capable of simply and economically preparing the organic fertilizer additive in an eco-friendly manner.    DETAILED DESCRIPTION - Use of cow dung and straw for preparing organic fertilizer additive, is claimed, where the application method comprises cutting wheat straw into 8-12 cm, uniformly mixing cow dung and straw in a volume ratio of 1:1, fermenting the mixed material in a fermenting tank, raising the temperature to 50 degrees C, reducing the temperature to 35 degrees C for 5 days to 1 times, then stacking at 4-12 degrees C, inoculating bacteria into 400 ml of PCS culture medium comprising 5 g of peptone, 4 g of sodium chloride, 3g of calcium carbonate, 1 g yeast powder, 0.025 g of tetracycline, 50 g of cow dung and 1 g of straw according to an inoculum size of 5%, then culturing in a culture flask, filtering the seed culture liquid using a filter paper.
NOVELTY - The device has throwing roller (6) which is connected to turning drive motor (20). End portion of stir pole is mounted with throwing material plate. Cross beam (10) is installed with baffle material door (11). First groove (13) is mounted with first belt conveyor (14). End of first belt conveyor is connected to fermentation pool (1). Second groove (16) is mounted with second belt conveyor (17). Widths of conveyors are same as bottom width of pool. Transverse platform (3) is mounted with spraying pipe (21). Pipe is connected to water storage tank (23) through soft pipe (22).    USE - Aerobic fermenting device of liquid fertilizer system.    ADVANTAGE - The aerobic fermenting device ensures the fertilizer to fully contact the air to prevent the over-high fertilizer stack temperature. The operator remote controls the aerobic fermenting device. The aerobic fermenting device is obtained with high efficiency. Continuous production of the aerobic fermenting device is obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the aerobic fermenting device of liquid fertilizer system.    Fermentation pool (1)    Transverse platform (3)    Throwing roller (6)    Cross beam (10)    Baffle material door (11)    Grooves (13,16)    Belt conveyors (14,17)    Turning drive motor (20)    Spraying pipe (21)    Soft pipe (22)    Water storage tank (23)
NOVELTY - Turning-throwing device lifting mechanism with turning-throwing machine comprises a turning-throwing mechanism and a hydraulic lifting rod. The turning-throwing mechanism is connected to a groove type turning-throwing machine walking trolley through a rotating shaft. The rotating shaft is fixedly arranged in a horizontal traveling trolley. The hydraulic lifting rod is set at one end of the walking trolley and the other end is connected to the turning-throwing mechanism. The hydraulic lifting rod is telescopic to drive the turning-throwing mechanism around the rotating shaft.    USE - The device lifting mechanism is useful for converting humus by biologically fermenting fungus dregs (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the turning-throwing device lifting mechanism with turning-throwing machine for converting humus by biologically fermenting fungus dregs.
NOVELTY - A soil fertility improved fertilizer comprises 35-45 pts. wt. peat, 12-25 pts. wt. ammonium bicarbonate, 14-25 pts. wt. phosphorite powder, 4-8 pts. wt. potassium mineral powder, 5-9 pts. wt. zeolite powder, 6-12 pts. wt. carbon powder, 4-6 pts. wt. diammonium phosphate, 3-7 pts. wt. ammonium dihydrogen phosphate, 0.01-0.02 pts. wt. silicate bacteria, 0.01-0.02 pts. wt. Bacillus cereus, 0.01-0.02 pts. wt. Bacillus thuringiensis, 25-30 pts. wt. cake, 25-30 pts. wt. chicken manure, 14-25 pts. wt. rice bran, and 10-16 pts. wt. wheat bran.    USE - Soil fertility improved fertilizer.    ADVANTAGE - The fertilizer can improve soil quality and it has enhanced fertility effect, long fertilizer efficiency, and no pollution.
NOVELTY - A 2-hydroxy-4-(3-pyridyl)pyrimidine derivative (I) is new.    USE - 2-Hydroxy-4-(3-pyridyl)pyrimidine derivative (I) used for preparing imatinib.    ADVANTAGE - The method is simple and easy, and has easy to obtain raw materials, and mild process condition. The imatinib preparation method has high yield and short process, produces imatinib with ideal purity, and does not use hazardous or toxic substances harmful to the environment.    DETAILED DESCRIPTION - A 2-hydroxy-4-(3-pyridyl)pyrimidine derivative of formula (I) is new.    R=1-8C straight chain or branch chain alkane, or benzyl, preferably methyl or ethyl.    An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - Preparation of moxifloxacin hydrochloride (II) comprises taking quinoline derivative (I) main ring chelate and (s, s)-2,8-diazabicyclo(4.3.0) nonane as raw materials, performing condensation reaction with acid-binding agent and solvent, treating salt by acidifying, crystallizing, filtering, washing, and drying. The condensation reaction solvent is alcohol.    USE - Method for preparing moxifloxacin hydrochloride (claimed).    ADVANTAGE - The simple method operates under low temperature and mild reaction condition, reduces impurity, saves energy, and saves steam for removing acetonitrile. It is suitable for industrial production.    DETAILED DESCRIPTION - Preparation of moxifloxacin hydrochloride of formula (II) comprises taking quinoline derivative of formula (I) main ring chelate and (s, s)-2,8-diazabicyclo(4.3.0) nonane as raw materials, performing condensation reaction with acid-binding agent and solvent, treating salt by acidifying, crystallizing, filtering, washing, and drying. The condensation reaction solvent is alcohol. An INDEPENDENT CLAIM is included for the synthesis of quinoline derivative (I) comprising heating acetic anhydride at 70-90 degrees C, slow adding boric acid, heating to reflux for 1 hour, cooling to 70 degrees C, stirring, adding 1-cyclopropyl-6,7-difluoro-1,4-dihydro-8-methoxy-4-oxo-3quinolinecarboxylic acid ethyl ester, heating to 100-105 degrees C, reacting for 1 hour, cooling to 0 degrees C, washing with water, filtering, washing crystals, and drying.
NOVELTY - Humic acid extracting device comprises fermentation jar (100), sludge injection port (110), alkali liquid injection port (130), sludge discharge port, upper layer clear liquid outlet and stirring device. The upper layer clear liquid outlet through pipeline is connected to centrifuge (200). The centrifuge through pipeline is connected to drier (400). The stirring device comprises motor (120) driven by rotary shaft (150), electric machine drive and stir rake (160).    USE - Device used for extracting humic acid from domestic sludge.    ADVANTAGE - The device has simple and convenient operation, and efficient extraction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the extraction of humic acid comprising injecting sludge into fermentation jar, injecting alkali liquid, mixing sludge and alkali, stirring for 20-30 minutes, standing for 2-3 hours, fermenting, transferring upper layer clear liquid into centrifugal machine, centrifuging and drying.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of humic acid extracting device from domestic sludge.    Fermentation jar (100)    Sludge injection port (110)    Motor (120)    Alkali liquid injection port (130)    Rotary shaft (150)    Stir rake (160)    Centrifuge (200)    Drier (400)
NOVELTY - A Streptomyces griseorubens JSD-1 laccase gene comprising a defined nucleotide sequence of 990 bp (SEQ ID NO. 2) and encoding a protein comprising a defined sequence of 329 amino acids (SEQ ID NO. 3), where the sequences are given in the specification, is new.    USE - The laccase gene is useful for producing laccase used for paper making and sewage treatment (claimed).    ADVANTAGE - The laccase protein has increased activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing S. griseorubens JSD-1 laccase gene.
NOVELTY - Microbial fermentation production of dehydroepiandrosterone (DHEA) using recombinant Mycobacterium smegmatis for single aqueous phase transformation of phytosterin for producing DHEA, comprises: (1) knocking out 5228up-kan-5228down; (2) construction of recombinant strains; and (3) fermentation, breeding and transformation of bacteria.    USE - The method is useful for the microbial fermentation production of dehydroepiandrosterone (DHEA) (claimed).    ADVANTAGE - The method has reduced production cost, DHEA quality yield is more than 90%; at the same time the method simplifies the extraction process, reduces the extracting cost, environment-friendly, and can be used in industrial production.
NOVELTY - Producing diosgenin involves releasing saponin from Dioscorea zingiberensis tubers, where the released saponin is then inoculated into a seed culture medium to obtain seed broth. Microbial transformation is performed by inoculating Aspergillus awamori and certain amount of seed broth into the fermentation medium. The obtained microbial transformed saponin yields diosgenin.    USE - Method for producing diosgenin from Dioscorea zingiberensis tubers (claimed).    ADVANTAGE - The method enables to produce diosgenin that has high biological conversion rate in an environment-friendly manner.
NOVELTY - The device has a hydrogen storage portion (30) that stores the hydrogen generated in the electric decomposition portion (10). The electric decomposition portion generates the hydrogen and oxygen. Second shifter pipe (40) is connected with the connection portion (41) and electric decomposition portion. First concatenated pipe (42) is connected with the connection portion. The electric decomposition portion and pyrolysis portion are connected with hydrogen storage portion. A combustion unit (50) is provided to spread the hydrogen gas.    USE - Combustion device for obtaining power from water mixed with hydrogen gas.    ADVANTAGE - The combustion device is environment-friendly. The inflammable article generated from the electric decomposition portion is immediately spread. The generation efficiency of the inflammable article is enhanced effectively. The generation of the hydrogen gas is promoted.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the combustion device for obtaining power from water mixed with hydrogen gas.    Electric decomposition portion (10)    Hydrogen storage portion (30)    Shifter pipe (40)    Connection portion (41)    Concatenated pipe (42)    Combustion unit (50)