NOVELTY - This new utility model aims to supply a kind of one can and the inner, outside heat type biomass pyrolysis furnace, comprising: furnace shell metal pot bottom, front and rear body, header and up and down and horizontal joint double taper double sand groove, vertical splicing joint fine sand sealing device composed of the sealing metal furnace shell and metal furnace and foundation bed stove, ignition, smoke pipe, an air (gas) pipe of two of 1/2 furnace liner connected with the assemble, metal heat guide silk, device, a draught fan, a chimney one. Smoke tube device shell of furnace, furnace liner in place furnace shell, an air (steam) pipe, metal heat guide silk insert furnace liner. The pyrolysis furnace convenient to carry, fast humidity, uniformity, fast cooling, simple operation, high yield.
NOVELTY - This utility new type biomass dry distillation for the pneuma., comprise mutually connected a dryer, vacuum machine, machine, separator, a condenser, a filter, a drier one side set with a crusher, a separator, a condenser, an outer filter are coated with thermal insulation layer, said filter further in turn with a Roots blower and a water seal, a Roots blower and water seal device set with a check valve, a rear water sealing the other side in turn connected with the air bag through air intake header pipe connect household fire arrestor, a air inlet pipe set with pneuma total valve. This utility new type structure is simple, operation is convenient, efficient of a rural straw and so on for waste gas, a recovery, the beautifying the rural environment and produce a considerable economic benefit.
NOVELTY - This utility new type provide a one biomass gas purification device. One said biomass gas purification device comprise a material mix cavity and dispersed in the purification chamber, a feeding port of the dispersing purification cavity of a material mix cavity connected, and a cavity are two seal a lower is in the working state, set with biomass raw material input port and a gas conveying tube connected with the biomass a material mix cavity of gas entrance and gas entrance set with input port of biomass raw material, stir dispersing device set with inner dispersion purification cavity, the discharge port on the lower part set with a dispersed purification chamber. This utility new type by biomass itself having a absorbing function, for the biomass gas purification process, a biomass gas purification can be only a rear, absorbing impurity of biomass raw material entering into dispersion chamber, dispersing the lower stir of dispersing device, rear crushing a continuing use, which greatly saves resource, reduces the operation cost, but also solves the problem that the post is not good purification of sewage.
NOVELTY - The utility model claims a new preparation device of biologic diesel oil, especially one from waste lipid and a kind of preparing biological diesel oil and device. This new utility model includes main reaction kettle, upper main reaction kettle cover and kettle reaction liquid feedstock port and remove glue substance under end kettle wall of reaction kettle is set with light phase outlet is connected, main reaction kettle and reacting mixing liquid outlet of connected to centrifugal pump, centrifugal pump input standing separation kettle top to the reaction mixed liquid feeding port, a standing separation kettle low end kettle wall provided with biologic diesel oil outlet. The utility model not only solves the updated of production chroma problem is, of course not too would use concentrated vitriol equal the corrosive agent, operation environment safety relative, to equipment requirement low. Put in device, small area small, and it will not generate second time waste and pollute water.
NOVELTY - This utility new type belonging to the waste water treatment field, claims a one with micro-computer water controller of acid-base waste water processing device, comprise in turn pipeline connecting a lattice well, a sedimentation tank, a first filter tank, a microorganism reaction tank, between the second filter tank, a sterilizing tank and dechlorinating tank, a first filter pool and microorganism reaction tank set with a micro-computer water acid-base controller, used for avoiding a floating excessive pH for microbial damage; a second filter tank and a pipeline of the sterilizing tank is set with plate frame filter, used for collecting microorganism and fermentation product to prepare a fertilizer. This utility new type aiming at different size and pollutant of variety, using various deposition medium and filter medium a multi-heavy absorbing, avoids the residue of harmful chemical substance.
NOVELTY - A domestic one wet garbage treatment device, in turn include wet garbage raw material unloading mechanism, wet garbage raw material bearing and feeding mechanism, wet garbage raw material selecting and wet garbage rough belt-type conveying mechanism, wet garbage rough crushing mechanism, first wet garbage fine material belt conveying mechanism, fine wet garbage dewatering mechanism, the fermentation material and add fungi mechanism, second wet garbage fine material transmitting mechanism, wet garbage fine material stir mechanism and compost material bearing mechanism, each adjacent mechanism are set with a plurality of through a belt conveyor is one a whole automatic operation of a complete device. Wet garbage raw materials for selected rear to be rough, the rough rear wet garbage crushing into a fine wet garbage, wet garbage fine material by dehydrating a rear fermentation material and add a stir fungi, entering into fertilizer by processing technology. Whole device is a automatic operation, working efficiency is high, cost is low, aritificial compost processing effect is good, the waste, the waste is changed into treasure, which meets the national industry standard.
NOVELTY - This utility new type claims a improved organic waste resource one fast a thremal enzyme. The device by machine frame, U type reaction kettle, motor, a gear transmission device, a speed reducer, a hammer head type stir blade, outer wall of fill material layer, the reaction kettle outer steel plate, and temperature control, two for electric hair dryer, an electric control cabinet, 1 group or several group weir top cover, a trumpet port, an exhaust port, a glass observation window, a discharge valve switch pneuma and aerosol separator of filter screen. Horn-shaped feeding reaction kettle top end by the original flat structure into a weir type structure, fixing the top cover up one end 1 a with a flashboard and a exhaust port 3 with a filter screen. This utility new type on the premise of satisfy waste thremal enzyme fermentation, and at 18-24 hours of low resource utilization, collecting water, at the same time it has function of removing peculiar smell, the fermentation process can be valid energy consumption is reduced 10 %-30 %.
NOVELTY - This utility new type relates to a one application to the aerobic compost of a cabinet, include a cabinet body, a cabinet body one side surface plate is provided with a material entrance, a material entrance set with a sliding door, a cabinet body set with one inner groove frame, a groove frame and the cabinet body through several connecting rod, and inner wall of groove frame and the cabinet body and is used for forming airflow in a wind channel, a groove wall of said groove frame is set with air hole, groove of said frame groove to bottom basin structure, and a groove bottom wall is provided with excess percolate out of discharge port, said discharge port by one control valve and a collecting tank is fixed on the cabinet body side wall upper connecting, the top part of said cabinet body set with one valve by control of an air outlet, said air outlet set with a active carbon for absorbing odour of bag, a cabinet body lower side wall set with a wind channel is connected with a air blower. This utility new type has simple structure, convenient operation, it can satisfy valid compost work requirement, but also for the environment also has a good protection effect.
NOVELTY - This utility new type provide the one a rough organic fertilizer processing system, include conveyer, turner, the turner, material groove, a conveyor, turner, material groove by up to low in turn mounting, a conveyor to mixing machine exit of entrance, mixing machine of exit through guide tube and opposite to the upper part, and the memory material groove; a ground and include turn frame and moving a polishing, polishing turn frame memory material groove bottom, moving a stage of memory material in a groove. This utility new type through whole set structure is of simple structure, the organic fertilizer rough treatment effect of a base, which ensures the enterprise cost is low, operation is easy, and organic fertilizer production enterprises realize automatic production with low cost and provide the good is a condition.
NOVELTY - This utility new type aims to provide a one organic fertilizer stacking, belonging to the field of organic fertilizer manufacturing technology field, in order to solve the existing technology in a single stack turning machine is suitable for range is small, at the same time, can only fix one over a horizontal plane, working efficiency is low, the draft depth and so on. The manure include walking device, turning device to stir lifting device, walking device comprise a walking machine frame, a walking motor, speed reducing mechanism, and set with two-section through a stir device of detachable structure, and a material height according to a turning rack of regulating extending length of stir device, increase range of suitable for turning and turning efficiency and increase quality.
NOVELTY - This utility new type provide the a one organic fertilizer turner include a block, a connecting rod, a turn throwing frame, a polishing turn frame is inverted V type, a moving block and turn polishing frame number are two more than a two per a mobile block set with a one turn throwing frame, a moving block and turn polishing frame through a connecting pole fixed. This utility new type) structure is simple, manufacturing cost is low, it does not need the multi-motor, little energy consumption, all a a a a a a, operation is simple, components, the eye can be seen understood, any easy to maintain.
NOVELTY - This utility new type relates to a one household organic fertilizer production device, belonging to the field of organic fertilizer production application technology field. It comprise straw crushing device, excrement processing device, mix stir device, a fermentation device, a straw crushing device, excrement processing device and a fermentation device through a connecting pipeline. This utility new type has simple structure, low production cost, small area, convenient to carry, the raw material to organic fertilizer finished product of integrated production device, crushing device crushing the straw into a powder, and excrement processing device processing a waste inner entering into fermentation treatment device with a fermentation, fermenting the organic fertilizer finished product is a fluffy shape, is brown, slightly with wine fragrance or soil smell, rich nutrition for fruit and vegetable, cash crop, flower nursery stock nutrition soil, value increment number.
NOVELTY - This utility new type claims a polyglutamic acid one straw covering combination production line, include flushing frame, a,, rinse wheel, screen, a conveyer belt, a washing machine spraying pipe, horizontal conveyer belt, wall-breaking machine, spiral packing auger, a juice extractor, concentrator, a fermentation tank, a circulation bin, regulating pH, membrane filter, air purification, culture liquid chamber, a membrane filter, a mixer, a drying machine, a granulator and packing machine, a polyglutamic acid wheat straw covering combination production line by the cleaning unit, extracting unit, the fermentation unit and covering unit. This utility new type using, concentrate technology prepare wheat extract liquid, and gamma-poly glutamic acid liquid wheat extract liquid with a mix, so that large amount of nutrition element in extract of wheat straw, microelement, active enzyme is gamma-poly (glutamic acid) covering, covering compound through low temperature vacuum drying, a gamma-poly (glutamic acid) straw covering combination, rich in nutrient supply of excellent fertilizer.
NOVELTY - This utility new type provide the one a simple organic fertilizer fermentation overturning and throwing machine, include polishing turn frame, a baffle plate, a motor, a connecting rod, a turn polishing frame is hollow cuboid, the upper lower; said turn polishing the top and the inner side of the bottom frame strip groove turn throwing width of baffle frame is set the strip-shaped inner groove, a polishing frame one end turn end surface centre fixed with a connecting rod, a motor power output shaft through connecting rod to turn polishing frame rotate. A strip-shaped groove end part of the turn throwing the outer side set with angle of a lock catch. This utility new type) structure is simple, manufacturing cost is low.) operation is easy, and it is easy to popularize, less component and easy maintenance.
NOVELTY - This utility new type claims a one organic fertilizer fermenting tank, comprise tank body and the tank body inner set with a stir device, a tank body side wall by wall, back wall and bottom wall plate, said upper side wall set with a stir driving shaft mounting hole and the driven stir shaft mounting hole, a stir device by motor, a driving shaft and a driven stir stir shaft, output end of said motor and the driving stir shaft, a driving shaft and a driven stir stir shaft mounting a stir shaft mounting hole on the driving and driven shaft mounting a stir hole, and through transmission belt driving, said tank body is also set with a seal cover. This utility new type through motor driving stir device, the stir device with a stir enough force, which can ensure the fermentation culture medium of the fermentation tank turning inner uniformity, which is more helpful for aerobic fermentation of a, that is, solves the problem that the current technology exist wastes time and labour, labour strength of high technology, and increase production efficiency and ensures the fermentation quality.
NOVELTY - This utility new type provide the a one organic fertilizer, include upper tube, lower tube, leaf, leaf, leaf, a upper tube, lower tube upper lower connecting along the direction vertical to a axis, axis a tube in the horizontal direction is provided with shaft lower tube in; shaft and a shaft, a a fixed shaft is sleeved with leaf, leaf, leaf, a leaf number is two or more, a lower stirring shaft along the circumference uniform distribute; said blade and blade number is four or more, a along a axis, axis of centre circumferential uniform multi-layer distribute, and , and , are between the different layer, lower cylinder body at the bottom is a discharging opening. This utility new type through a mixing leaf, leaf, leaf of structure, and opening and closing the discharge hole of a structure, the low cost, simple operation of low so that the fertilizer fully, stir uniform.
NOVELTY - This utility new type relates to a farm chemical preparation, especially claims one one a chlorpyrifos microcapsule suspension agent. The chlorpyrifos microcapsule suspension agent, a core outer in turn is covered with inner layer shell and the outer layer shell, a core is chlorpyrifos liquid, said inner layer outer shell to said core, one with an opening of the ball structure or similar ball structure, said outer shell wrapped on said inner layer shell. This utility new type is a one type environment-friendly preparation chlorpyrifos coating of oil-soluble in the hollow micro-sphere, the increase of a pesticide farm chemical microcapsule through rear. Chlorpyrifos can continuously volatilizing, killing the soil in survival harm of underground pests, a period up to 2 months in a the soil is one of preventing and curing crop underground pests most ideal medicine preparation.
NOVELTY - The method involves mixing a building rubbish nutrition soil with distribution material. A nutrition earth sheet is conveyed to a belt-type microwave drying sterilization machine. The building rubbish is dried under low temperature of a sterilizing device. The building rubbish nutrition soil is cooled and packaged in the nutrition earth sheet. The building rubbish nutrition soil sheet is conveyed to a heat-insulating sterilizing unit. Liquid of a concave convex stick stone is leached. A pH value of sludge is 5.0-7.0 in a sludge natural fermentation process.    USE - Building rubbish nutrition soil manufacturing method.    ADVANTAGE - The method enables containing nitrogen, phosphorus, potassium and organic matter with building rubbish for providing plant growth of a nutrition element, reducing pathogenic bacteria and pest harm for a plant to achieve normal growth and development of plant with better ecological environment.
NOVELTY - Substrate material, produced by (i) taking 60-70% Chinese chestnut preserved fruit, 10-20% sawdust, 15-20% wheat bran, 0.5-1% tea seed cake, 0.5-1% precipitated calcium carbonate and 1-1.5% sugar, (ii) treating Chinese chestnut preserved fruit and sawdust to remove impurities, and (iii) taking the treated Chinese chestnut preserved fruit and sawdust, and then adding wheat bran, tea seed cake, precipitated calcium carbonate and sugar, stirring by adding water to mix, and adding a base material and water in ratio of 1:1.25-1.3, and regulating the pH to 7-7.5, is claimed.    USE - The substrate material is useful in the production of mushroom.    ADVANTAGE - The method reduces the utilization rate of raw materials; is economical; has simple, and easy operation procedures; and simultaneously carries out fermentation of wooden meal and Chinese chestnut preserved fruit under decomposition effect of wood fiber, and conducive to mycelium growth after inoculation; and shortens the mycelium incubation period.
NOVELTY - Preparing matrix material comprises weighing and taking 60-70 wt.% of Chinese chestnut preserved fruit, 15-25 wt.% of sawdust, 15-20 wt.% of wheat bran, 0.5-1 wt.% of calcium superphosphate, 0.5-1 wt.% of gypsum and 1-1.5 wt.% of sugar, performing harmless treatment of the Chinese chestnut preserved fruit and sawdust, adding the wheat bran, calcium superphosphate, gypsum and sugar, then adding the mixture and water in a ratio of 1:1.25-1.3, stirring the mixture and regulating the pH value to 6.5-7.    USE - The matrix material is useful for planting white fungus (claimed).    ADVANTAGE - The method simply and easily prepares the matrix material with improved utilization of raw materials and increased production efficiency at low cost.
NOVELTY - Continuous process for production of ammonium sulfate in combination with caprolactam involves: (a) neutralizing with ammonia a mixture comprising caprolactam and sulfuric acid; (b) separating the aqueous ammonium sulfate phase from the aqueous crude caprolactam phase; (c) extracting into an organic solvent caprolactam present in the aqueous ammonium sulfate phase; (d) stripping organic solvent from the purified aqueous ammonium sulfate phase; and (e) withdrawing organic solvent-containing gas produced in, or subsequent to, any one of steps (c) and (d).    USE - The continuous process is useful for production of ammonium sulfate in combination with caprolactam (claimed).    ADVANTAGE - The process has the particular advantage that a lower amount of organic solvent is consumed in the process, because organic solvent is recovered, and may be reused in the process. Accordingly, it is neither released to the environment, nor burned, generating harmful waste products.    DETAILED DESCRIPTION - Continuous process for production of ammonium sulfate in combination with caprolactam involves: (a) neutralizing with ammonia a mixture comprising caprolactam and sulfuric acid to form an aqueous ammonium sulfate phase and an aqueous crude caprolactam phase; (b) separating the aqueous ammonium sulfate phase from the aqueous crude caprolactam phase; (c) extracting into an organic solvent caprolactam present in the aqueous ammonium sulfate phase to form a caprolactam-containing organic phase and a purified aqueous ammonium sulfate phase; (d) stripping organic solvent from the purified aqueous ammonium sulfate phase; and (e) withdrawing organic solvent-containing gas produced in, or subsequent to, any one of steps (c) and (d); and (f) organic solvent is recovered from the organic solvent-containing gas.
NOVELTY - A hydrogen dissolved water generator comprises electrolysis part (2) consisting of anode (14) and cathode (15) and liquid feeding path (5) which introduces acidic water (W1) into electrolytic cell (1) with which cathode is installed and is equipped with liquid feeding tube (8) and liquid feeding pump (9) interposed in the middle of the liquid feeding tube. The water generator mixes acidic water containing hydrogen ion and oxygen which are produced by the anode with alkaline water containing hydroxide ion and hydrogen which are produced by the cathode.    USE - A hydrogen dissolved water generator (claimed).    ADVANTAGE - Hydrogen dissolved water with large amount of dissolved hydrogen can be obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen dissolved water generator.    Electrolytic cell (1)    Electrolysis part (2)    Liquid feeding path (5)    Liquid feeding tube (8)    Liquid feeding pump (9)    Anode (14)    Cathode (15)    Acidic water (W1)
NOVELTY - Konjak cultivation involves fermenting sheep manure using an airtight plastic cloth seal at high temperature for 10-20 days. Planting strips are opened (15-20 centimeters), and then konjak is planted in fine soil (4-5 millimeters grain diameter). The fermented sheep manure is applied one time, and then covered with a layer of fine soil 3-5 centimeters thick.    USE - Method for cultivating konjak (claimed).    ADVANTAGE - The method enables to produce the product that is safe, eco-friendly, and has improved the organic matter of soil, yield and stress resistance of crops.
NOVELTY - The method comprises placing the animal carcasses into crusher and then absorbing water using substances including sawdust, crop straw, wheat bran, corn powder, bran shell and grass, than passing the mixture into microbial fermentor comprising a stirring device and a bacteria spraying device, adding microbial agents, and then heating to generate solids and gases separately and then directly passing into a gas purification device comprising an air inlet and an air outlet at 800-1000 degrees C. The method is carried out using a fixed or movable device.    USE - The method is useful for disposing animal carcasses (claimed).    ADVANTAGE - The method safely disposes the animal carcasses with reduced energy consumption in an eco friendly manner.
NOVELTY - Preparing organic fertilizer, comprises collecting edible mushroom waste, then washing with water, drying and crushing in a fertilizer machine.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The slow release organic fertilizer can be easily absorbed by plant, and improves the nutrition content in the soil.
NOVELTY - A honeysuckle special organic fertilizer comprises 20-50 wt.% dry chicken manure, 10 wt.% mushroom, 5 wt.% pepper, and 35-65 wt.% lees.    USE - As honeysuckle special organic fertilizer (claimed).    ADVANTAGE - The honeysuckle special organic fertilizer has strong pertinence, and good effect; and promotes yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the honeysuckle special organic fertilizer involving weighing dry chicken manure, mushroom, pepper, and lees, mixing uniformly, fermenting at 70 degrees C for 4-10 days, drying at low temperature, grinding fertilizer, and mixing uniformly to obtain the product.
NOVELTY - A sewage processing system one ammonia nitrogen early warning standard integrated device, wherein it comprise ammonia nitrogen monitoring early warning unit (1), said ammonia nitrogen monitoring early warning unit (1) and agent metering module (2) is connected with the said agent metering module (2) is connected with the activate/cultivation device (3) a, a metering agent. (2) the fungus, the cultivation nutrition liquid according to monitor measuring a conveying to activate/cultivation device (3). This utility new type provide a. ammonia nitrogen sewage early warning standard integrated device can be efficient in a stable monitoring sewage ammonia nitrogen content and a risk pre-warning, it solves the automatic add ammonia nitrogen degrading strain for sewage treating sewage ammonia nitrogen standard, aritificial save cost, increase the sewage treatment capacity.
NOVELTY - This utility new type claims a one dry and wet fermentation methane tank, isolated comprise a fermenting tank body (1) and tank cover (2), a fermenting tank body (1) include sewage treatment tank (3) and dry fermentation tank (4), a sewage tank (3) and the water inlet (5) and water outlet (6) is connected with a dry fermentation tank (4) is set with the sewage treatment tank (3) in, the two through vent tube (7) is connected, forming a common gas storage room (8), the marsh gas tank a dry fermentation tank and a relative independent of the sewage treatment pool, a sewage in sewage treatment pool would not overflow vine to dry in a fermenting tank, valid for a protection of dry fermentation tank, the fermentation in a dry fermentation tank smoothly proceed when the vent tube cut off time, open time dry fermentation tank cover taking the input/change operation, would not interference normal operation of sewage treatment tank, a the use of marsh gas.
NOVELTY - The cabinet has exhaust gas storage cabinet (18) whose top portion is provided with gas tube (20). One side wall of sludge tank (19) is connected with water outlet (21) and other side wall is connected with exhaust gas storage cabinet. The sludge tank is connected at bottom portion of storage cabinet along specific direction. The gas tube is provided on top of cabinet and is provided with safety valve (22). Water inlet device (24) is connected at bottom of storage cabinet. Water discharging device (25) is connected at bottom of sludge water outlet of sludge tank.    USE - Marsh gas storage cabinet of marsh gas tank.    ADVANTAGE - The structure of the cabinet is simplified and the manufacturing cost is reduced. The lifetime of the storage cabinet is prolonged. The gas quantity can be increased. The fermentation temperature of fermentation tank can be ensured, so as to ensure the gas production. The quality of the fertilizer is increased and the ecological environment is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of marsh gas storage cabinet of marsh gas tank.    Exhaust gas storage cabinet (18)    Sludge tank (19)    Gas tube (20)    Water outlet (21)    Safety valve (22)    Water inlet device (24)    Water discharging device (25)
NOVELTY - The SOFC has a fuel rod assembly with a fuel rod which comprises an outer wall enclosing a hollow longitudinal conduit. An outside diameter of each tube stub is engaged with a flexure through hole with an interference fit that provides a mechanical retention force suitable for holding the fuel rod in place and maintains a gas tight seal between the outside diameter of the tube stub and the inside diameter of the base wall through hole when the fuel rod assembly is operated at temperatures ranging from 500 degree to 1000 degree.    USE - Solid oxide fuel cell for generating power.    ADVANTAGE - The annular flexures eliminates the need for potting of the rod ends. Thus the assembly labor is reduced, the reliability is improved, and the rod removal for cleaning and or replacement is allowed. The SOFC stack is provided with rod end and annular flexure configurations formed to allow assembled rod ends and end plates to be held in place by clamping forces generated by annular flexures. Thus the flexibility of the annular flexures enables bending and twisting of the assembly without breaking or cracking the rods. The reduced material thickness of the annular pattern reduces the mechanical stiffness of the annular pattern as compared to the mechanical stiffness of the surrounding end plate.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of the endplate.    End plate (1200)    Flexure insert (1220)    Hole (1225)    Backing plate (1230)    Mating surface (1238)
NOVELTY - Crystalline form of apixaban (I) having X-ray powder diffraction pattern as given in the specification is new.    USE - (I) is useful as an antithrombotic agent. No biological data given.    ADVANTAGE - (I) is prepared with less hazardous in an efficient and eco-friendly manner. (I) is easy to process, and has high purity (99%) and improved storage stability.    DETAILED DESCRIPTION - Crystalline form of apixaban of formula (I) having X-ray powder diffraction pattern as given in the specification is new. INDEPENDENT CLAIMS are included for:    (1) an isolated intermediate of apixaban comprising 6-(4-(5-bromopentanoylamino)phenyl)-1-(4-methoxyphenyl)-7-oxo-4,5-dihydropyrazolo(3,4-c)pyridine-3-carboxamide (IIA), 6-(4-(5-chloropentanoylamino)phenyl)-1-(4-methoxyphenyl)-7-oxo-4,5-dihydropyrazolo(3,4-c)pyridine-3-carboxamide (IIB) and 1-(4-methoxyphenyl)-6-(4-nitrophenyl)-7-oxo-4,5-dihydropyrazolo(3,4-c)pyridine-3-carboxamide (IVA);    (2) an amorphous form of ethyl 6-(4-aminophenyl)-1-(4-methoxyphenyl)-7-oxo-4,5-dihydropyrazolo(3,4-c)pyridine-3-carboxylate (III) and (IIA), and a crystalline form 6-(4-aminophenyl)-1-(4-methoxyphenyl)-7-oxo-4,5-dihydropyrazolo(3,4-c)pyridine-3-carboxamide (II), (IIB), ethyl 1-(4-methoxyphenyl)-6-(4-nitrophenyl)-7-oxo-4,5-dihydropyrazolo(3,4-c)pyridine-3-carboxylate (IV) and (IVA) characterized by an X-ray powder diffraction; and    (3) an improved process for the preparations of apixaban (I).
NOVELTY - The system (100) has air supply device (9) to supply combustion air to combustor (1). Waste gas from combustor flows into waste gas flow path (3) and carbon mono-oxide detector (4) detects carbon mono-oxide in waste gas. Temperature detector (6) detects temperature of waste gas. Controller (7) detects abnormality of waste gas flow path based on change in detected temperature with respect to change in heating amount of waste gas by heater and to change in output of fuel-supply device (19) and/or air supply device, when waste gas is flowing through waste gas flow path.    USE - Electric power generation system.    ADVANTAGE - The abnormality of waste gas flow path is detected from the detected temperature of temperature detector, and the state which inhibits carbon mono-oxide detection is known appropriately, while the possibility that waste gas does not reach temperature detector and carbon mono-oxide detector is increased and the possibility of leak of carbon mono-oxide from waste gas flow path is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for operating electric power generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the of the electric power generation system. (Drawing includes non-English language text)    Combustor (1)    Waste gas flow path (3)    Carbon mono-oxide detector (4)    Temperature detector (6)    Controller (7)    Air supply device (9)    Fuel-supply device (19)    Electric power generation system (100)
NOVELTY - A method of treating animal waste, involves locating farm slurry in a receptacle, introducing air into the slurry via air diffusion to provide dissolved oxygen level of 0.5 mg/l-1 to 2 mg/l-1, thereby creating aerobic conditions in the slurry, monitoring and optionally adjusting the pH level of the slurry to be 6 to 8, and adding a mixed culture of Bacillus and nitrosifying and nitrifying bacteria to the slurry.    USE - For treating animal waste (claimed) to enhance the natural nutrients for use as a fertilizer.    ADVANTAGE - The introduction of oxygen has an immediate effect of promoting activity with the existing native heterotrophic aerobic bacteria, which will grow, regenerate and multiply. The bacteria rapidly degrade organic solids and debris composing of fats, proteins, carbohydrates and cellulose. The aeration eliminates anaerobic activity, which produces hazardous slurry gases and pungent odors. The method improves the situation of the farmer regarding farm slurry management, regarding its safety, practicality, and efficiency. The method provides a comparatively effortless and simplified process that utilizes only minimal involvement by the farmer. The method exhibits improved efficiency and practicality.
NOVELTY - The method involves supplying nitrogen and carbon dioxide in an electrolysis process with water and hydrazine carbonate, where the water and hydrazine carbonate are isolated in a form of a solid or in form of a concentrated solution of the mixture. The nitrogen and the carbon dioxide are fed in the form of atmospheric air. The hydrazine carbonate is converted into hydrogen, carbon dioxide, nitrogen and water, where the hydrogen is used as energy carriers and sunning energy is converted into electricity by using a solar plant.    USE - Method for storing energy e.g. solar power and electricity (all claimed).    ADVANTAGE - The method enables reducing nitrogen in reactors by using solar current, so that other energies utilized for generation of energy carrier hydrazine carbonate can be eliminated in an easy manner, thus achieving better electrical conductivity in an effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for deploying an energy carrier.
NOVELTY - A protein is new. The protein is chosen from (a) protein comprising a 495 amino acid sequence (SEQ ID NO: 4) fully defined in the specification, (b) endoglucanase comprising amino acid sequence of SEQ ID NO: 4 in which one or more amino acids are deleted, substituted and/or added, and (c) endoglucanase comprising amino acid sequence having /-70% identity with amino acid sequence of SEQ ID NO: 4.    USE - The protein or cellulase preparation is useful for saccharifying biomass containing cellulose, deinking paper, improving filterability of paper pulp and improving digestive ability of animal feed. The biomass is fiber material (all claimed).    ADVANTAGE - The protein is specific and produced by inexpensive method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) polynucleotide comprising base pair sequence that encodes for the above-mentioned protein;    (2) DNA chosen from (a) DNA comprising a 1839 base pair sequence (SEQ ID NO: 3) fully defined in the specification or its modified sequence, (b) (i) DNA encoding for the protein, (ii) DNA comprising base pair sequence at position 128-1615 of SEQ ID NO: 3, or (iii) DNA comprising base pair sequence at position 128-1615 of SEQ ID NO: 3 and encoding for protein which hybridizes under stringent conditions and has endoglucanase activity, and (c) DNA lacking base pair sequence that encodes for signal sequence from DNA (a) or DNA (b);    (3) expression vector comprising the polynucleotide or DNA;    (4) host cell transformed the above-mentioned expression vector;    (5) method for manufacturing the protein involves culturing the host cell and extracting the protein from the culture;    (6) protein produced by the above-mentioned method; and    (7) cellulase preparation comprising the protein.
NOVELTY - Reclamation of green tailing comprises selecting mine waste tailings, adding peat soil modifier and wood chips to the tailings to obtain a matrix, and adding 20-30 g/m2 of water retaining agent to the matrix. The weight ratio of peat soil modifier, wood chips and the tailings is 2-4:0.8-1.2:0.8-1.2.    USE - The method is useful for reclamation of green tailings (claimed).    ADVANTAGE - The method allows the reclamation of green tailings without using foreign soil as plant growth substrate in an eco-friendly manner, and is capable of reducing the accumulation of mine tailings.
NOVELTY - Planting Dendrobium candidum using construction material comprises e.g. selecting plane planting Dendrobium candidum plant material by selecting e.g. barks, fill material, sawdust, crushed tree pieces and stem crushed grain sheet, selecting construction material which is angle iron and metal welded bed body, paving bamboo, wood, and asbestos mixture to construct bed body, using plant bearing material, constructing load bearing bed body material, selecting sand brick, brick, red brick, cement block used for constructing standard brick, planting around the edge of the bed.    USE - The method is useful for planting Dendrobium candidum using construction material (claimed).    ADVANTAGE - The method has great effect of changing waste material into valuable product, and is environmentally friendly.    DETAILED DESCRIPTION - Planting Dendrobium candidum using construction material comprises (i) selecting plane planting Dendrobium candidum plant material: selecting barks, fill material, sawdust, wood tip, crushed tree pieces, and stem crushed grain sheet without rot, (ii) selecting construction material which is angle iron and metal welded bed body construction materials, paving 1.5-6 cm of ceramic tile strip with bamboo, wood, and asbestos mixture to construct bed body, (iii) using plant bearing material of new and old shading net and metal mesh, plastic mesh, bamboo skin, wood and tree bark, (iv) constructing load bearing bed body material i.e. bed body foot, selecting sand brick, brick, red brick, cement block is used in constructing standard brick, mixing metal, bamboo or wood, (v) the width of bed body is 100-200 cm, height is 30-120 cm, (vi) planting around the edge of the bed, selecting bamboo, wood, metal, plastic, and plant, and filling nutrition cup with plant material, and (vii) planting Dendrobium candidum plant material of height 5-15 cm.
NOVELTY - Solid alkali catalyst is claimed. The preparation of solid alkali catalyst comprises dissolving 5.7-8.5 pts. zinc chloride, 10-16.5 pts. manganese chloride and 18-22 pts. potassium carbonate in deionized water; mixing zinc chloride and manganese chloride solution with potassium carbonate solution to obtain a precipitate; aging the precipitate, filtering, washing, drying, and calcining to obtain manganese carbonate/zinc oxide composite solid alkali catalyst.    USE - The solid alkali catalyst is useful for preparing biodiesel (claimed).    ADVANTAGE - The solid alkali catalyst carries out efficient catalytic transesterification of sub-critical methanol, achieves maximum conversion rate of up to 99% and fast transesterification reaction rate.
NOVELTY - A metal and/or its oxide-doped silica composite is silica complex obtained by in-situ doping of metal and/or its oxides, and has BET specific surface area of 100-800 m2/g. Metal and/or its oxide-doped silica composite comprises 1-20 wt.% metallic nickel and/or its oxide, 0-5 wt.% rare-earth metal and/or its oxide, 0-10 wt.% rare-earth metal and/or its oxide and 0-5 wt.% alkali metal and/or its oxide. The rare-earth metal is zirconium, vanadium, manganese, or group VIB metal.    USE - Metal and/or its oxide-doped silica composite is used as catalyst for preparation of synthesis gas from methane (claimed).    DETAILED DESCRIPTION - A metal and/or its oxide-doped silica composite is silica complex obtained by in-situ doping of metal and/or its oxides, and has BET specific surface area of 100-800 m2/g. Metal and/or its oxide-doped silica composite comprises 1-20 wt.% metallic nickel and/or its oxide, 0-5 wt.% rare-earth metal and/or its oxide, 0-10 wt.% rare-earth metal and/or its oxide and 0-5 wt.% alkali metal and/or its oxide. The rare-earth metal is zirconium, vanadium, manganese, or group VIB metal. The metal and/or its oxide-doped silica composite is obtained by stirring template, alkaline source and silica source at room temperature in a reactor for 5-24 hours, dripping metal source solution, stirring continuously for 0.5-24 hours, obtaining emulsion, hydrothermally reacting at 80-180 degrees C for 12-100 hours, quenching to room temperature, filtering, washing filter cake until neutral, drying, and calcined at 400-800 degrees C. The molar ratio of template, alkaline source, silica source and metal source is 0.06-0.24:0.1-0.3:1:0.01-0.2. The metal source solution is nickel salt solution, or mixture of nickel salt solution and rare-earth metal salt solution.
NOVELTY - This utility new type claims a one ecological toilet with solid-liquid separator, this utility new type is, the original patent (one ecological toilet with a turn type solid-liquid separator, authorization number: ZL201220112091.4), through practical test rear made great after modifying. Include blowing nozzle,, a shaft, a hopper body, a drainage port, filter plate, a bracket, a bearing base, a striker plate, an electric push rod, an air compressor, an electric control system, the rear manure flushing water mixture together entering into skip bucket, the inner bucket separate, a a a a a a, solid-liquid separate substantially completely, an electric push rod would push the bucket to make the pouring action is finished, d would d through a channel into the solid fermentation system, liquid by a channel into the fecal sewage collecting device. The following advantages: suitable for early treatment of all kinds of ecological toilet drainage and automatic degree high, simple and convenient maintenance, the ecological toilet system greatly saves manpower and material resources, efficient and environment-friendly.
NOVELTY - Bio-butanol fermentation wastewater treatment and organic acid co-production includes pumping bio-butanol fermentation wastewater into fixed bed column for hypercrosslinked resin adsorption, washing impurities with deionized or tap water to obtain an azeotrope having boiling point of less than 100 degrees C, eluting with water-soluble organic solvent, completing elution with deionized water or tap water, regenerating adsorption effluent, returning to batch fermentation and subjecting the eluent through atmospheric pressure distillation and vacuum distillation to obtain acetic acid and butyric acid.    USE - Bio-butanol fermentation wastewater treatment and organic acid co-production (claimed).    ADVANTAGE - The method is simple, environment friendly and easy for industrial implementation, has low production cost and provides organic acid having purity of more than 98.5% and total yield of 95.8%.    DETAILED DESCRIPTION - Bio-butanol fermentation wastewater treatment and organic acid co-production comprises pumping bio-butanol fermentation wastewater into fixed bed column for hypercrosslinked resin adsorption, washing impurities with deionized or tap water to obtain an azeotrope having boiling point of less than 100 degrees C, eluting with water-soluble organic solvent, completing elution with deionized water or tap water, regenerating adsorption effluent, returning to batch fermentation, subjecting the eluent through atmospheric pressure distillation and vacuum distillation to obtain acetic acid and butyric acid, regenerating the eluent and recycling.
NOVELTY - The reactor has a main body provided with an external control device. A lower end of the main body is fixed with a cloth water discharging unit, a reaction unit, a liquid surface float sludge crushing unit, a liquid surface float sludge collecting unit, a circulation unit and a water outlet unit. An injection tube is connected with a gas collection chamber. The external control device is provided with a liquid level relay. The reaction unit is connected with the liquid surface float sludge collecting unit and the circulation unit. The water outlet unit is connected with a control valve.    USE - Automatic float sludge crushing and circulation-type autotrophic denitrification granule sludge reactor.    ADVANTAGE - The reactor performs rest gas aeration process and autotrophic denitrification process in a better manner. The reactor removes bubble from a sludge surface. The reactor realizes floating sludge collecting, crushing and sedimentation process in a better manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an automatic float sludge crushing and circulation-type autotrophic denitrification granule sludge reactor.
NOVELTY - The method involves collecting potato product production waste water in a hydrolysis acidification pool. Alkali is added into the pool. An aerobic fermentation process is carried out to the pool for 20-26 hours. Non-dissolved organic matter is mixed into the waste water. Sludge content in liquid material is determined by using a biochemical sedimentation process. Discharging supernatant, 25 kg of polymerization aluminum chloride, 0.25 kg of polyacrylamide and hydrogen sodium oxide are added into to a coagulation accelerator.    USE - Potato products production waste water processing method.    ADVANTAGE - The method enables simplifying waste water processing process, and ensures processing effect and reducing COD value in the liquid material.
NOVELTY - A pyridine-containing compound is prepared by reducing sodium benzoate-containing compound to obtain benzoic acid-containing compound, esterifying with alkylating agent to obtain 3-hydroxypropyl-containing compound, reacting with methyl Grignard reagent to obtain propanol-containing compound, oxidizing to obtain ketone alcohol intermediate which is propanone-containing compound, and coupling with quinoline-containing compound in the presence of catalyst.    USE - Synthesis of pyridine-containing compound (claimed).    ADVANTAGE - Process is simple, low cost, and environment-friendly, and has easy to obtain raw materials and high yield.    DETAILED DESCRIPTION - A pyridine-containing compound of formula (1) is prepared by reducing sodium benzoate-containing compound of formula (2) to obtain benzoic acid-containing compound of formula (3), esterifying with alkylating agent to obtain 3-hydroxypropyl-containing compound of formula (4), reacting with methyl Grignard reagent to obtain propanol-containing compound of formula (5), oxidizing to obtain ketone alcohol intermediate which is propanone-containing compound of formula (6), and coupling with quinoline-containing compound of formula (7) in the presence of catalyst.    X, X'=halo; and R=1-4C alkyl.
NOVELTY - Preparing N-formyl phenothiazine comprises adding formic acid and phosphorus oxychloride into a reaction container, then uniformly grinding and adding phenothiazine, continuously grinding the mixture, then filtering to obtain filter cake, washing the filter cake, drying and standing the washed product. The mole ratio of formic acid, phosphorus oxychloride and phenothiazine is 1-1.2:1-1.2:1.    USE - The method is useful for preparing n-formyl phenothiazine (claimed).    ADVANTAGE - The method is capable of simply and conveniently preparing the n-formyl phenothiazine with high yield of 93% in an eco-friendly manner.
NOVELTY - A N-acetyl-phenothiazine is prepared by adding 1-1.2 moles acetic acid and 1-1.2 moles phosphorus pentachloride into reaction container, uniformly grinding, adding 1 mole phenothiazine, continuously grinding, completely reacting, filtering, washing filter cake, drying, recrystallizing, and standing.    USE - Preparation of N-acetyl-phenothiazine (claimed).    ADVANTAGE - Process is simple, low cost, environment-friendly, and safe and has mild reaction condition, short reaction time, and low toxicity, and product has high yield.
NOVELTY - Preparing N-acyl-phenothiazine comprises: adding to a reaction vessel, A1 mol of aromatic acids and B1 mol phosphorus pentachloride as a catalayst and grinding them uniformly, adding C1 mol phenothiazine, and continuing the grinding to grind phenothiazine until completion of the reaction to obtain a product, where the ratio of A1, B1 and C1 is 1-1.2:1-1.2:1; and allowing the product to stand, washing, filtering, and subjecting the obtained cake to drying and recrystallization.    USE - The method is useful for preparing N-acyl-phenothiazine (claimed).    ADVANTAGE - The method: can be carried out in a simple, safe and convenient manner under mild conditions; requires less time; reduces the equipment requirements; utilizes phosphorus pentachloride catalyst, which is inexpensive and less toxic, hence it is environmentally friendly; and provides the target product with high yield i.e. 92%.
NOVELTY - This utility new type provide an integrated pollution soil crushing pre-mix repairing device, comprise one vehicle body, said vehicle body front end set with one rotary cultivator, a lower vehicle body in turn set with a soil conveying device and material stir conveying device, soil conveying device comprise the upper part of cutting shovel, first conveyor and material lifting device, a end of the stir material conveying device of a first conveyor, a vehicle body is set with one adsorbent feeding hopper, and the adsorbent feeding a stir the material inlet hopper of conveying device, the material conveying device of stir discharge hole is set with one second conveyor, a second conveyor set with one magnetic separate device between a housing of a separate device magnetic stir the material conveying device is provided with one adsorbent is a hopper. The repairing time in a process operation, adding adsorbent that is a in a soil heavy metal and pesticide drug such as with no separate a soil is soil repairing a one of a green and environment-friendly.
NOVELTY - This utility new type provide the one high water pollution soil of a repairing device, comprise one car body, a car body set with a soil conveying device in turn and stir the material conveying device, the hopper of the material stir conveying device set up with one crushing device, conveying device comprise soil cutting shovel, first conveyor and material lifting device, lower device include: housing, stir rotate roller, semicircular, first electric machine and a hopper, a vehicle body is set with one adsorbent feeding hopper, and the feeding opening is located in the material hopper of the upper part, the discharging port of the material stir conveying device is set with one second conveyor, a second conveyor set with one magnetic separate device between a shell of magnetic separate. stir the material conveying device is provided with one adsorbent is a hopper. The repairing time in a process operation, adding adsorbent that is a in a soil heavy metal and pesticide drug such as with no separate a soil is soil repairing a one of a green and environment-friendly.
NOVELTY - This utility new type provide the a one is suitable for repairing pollution soil of a powder, comprise one vehicle body, said vehicle body upper set with soil conveying device in turn and stir the material conveying device, the hopper of said material stir conveying device set up with one crushing device, a soil conveying device comprise cutting shovel, first conveyor and material lifting device, crushing device comprise chassis and first electric machine, a vehicle body is provided with one said adsorbent feeding hopper, and the feeding hopper is located in the material inlet of the upper part, a material conveying device a second stir discharge hole is set with one second lower conveyor, a second conveyor set up with one magnetic separate device between a shell of magnetic separate. stir the material conveying device is provided with one adsorbent is a hopper. The repairing time in a process operation, adding adsorbent that is a in a soil heavy metal and pesticide drug such as with no separate a soil is soil repairing a one of a green and environment-friendly.
NOVELTY - The device has a high temperature cracking furnace (100) connected with a cylindrical body that is formed of high temperature-resistant material. A side wall of an interlayer (103) is made of a guide material. A water outlet joint is connected with a heat preservation hot water tank through a tube. The high temperature cracking furnace is arranged with a hearth (102). A water storage tank is connected with a pneuma valve (303), an oxygen connecting valve (700) and a biomass gas stove (400). Length of a steel pipe (703) is about 100-150 mm.    USE - Household biomass pyrolysis gas producing device.    ADVANTAGE - The device ensures high outcome of gas production, and is easy to operate, inexpensive, energy-saving and environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a household biomass pyrolysis gas device.    High temperature cracking furnace (100)    Hearth (102)    Interlayer (103)    Pneuma valve (303)    Biomass gas stove (400)    Oxygen connecting valve (700)    Steel pipe (703)
NOVELTY - A bio-oil preparing method involves preparing material by mixing fermentation antibiotic dreg with water at ratio of 70-95%, and stirring to uniform slurry material. Hydrothermal liquefaction reaction is performed on the slurry material into the hydrothermal liquefaction reactor, so that the material in the slurry organic matter is converted to bio-oil followed by removing the slurry material residual antibiotics, separating the reaction products of hydrothermal liquefaction to obtain finished product.    USE - Method for preparing bio-oil.    ADVANTAGE - The method enables preparing bio oil in simple and feasible, high efficiency, environment-friendly effect and energy saving effect manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for utilization of fermentation antibiotic dreg to prepare bio oil.
NOVELTY - Preparing gasoline involves using biomass as raw material and then subjecting the biomass for hydrolysis to obtain levulinic acid. The levulinic acid is dehydrated to obtain angelica lactone and then the angelica lactone is polymerized to obtain angelica lactone polymer. The angelica lactone polymer is subjected to hydrodeoxygenation process to obtain the desired product. The mass concentration of hydrochloric acid or sulfuric acid aqueous solution catalyst is 0.1-10%. The biomass is hydrolyze for 5-240 minutes. The levulinic acid is dehydrated at 140-220 degrees C.    USE - Method for preparing gasoline (claimed).    ADVANTAGE - The method enables to prepare gasoline with high yield and good quality under mild conditions.    DETAILED DESCRIPTION - Preparing gasoline involves using biomass as raw material and then subjecting the biomass for hydrolysis to obtain levulinic acid. The levulinic acid is dehydrated to obtain angelica lactone and then the angelica lactone is polymerized to obtain angelica lactone polymer. The angelica lactone polymer is subjected to hydrodeoxygenation process to obtain the desired product. The mass concentration of hydrochloric acid or sulfuric acid aqueous solution catalyst is 0.1-10%. The biomass is hydrolyze for 5-240 minutes. The levulinic acid is dehydrated at 140-220 degrees C and the levulinic acid product is washed with 0.1-5%. The acidic ionic liquid or ZSM-5 zeolite catalyst is separated by distillation at 130-180 degrees C for 60-180 minutes to obtain angelica lactone. The angelica lactone is polymerized to lengthen the carbon chain.
NOVELTY - This utility new type provide the one a pollution soil non-blocking vertical crusher mix repairing device, comprise one vehicle body, a vehicle body in turn set with a soil conveying device and stir the material conveying device, the hopper of said material stir conveying device set with one crushing device, conveying device comprise soil cutting shovel, first conveyor and material lifting device, crushing device include: housing, a main shaft and a first electric machine, a vehicle body is provided with one said adsorbent feeding hopper, and the feeding hopper is located in the material inlet of the upper part, the material stir conveying device of second discharge hole is set with one second lower conveyor, a second conveyor set with one magnetic separate device between a housing of a separate device magnetic stir the material conveying device is provided with one adsorbent is a hopper. The repairing time in a process operation, adding adsorbent that is a in a soil heavy metal and pesticide drug such as with no separate a soil is soil repairing a one of a green and environment-friendly.
NOVELTY - This utility new type provide the one suitable for a repairing device of sand pollution soil, comprise one vehicle body, a vehicle body in turn set with a soil conveying device and material stir conveying device, a hopper of the material stir conveying device set with one crushing device, a soil conveying device comprise cutting shovel, first conveyor and material lifting device, crushing device comprise: a housing, and a first electric machine, a vehicle upper body one is provided with adsorbent feeding hopper, and the feeding hopper is located in the adsorbent material, a second discharging said material stir conveying device of the lower frame is provided with one second conveyor, a second conveyor set up with one magnetic separate device between a shell of magnetic separate. stir the material conveying device is provided with one adsorbent is a hopper. The repairing time in a process operation, adding adsorbent that is a in a soil heavy metal and pesticide drug such as with no separate a soil is soil repairing a one of a green and environment-friendly.
NOVELTY - This utility new type provide the a one is suitable for pollution soil repairing device of hard mixed material, comprise one vehicle body, a vehicle body in turn set with a soil conveying device and stir the material conveying device, the hopper of the material stir conveying device set with one crushing device, conveying device comprise soil cutting shovel, first conveyor and material lifting device, crushing device comprise: comprise machine shell, motor, first feeding hopper, a discharging hopper, a semicircular-shaped screen, a roller and a crushing cutter, the vehicle body is set with one adsorbent feeding hopper, the discharge hole of said material stir conveying device is set with one second lower conveyor, a second conveyor set up with one magnetic separate device between a housing of a separate device magnetic stir the material conveying device is provided with one adsorbent is a hopper. The repairing time in a process operation, adding adsorbent that is a in a soil heavy metal and pesticide drug such as with no separate a soil is soil repairing a one of a green and environment-friendly.
NOVELTY - The furnace has a furnace body (12) whose lower part is connected with a furnace wall (9). A lower part of the furnace wall is formed with an air inlet (10). An upper part of the furnace body is connected with a material adding device (1) that is connected with a storage hopper (2). A cyclone dust remover (5) is connected with the furnace body and formed with a gas outlet (3) that is matched with the furnace body. The cyclone dust remover is formed with a tangent air inlet (4) and connected with a water seal part (8) by a connecting tube (7).    USE - Biomass gasification furnace.    ADVANTAGE - The furnace is convenient to process, and avoids air blockage and ensures long-term stability during gasification operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification furnace.    Material adding device (1)    Storage hopper (2)    Gas outlet (3)    Tangent air inlet (4)    Cyclone dust remover (5)    Connecting tube (7)    Water seal part (8)    Furnace wall (9)    Air inlet (10)    Furnace body (12)
NOVELTY - Usage of biodiesel in preparation of environmentally-friendly metalworking fluid, is claimed.    USE - Usage of biodiesel in preparation of environmentally-friendly metalworking fluid (claimed).    ADVANTAGE - The environmentally-friendly metalworking fluid is efficiently prepared using biodiesel with excellent workability.
NOVELTY - Preparing biological diesel oil comprises taking sodium hydroxide as catalyst and then adding 1.5% of methanol and soybean oil, heating the mixture at 60 degrees C for 3 hours, allowing the mixture to stand for 2 hours in a separation funnel and then adding glycerol, adjusting the pH to 7 by adding hydrochloric acid and then washing with 3x 90 ml of deionized water for three times, decompressing and distilling. The molar ratio of methanol and soybean oil is 6:1.    USE - The method is useful for preparing biological diesel oil (claimed).
NOVELTY - The machine has a reaction tank connected with a baffle plate. A marsh gas exit is clamped with feeding and discharging channels. A bio-gas pneumatic exit is fixed on a top part of the reaction tank. Clapboard is arranged with an outlet extrusion channel. A stir device is connected with a U-shaped tube and an electric pump. A bending part is provided with a three-way valve door. A heating tube is installed on a bottom part of the reaction tank. A liquid body is fixed with a piston device. A non-metal anti-freezing control valve is arranged with an elastic seal part.    USE - Intelligent self-stir marsh gas stirring machine.    ADVANTAGE - The machine has better working efficiency and speed.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an intelligent self-stir marsh gas stirring machine.
NOVELTY - Production of alcohol involves crushing cellulose-containing substance of a crop straw raw materials into 5-15 mm of small section; preparing yeast mash, diluting to 14-18% fermentable sugar, inoculating microzyme, to obtain mature A; mixing the powder of crop straw raw materials and the mixture A, through auger mixer, to obtain mixture B; fermenting the mixture B in a continuous fermentation tank; fermenting the solid mash into continuous wine steaming machine, to obtain light alcohol; and rectifying the light alcohol to obtain the alcohol product.    USE - For production of alcohol (claimed).    ADVANTAGE - The process has low cost; produces high alcohol content; and produces alcohol without liquid lees.    DETAILED DESCRIPTION - Production of alcohol involves crushing cellulose-containing substance of a crop straw raw materials into 5-15 mm of small section; preparing yeast mash, by acidification treatment, diluting to 14-18% fermentable sugar, inoculating microzyme, in culture medium at 28-32 degrees C for 8-12 hours, to obtain mature A; mixing the powder of crop straw raw materials and the mixture A, through auger mixer, to obtain mixture B having 15-30% sugar; fermenting the mixture B in a continuous fermentation tank, at 28-36 degrees C, and at a pH of 5-5.5; fermenting the solid mash into continuous wine steaming machine, to obtain light alcohol; rectifying the light alcohol to obtain the alcohol product. The cellulose-containing substance of crop straw is a high sweet sorghum straw.
NOVELTY - A activated sludge based organic chemicals biodegradability detecting method involves preparing phosphate buffer, and calcium chloride, magnesium sulfate and iron chloride solution, and adding inorganic salt solution to distilled water. The obtained inorganic salt medium is aerated to collect effluent and filtered. The filtrate is added to microbial inoculum and test substance is added to BOD bottle. Reference substance is added to the BOD bottle and filled with the prepared inorganic salt medium to form a liquid seal and incubated. The incubated product is subjected to an HPLC technique.    USE - Method for detecting biodegradability of activated sludge based organic chemicals.    ADVANTAGE - The method enables detecting the biodegradability of activated sludge based organic chemicals in a simple, rapid and accurate manner.    DETAILED DESCRIPTION - A activated sludge based organic chemicals biodegradability detecting method involves preparing 1 g/l phosphate buffer, and calcium chloride, magnesium sulfate and iron chloride solution, and adding inorganic salt solution to 1 part distilled water and mixing so that the concentration of inorganic salt is 1 ppm to obtain inorganic salt medium, where pH is adjusted to 6.5-7.5. The inorganic salt medium is aerated for 10-30 minutes and kept for 24-72 hours to collect secondary effluent and filtered. The filtrate is added to microbial inoculum and 1 g/l test substance is added to a 1.5-3 ml BOD bottle. 1 g/l reference substance is added to the BOD bottle and filled with the prepared inorganic salt medium to form a liquid seal, at 20-40 degrees C and incubated in the dark condition for 14-50 days. The incubated product is subjected to an HPLC technique to establish the detection of biodegradability of activated sludge based organic chemicals.
NOVELTY - The method involves entering waste water into a primary sedimentation tank. A solid-liquid separating process is performed in a secondary sedimentation tank. Separating clean water is discharged into an aeration tank. A material balance law math model of a growth dynamics equation is established. A micro-organism of sewage processing aeration process is removed. The sewage processing aeration process is controlled by a slip controller. A dissolve oxygen concentration of the aeration process is determined.    USE - Active sludge sewage aeration process modeling method.    ADVANTAGE - The method enables improving a decontamination ability of the active sludge sewage processing aeration process and water quality and controlling dissolve oxygen concentration in a real-time so as to avoid the waste of energy.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a slip controller    (2) an active sludge sewage aeration process control method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating an active sludge sewage aeration process modeling method.'(Drawing includes non-English language text)'
NOVELTY - This utility new type relates to a one by using waste biomass absorbing heavy metal polluted water body of floating bed. Purpose is to supply a floating bed should be a repairing heavy metal polluted water body, resource with high utilization rate, low cost, simple and convenient operation, convenient maintenance and construction of beautiful appearance. Technology solution is as follows: a one by using waste biomass absorbing heavy metal polluted water body of floating bed comprise one with multiple seal of hard tube form a rectangular floating bed main body, wherein a middle floating bed main body is provided with one rope and the bed main body through connecting and provide buoyancy of the foam plate, the bottom of said foam plate arranged with a nylon rope hanging network, said upper hanging network with several hanging a heavy metal absorbing bag, a metal absorbing bag in is provided with absorbing material.
NOVELTY - A marsh gas tank with urban residents marsh gas tank, septic tank, urine suction pump, a three-way valve, a garbage crusher, a slag, anti-explosion device and pipeline, wherein a resident a urine discharging tube and the septic tank connected, urine tube and urine intake suction pump is connected with the inlet, the exit through a three-way valve a and the left and right manure feeding tube and left and right pneuma biogas tank connected, domestic garbage by the garbage crusher crushing the garbage into the material through a tube into a two marsh gas tank, marsh gas tank upper part set with marsh gas outlet tube and anti-explosion device, marsh gas tank set with bottom slag, the other end and the discharging pump is connected with the inlet. The advantages is marsh gas tank, septic tank is built on the ground, solves the residential area domestic garbage processing problem of waste and garbage by preprocessing rear entering into marsh gas tank to make the material thinning of inner marsh gas tank fermenting uniformity, fully, is increased. A multi-marsh gas pool, staggering feeding reloading, the residential area for continuous stable gas supply, biogas residue as organic fertilizer.
NOVELTY - This utility new type relates to a one from the marsh gas in the purifying a carbon dioxide and a device system, include a compressor I, a pre I, first level hollow fiber film, second level hollow fiber film and CO2 a device, inlet of the methane raw material pipeline of compressor I a, exit of compressor is connected with the inlet of device I I a, exit device I and a first level hollow fiber film of the inlet a, first level hollow fiber film of non-penetration gas exit is connected with the inlet of second level hollow fiber film a, first level hollow fiber membrane of permeating gas exit and CO2 a device of inlet a, purifying pneuma of exit CO2 a device CO2 for purifying pneuma exit, second level hollow fiber film of non-penetration gas exit is CH4 purifying pneuma exit, the device has a simple technique, a compact structure, a small volume, automatic degree high, operation is convenient, safety and reliable, application range of application.
NOVELTY - This utility new type relates to a propylene and propane separate one of rectifying device, heat pump rectification system include the tower top stream compressor, condensing reboiler heat exchanger, the tower top reflux pump and stream tower stream separate tank, rectifying section heat pump rectification system rectifying section comprise stream compressor, condensing reboiler heat exchanger section and rectifying section stream reflux pump, stripping heat pump rectification system include the stripping stream compressor section, stripping section reflux pump and stripping stream condensing reboiler heat exchanger. Staggered set with regular filler rectifying section and stripping section. Staggered regular filler is windowing guide structured filler according to the height difference and so on alternating arrangement, inner the one disk filler, each adjacent 2-30 filler is one group filling unit, each filler unit group parallel arrangement, each filler unit group the same height difference is 5 %-75 % of filling height, the filler is sawtooth-shaped arrangement. Through multi-heat pump rectification system optimizes the energy coupling between the pneuma of liquid stream inner tower, reduces 30% of energy consumption, reduces the total investment process.
NOVELTY - This utility new type relates to a one box type skid-mounted marsh gas purifying device, comprise box body and mounting a biogas purifying system in said inner box body, a biogas purifying system comprise in turn of a marsh gas compressor, a gas-liquid separator, a marsh gas cooling, a precise filter group, a marsh gas heater, CO2 separate film group and marsh gas tank, the utility model is new type skid-mounted through mounting, small occupied space, convenient to move, a centralized control, which is helpful to reduce the labour cost, and purifying device does not need further protection, and has heat preservation function, safety efficient.
NOVELTY - This utility new type relates to a membrane method one marsh gas purifying device system, include desulphurization device, three hollow fiber membrane and level CH4 storage tank, inlet of desulphurization device and marsh gas source connect, exit and evaporator is connected with the inlet of a first level hollow fiber membrane group connecting the first level hollow fiber film of non-penetration gas exit is connected with the inlet of second level hollow fiber film a, first level hollow fiber membrane of permeating gas exit the third level hollow fiber film of the inlet a, second level hollow fiber film of non-penetration gas exit and a CH4 storage tank, exit of second level permeating hollow fiber film is connected with the inlet of first hollow fiber film a level, third level hollow fiber film of non-penetration gas exit and the first level hollow fiber film of the inlet a, third level hollow fiber membrane of permeating gas exit and CO2 a treatment device through the pipe line connecting with the atmosphere, this utility new type can be fully recovered for CH4, reducing a pollution for environment, and increase the utilization efficiency of the marsh gas.
NOVELTY - This utility new type provide the one a water curtain wall connecting glue film sealing head cover seal type marsh gas fermentation cellar, belonging to the marsh gas fermentation device technology field, aiming at solving the problems of underground concrete marsh gas fermenting device of marsh gas fermentation cellar body seal is bad, potential leakage hidden trouble of. It using a top Barrel type reinforced concrete marsh gas fermenting cellar body of annular water storage groove, a marsh gas fermentation cellar body top part of annular water storage groove is equipped with inner water cover and connected with a glue film sealing head, a marsh gas fermentation cellar body of annular water storage groove lower part circumference side body is water curtain wall. The whole structure is simple and practical, it is suitable for methane fermentation cellar body at 200 to 1000 m3 or more volume of continuous biogas fermentation air supply work.
NOVELTY - This utility new type provide the one side a circulation feeding and water curtain seal marsh gas ferment device of interlayer type belongs to methane fermentation device technology field, aiming at solving the problems of marsh gas fermentation tank seal performance of underground concrete marsh gas fermenting device, potential leakage hidden trouble of. Methane fermentation tank body is the top of the annular water storage groove, comprising a side body connected from lower to upper is provided with a material liquid outlet well and Barrel type water curtain groove of interlayer reinforced concrete marsh gas fermenting tank, marsh gas fermentation tank body top part of annular water storage groove is connected with inner glue film cover, a discharge liquid outlet well bottom side body is provided with a sludge pump, pump inlet of the sludge pump is connected material liquid connected tube connected marsh gas fermentation cylinder body inner cavity, pump exit set with material liquid conveying tube connected groove, the inner groove is set with feeding control valve, the control valve is equipped with the material liquid tube connected with a marsh gas fermentation cylinder body. The whole structure is simple and practical, which is suitable for continuous biogas fermentation air supply work.
NOVELTY - This new type utility claims one a positive and negative pressure protector include inner cylinder, an outer cylinder, a tube, discharge tube, wherein the outer cylinder is provided with inner liquid sealing, inner water line is higher than the bottom edge of the inner cylinder and the outer cylinder is separated from liquid sealing structure, inner cylinder upper part is diameter-expanding part, an expanding part diameter is more than inner cylinder diameter and smaller than the outer diameter, height and large biogas pneuma amount most inner cylinder expanding part of the outer cylinder water level time of equal height, inner cylinder and the discharge tube and the inner cylinder structure the same axis to the a axis; a tube connected with the outer cylinder, and a tube opening lower edge is higher than the protection time negative pressure outer cylinder liquid water sealing water level discharge tube and the inner cylinder connected. This utility new type is a protection reactor tank body internal pressure environment., simplifies the structure, and internal structure to symmetrically along the axis, in the actual production process of positive and negative pressure protector for calculation, measurement and processing of a more convenient and labour-saving and reduces the production difficulty.
NOVELTY - A one using solar energy to heating of biogas production device. Is using solar energy heat collecting system for water heating, hot water entering into circulation heating system for methane tank material liquid a heating marsh gas, marsh gas pool temperature reaches a certain range produce marsh gas, the whole production process is provided with a system to control, marsh gas in daily life, in a process saves a lot of other a renewable resource, reduces the production and living cost, a marsh gas process produce a material in a liquid to replace organic fertilizer, valid protects the ecological system.
NOVELTY - This utility new type claims a new-type biological diesel oil of one reaction device, comprise reaction kettle, methanol tank, oil tank, tank, first driving pump, a depositing tank and filter, further comprise one uniform material circulation device, a circulation material uniformly. include mounting the mix liquid inlet tube of a mixing tank, the bottom of the reaction kettle and a connecting on the said mixing liquid groove water inlet of reflux tube, and second driving pump is set on up tube of return. This utility new type using a circulation material device can quickly and uniformly of the multi-a. raw material mix uniform, and strong practicability and is worth to be popularized.
NOVELTY - This new type utility claims one based on a portable of TL494 electrolytic water hydrogen producing a control device. It comprise a MCU module, a PWM output voltage adjust module, electrical source module, display module, a switch control module, a water output module and sensor signal collect module, an MCU control module and a PWM regulating output voltage module, an electric source module, display module, a switch control module, a water output module and sensor signal collect module. This utility new type is convenient to carry, the cost is low, which is greatly convenient for people to use.
NOVELTY - This utility new type relates to a one for sewage treatment and biogas production system, mainly comprise grid, sewage collecting tank, solid-liquid separate machine, regulating pool, a first-stage UASB, aeration regulating pool, a UASB, level A/O tank, a coagulative precipitation tank, aritificial wetland, a steam-water separator, a desulfurizing tank, a storage cabinet, a pneuma, concentrate the sludge tank, a sludge dehydrating machine, and air blower. This utility new type of beneficial effects include: 1) a farm of sewage would not for the surrounding water body pollution, realize standard discharge, 2) can be in separate manure sewage solid substance and so on, a organic fertilizer, produce a considerable economic benefit, 3) for a rear sewage solid-liquid separate processing process and reduces the sewage processing energy consumption and produce marsh gas by marsh gas power generation supply sewage station to use or organic fertilizer production; 4) a the modernization of excrement sewage comprehensive treatment and resource circulation can be used.
NOVELTY - This utility new type provide a one full automatic biomass gasification gas boiler, it comprise feeding belt machine, spiral feeder, , pneuma furnace, a tar waste water cleaner boiler, feeding belt machine front end of the spiral feeder, a spiral feeder is feeding port of the pneuma furnace, is set on the low part of the pneuma furnace, pneuma furnace with the tar waste water cleaner, the tar waste water cleaner through the pneuma tube with the boiler. Effect of it are as follows: 1, it saves a large amount of is a renewable energy source, wherein the patient is a human social sustainable development provide support, 2, automatic degree high;
NOVELTY - An acrylonitrile refining method involves utilizing waste water into the ammoxidation process by producing propylene or propane during the manufacture of acrylonitrile, as a raw material, followed by mixing the raw material with oxygen containing catalyst in a wet oxidation reactor at 200-320 degrees C and pressure of 5-15 MPa for 5-120 minutes, where the catalyst comprises component A comprising 96-98 pts. wt. zirconium oxide ceramic foam plate, and component B comprising 2-4 pts. wt metal oxide such as copper, manganese, cerium and/or cobalt.    USE - Method for refining acrylonitrile.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing catalyst, which involves impregnating zirconium oxide ceramic foam plate in salt selected from a group consisting of copper, manganese, cerium or cobalt at 20-100 degrees C for 12-24 hours, and drying to obtain catalyst precursor followed by placing the obtained catalyst precursor in air atmosphere at 200-800 degrees C for 1-10 hours to obtain the finished product.
NOVELTY - Microbial selenium-enriched foliar fertilizer composition comprises 5 kg pure selenium powder, 50 kg soybean protein powder, 20 kg edible starch, 10 kg glucose, 15 kg dipotassium hydrogen phosphate, 1000 kg water, 100 kg Bacillus megaterium, 100 kg potassium humate, and 600 m3 sterile air.    USE - The fertilizer composition is useful for promoting crop growth.    ADVANTAGE - The fertilizer composition can be easily prepared, significantly increases selenium content in agricultural products, and improves crop disease resistance ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for manufacturing microbial selenium-enriched foliar fertilizer composition, comprising (a) introducing 5 kg pure selenium powder, 50 kg soybean protein powder, 20 kg edible starch, 10 kg glucose and 15 kg dipotassium phosphate into a bioreactor, adding 1000 kg water, and sterilizing at 120 degrees C for 30 minutes, (b) cooling the obtained sterilized mixture to 35 degrees C, adding 100 kg Bacillus megaterium into the obtained sterilized mixture, introducing 600 m3 sterile air, and reacting, and (c) adding 100 kg potassium humate into the obtained reaction product, uniformly mixing, and packaging the obtained product.
NOVELTY - Producing mica mine tailings comprises introducing mine tailing soil into a mixer and then stirring, compressing the tailings in a compression machine to obtain flakes having a thickness of 5-30 mm, introducing the flakes to a microwave drying sterilizing machine using a conveyor belt and then sterilizing and drying at 60-100 degrees C for 3-120 minutes to reduce water content to less than 15%, and cooling flakes and then packaging.    USE - The method is useful for producing mica mine tailings (claimed) that are useful as fertilizer for promoting growth of plants.    ADVANTAGE - The method is capable of producing the mica mine tailings with high nutritional content in eco-friendly manner.    DETAILED DESCRIPTION - Producing mica mine tailings comprises introducing mine tailing soil into a mixer and then stirring, compressing the tailings in a compression machine to obtain flakes having a thickness of 5-30 mm, introducing the flakes to a microwave drying sterilizing machine using a conveyor belt and then sterilizing and drying at 60-100 degrees C for 3-120 minutes to reduce water content to less than 15%, and cooling the flakes and then packaging. The mine tailing soil comprises 15-35 wt.% of acidified mica tailings, 25-55 wt.% of acidified sludge, 2-15 wt.% of high-viscosity attapulgite clay, 2-15 wt.% of soaked, flower-shaped ceramic slurry, 2-15 wt.% of pulverized peat, 2-15 wt.% of slag, 1-10 wt.% of pulverized plant fiber, 0.5-5 wt.% of vermiculite, 0.5-5 wt.% of perlite and 0.1-5 wt.% of super absorbent resin.
NOVELTY - Nutrition soil production involves preparing clay by putting them into machine and then stirred and transferred into a microwave belt type sterilizing machine to sterilize them at 60-100 degrees C under low temperature. The obtained material is treated with water at 30-120 degrees C to obtain a product. The product is mixed with material and then packaged. Material comprises (in wt.%): acid sludge (15-35), high-viscosity attapulgite clay (25-55), leaching liquid (2-15), attapulgite floral ceramic (2-15), peat (2-15), slag (2-15), crushed plant fiber (1-10) and expanded vermiculite (0.5-5).    USE - Method for producing nutrition soil by using clay (claimed) for growth and development of plant.    ADVANTAGE - The method enables to produce nutrition soil in eco-friendly manner that provides nitrogen, phosphorus, potassium, organic matter and multi-element to soil, and reduces pathogenic bacteria and pest which are harmful to plant.    DETAILED DESCRIPTION - Nutrition soil production involves preparing clay by putting them into machine and then stirred and transferred into a microwave belt type sterilizing machine to sterilize them at 60-100 degrees C under low temperature. The obtained material is treated with water at 30-120 degrees C to obtain a product. The product is mixed with material and then packaged. Material comprises (in wt.%): acid sludge (15-35), high-viscosity attapulgite clay (25-55), leaching liquid (2-15), attapulgite floral ceramic (2-15), peat (2-15), slag (2-15), crushed plant fiber (1-10), expanded vermiculite (0.5-5), expanded perlite (0.5-5), and high water absorbing resin (0.5-5).
NOVELTY - Microbial fertilizer comprises 50 kg sodium carboxymethyl starch, 80 kg rice Flavobacterium fermentation broth, 100 kg Aspergillus glaucus fermentation broth, 100 kg Bacillus subtilis fermentation broth, 3 kg chitin, 2 kg nucleotide, 20 kg potassium nitrate, 20 kg dipotassium hydrogen phosphate, 50 kg fulvic acid and 1500 kg water.    USE - The microbial fertilizer is useful for reducing pesticide and heavy metal residues (claimed).    ADVANTAGE - The fertilizer is simple to prepare and improve the quality of agricultural products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing microbial fertilizer, comprising: (i) adding chitin extract, nucleotide, potassium nitrate, potassium hydrogen phosphate, fulvic acid and water into a stainless steel reactor, mixing uniformly and heating to 80 degrees C for 40 minutes; and (ii) cooling the above mixture to 30 degrees C, then adding sodium carboxymethyl starch, rice Flavobacterium fermentation broth, Aspergillus glaucus fermentation broth and Bacillus subtilis fermentation broth, and mixing uniformly by stirring.
NOVELTY - Preparing fertilizer comprises washing urea-formaldehyde with water, introducing washed urea-formaldehyde to a reaction vessel and then heating, crushing the urea-formaldehyde, adding monoammonium phosphate, potassium chloride and fillers to the urea-formaldehyde powder and then mixing at 200-350 degrees C and crushing to obtain mixed powder, introducing mixed powder into a fertilizer dosing device, screening quality of the powder, drying to obtain a final product, and packaging the final product.    USE - The method is useful for preparing fertilizer (claimed) for crop.    ADVANTAGE - The method is capable of preparing the slow-release fertilizer with reduced energy consumption and moisture content and increased strength and nutrient content in an eco-friendly manner thus improving productivity of the crop.    DETAILED DESCRIPTION - Preparing fertilizer comprises washing urea-formaldehyde with water, introducing washed urea-formaldehyde to a reaction vessel and then heating at 90 degrees C, crushing the urea-formaldehyde using a granulator, adding monoammonium phosphate, potassium chloride and fillers to the urea-formaldehyde powder in a buffer tank and then mixing at 200-350 degrees C and crushing to obtain mixed powder, introducing mixed powder into a fertilizer dosing device, screening quality of the powder and then drying to obtain a final product, and packaging the final product. The weight ratio of urea and formaldehyde is 3:5. An INDEPENDENT CLAIM is included for device for producing the fertilizer comprising a reaction vessel, a pump connected to the reaction vessel, an urea storage tank connected to the reaction vessel, a buffer tank connected to the reaction vessel, a granulator connected to the buffer tank, a dryer, a cooler, a screening machine, and a packaging machine, where the storage tank includes a bucket elevator, the pump is equipped with an electromagnetic flow meter and the granulator is provided with a nozzle.
NOVELTY - The device has a machine body (1) fixed with a synthetic pneuma inlet (3). The machine body is connected with a diesel oil exit (4) and an upper part of a waste pneuma exit (5). A middle part of the machine body is fixed with a coupler (7). A rotating shaft (8) is fixed with a horizontal electric machine (6). A packed bed (2) is arranged on the machine body that is fixed with the rotating shaft, where a shape of the machine body is cylindrical and square.    USE - Bio-mass synthetic pneuma rotate synthetic diesel oil device.    ADVANTAGE - The device occupies less area, and has simple and convenient operation and high strength.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a bio-mass synthetic pneuma rotate synthetic diesel oil device.    Machine body (1)    Packed bed (2)    Synthetic pneuma inlet (3)    Diesel oil exit (4)    Waste pneuma exit (5)    Horizontal electric machine (6)    Coupler (7)    Rotating shaft (8)
NOVELTY - Composite additive comprises 2-32 wt.% of solvent A, 3-26 wt.% of solvent B, 2-24 wt.% of steam pressure regulator, 20-85 wt.% of antiknock agent, 1-14 wt.% of antioxidant, 1-12 wt.% of metal corrosion inhibitor, and 1-14 wt.% of rubber swelling inhibitors.    USE - The composite additive is useful in methanol gasoline (claimed) for a cryogenic engine.    ADVANTAGE - The composite additive has increased resistance to air, corrosion and temperature, and does not contain t-butyl ether, lead, aluminum, manganese and zinc, is environmentally friendly, and ensures easy starting of cryogenic engine at low temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for methanol gasoline comprising the composite additive.
NOVELTY - Preparing biofuel granular product involves crushing root, stem, branch, and leaf, peeling skin or shell of plant, and mixing to form mixture, steam-exploded treating at 200-300 degrees C and at pressure of 1-2 MPa for 5-8 minutes, forming raw material, solid-liquid separating, recrushing, sieving through 30-80 meshes, and drying to form 15-25 wt.% powder, mixing the powder with lubricant oil, where the lubricant comprises biological waste or grass dregs, pressure molding, granulating, and cooling.    USE - For preparing biofuel granular product (claimed).    ADVANTAGE - The method is more efficient, and environment-friendly; increases the combustion efficiency; and reduces the production cost.
NOVELTY - Windrow-based fermentation method for preparation of bioorganic fertilizer, by mixing food waste and sheep manure, stirring materials, stacking mixed material into windrows, inoculating fermentation agent as microbial inoculum on windrows, performing aerobic fermentation, turning mixed material, measuring inner temperature of the windrows, turning the windrows once when temperature of the windrows is increased up to 60 degrees C, detecting characteristic properties of fermented product, obtaining qualified and tested bioorganic fertilizer and packaging fertilizer.    USE - Windrow-based fermentation method for preparation of bioorganic fertilizer (claimed).    ADVANTAGE - The method enables effective utilization of wastes, and hence environmental pollution resulting due to waste disposal is reduced.    DETAILED DESCRIPTION - Windrow-based fermentation method for preparation of bioorganic fertilizer, involves (a) mixing food waste having 86-92% water content and sheep manure having 35-45% water content in weight ratio of 2:3, and stirring materials uniformly to obtain mixed material, (b) stacking the mixed material into windrows, (c) inoculating fermentation agent as microbial inoculum on the windrows in weight ratio of 1:1000, performing aerobic fermentation and turning mixed material during the fermentation process by machine, (d) measuring inner temperature of the windrows, turning the windrows once when temperature of the windrows is increased up to 60 degrees C and continuously turning the windrows once every 3-4 days until temperature of the windrows reaches 60 degrees C or less, and (e) detecting characteristic properties of obtained fermented product, obtaining qualified and tested bioorganic fertilizer having 30% water content, 5% or more nitrogen, phosphorus pentoxide and potassium oxide content and 45% or more organic matter, packaging the bioorganic fertilizer and subjecting unqualified fermented product back to the fermentation process.
NOVELTY - The recycling method comprises establishing farms and plantations for growing feed materials, and then stocking pigs in the farms, collecting farm manure for marsh gas fermenting process, collecting methane using the marsh gas for detoxification process, using methane as energy source, solid-liquid separation of marsh gas fermenting residue, using liquid substance as a liquid fertilizer for planting and increasing soil nutrient, using solid substance as raw material for producing organic fertilizer, which is useful for producing raw material, and using raw material as a feed for feeding pigs.    USE - The recycling method is useful in a pig breeding industry (claimed).    ADVANTAGE - The recycling method is economical.    DETAILED DESCRIPTION - The recycling method comprises establishing farms and plantations for growing feed materials, and then stocking pigs in the farms, collecting farm manure for marsh gas fermenting process in a marsh gas fermenting tank, collecting methane using the marsh gas for detoxification process, using methane as energy source, solid-liquid separation of marsh gas fermenting residue as liquid and solid substance, using liquid substance as a liquid fertilizer for planting and increasing soil nutrient, using solid substance as raw material for producing organic fertilizer, which is useful for producing raw material, and using raw material as a feed for feeding pigs. The marsh gas fermenting tank comprises a marsh gas supplying device and a marsh gas heating device. The marsh gas is used in the separation of elemental sulfur.
NOVELTY - A biomass-based pulp enzymatic bleaching method involves feeding unbleached pulp to the reaction kettle, adding water to adjust the concentration, even after mixing treated biomass-based enzyme solution. The pulp after enzyme treatment is placed in biomass-based feed bleaching tower, by using solution containing an oxidizing chemical, after a period of reaction bleached pulp, where the biomass-based enzymes include acetyl esterases, acetyl xylan esterase, alkaline endoxylanase, alpha -L-arabinofuranosidase, alpha -galactosidase and polylactase.    USE - Method for enzymatic bleaching or preprocessing biomass-based pulp.    ADVANTAGE - The method enables reducing bleach and other drug, improving physical properties of pulp bleaching and reducing the pollution load of wastewater.
NOVELTY - Preparation of natural vitamin E soft capsule includes adding glycerol and purified water in digesting tank, stirring, heating, adding gelatin, heating, stirring, digesting, vacuumizing, defoaming and boiling; adding natural vitamin E oil and olive oil in stainless steel barrel, stirring and discharging; preheating materials, cooling with water, molding, detecting, filling in capsules and drying; and putting qualified capsules in special container, sterilizing, spraying alcohol, cleaning, washing surface of soft capsule, drying, packing in bottles and warehousing.    USE - Method for preparing natural vitamin E soft capsule (claimed).    ADVANTAGE - The capsule has uniform size and gloss. The method has high rate of finished products, thus reducing waste.    DETAILED DESCRIPTION - Preparation of natural vitamin E soft capsule comprises:    (A) weighing 2400 g natural vitamin E oil, 600 g olive oil, 1950 g gelatin, 877.5 g glycerol and 1950 g purified water;    (B) adding glycerol and purified water in digesting tank, stirring, heating at 60 degrees C, adding gelatin, heating at 70 degrees C for 2-3 hours, stirring, digesting, vacuumizing, defoaming and boiling to obtain blackish yellow liquid;    (C) adding natural vitamin E oil and olive oil in stainless steel barrel, stirring for 20 minutes and discharging;    (D) preheating materials at 50-60 degrees C, cooling with water at 16-23 degrees C, molding, detecting, filling in capsules and drying at 25-30 degrees C; and    (E) putting qualified capsules in special container, sterilizing, spraying 95% alcohol, cleaning for 5-10 minutes, washing surface of soft capsule, drying at 25-30 degrees C, packing in bottles and warehousing.
NOVELTY - Nanomicrobial fertilizer comprises 0.2-0.25 wt.% Bacillus laterosporus spore powder, 0.2-0.25 wt.% B.megaterium spore powder, 30-35 wt.% organic fertilizer, 40-45 wt.% organic matrix, 2-2.5 wt.% nanomaterials, and 20-25 wt.% carrier.    USE - The nanomicrobial fertilizer is useful for repairing soil (claimed).    ADVANTAGE - The nanomicrobial fertilizer improves soil structure, and exhibits significant restorative effect preferably against polluted soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned nanomicrobial fertilizer, which involves mixing the above-mentioned raw materials in the above-mentioned weight proportions uniformly.
NOVELTY - Organic-inorganic compound fertilizer comprises 100-1000 pts. wt. biological formulation, 0.3-100 pts. wt. humic acid, 90-100 pts. wt. ammonium oxalate, 1-10 pts. wt. magnesium sulfate, 1-10 pts. wt. rare earth complex, 5-20 pts. wt. zeolite powder, 15-38 pts. wt. calcium sulfate and 1-20 pts. wt. sodium silicate, where the biological preparation comprises nitrogen-fixing bacteria, phosphate solubilizing bacteria, potassium solubilizing bacteria, photosynthetic bacteria, Actinomycetes and microzyme.    USE - As organic-inorganic compound fertilizer.    ADVANTAGE - The fertilizer has long-lasting effect and increased utilization rate, reduces the dosage of agrochemical, is cost-effective and convenient to use, can be prepared simply, and exhibits fertilizing effect within 10-20 days.    DETAILED DESCRIPTION - Organic-inorganic compound fertilizer comprises 100-1000 pts. wt. biological formulation, 0.3-100 pts. wt. humic acid, 90-100 pts. wt. ammonium oxalate, 1-10 pts. wt. magnesium sulfate, 1-10 pts. wt. rare earth complex, 5-20 pts. wt. zeolite powder, 15-38 pts. wt. calcium sulfate and 1-20 pts. wt. sodium silicate, where the biological preparation comprises nitrogen-fixing bacteria, phosphate solubilizing bacteria, potassium solubilizing bacteria, photosynthetic bacteria, Actinomycetes and microzyme, the viable count of the organism is more than 2 billion/g, and the rare-earth complex is lanthanum oxide, cobalt oxide or neodymium oxide. An INDEPENDENT CLAIM is included for method of preparing the fertilizer, which involves passing the humic acid, ammonium oxalate, magnesium sulfate, rare earth complex, zeolite powder, calcium sulfate and sodium silicate into 10 meshes sieve, adding biological preparation and mixing uniformly to obtain the product.
NOVELTY - Purification of biogas comprises introducing marsh gas into particulate filter, separating condensate, and drying; introducing into desulfurization tower, compressing, and cooling; and purifying gas with liquefied carbon dioxide, cooling, heat exchanging, discharging, and collecting purified methane.    USE - Method for purifying biogas (claimed).    ADVANTAGE - The method has high purifying rate, removes hydrogen sulfide, water, carbon dioxide, and mix gas, and produces more than 99% methane concentration.
NOVELTY - Preparing biomass pellet fuel additive comprises (i) drying calcium oxide, calcium carbonate, attapulgite clay and iron oxide, (ii) uniformly mixing attapulgite clay, calcium oxide, iron oxide and calcium carbonate, to obtain biomass pellet fuel additive; and (iii) adding biomass raw material into the obtained additive, uniformly mixing in a mixer, mechanically compressing, granulating and cooling to obtain biomass pellet fuel having high combustion property.    USE - The additive is useful for producing biomass pellet fuel (claimed).    ADVANTAGE - The additive does not easily form slag in the combustion process, has high combustion efficiency, and greatly contributes to combustion properties of biomass fuels, thus enhancing the operational efficiency of the biomass boiler.
NOVELTY - A kind of one containing cyclo alkyl ethylene multi-step sewage treatment system, wherein the containing ring B alkyl multi-step sewage treatment system can utilize ring ethanol alkyl and water and physical characteristics for containing sewage and ethylene alkyl ring for processing, and reducing the pollute to environment.
NOVELTY - This utility new type claims a one organic waste aerobic compost forced ventilation and deodorizing system, the aerobic fermentation tower is a sealed tower body, a multi-pipe in the aerobic fermenting tower outer side of different height are arranged in parallel, one end radial access tower body, and the other end is externally connected with air blower, exhaust pipe and vent-pipe are arranged in parallel, one end thereof in the fermentation tower body part radial access tower, and the other end is externally connected with an exhaust fan, the top part of tower body set with aerobic fermentation at the bottom of a closed body feeding port of the feeding time and set with the top tail pneuma exit, the aerobic ferment tower set with discharging time is not a closed discharge hole and set with a bottom tail pneuma exit, odor sensor, oxygen-temperature sensor mounting inner in the aerobic fermenting tower, a PLC control system and the ozone sensor, oxygen-temperature sensor and a fan to realize automatic control. This utility new type a aerobic composting body solves the ventilation of excessive or inadequate ventilation, inner pile body oxygen supply is not uniform, body odour pneuma, difficult to remove odour and so on technology.
NOVELTY - This utility new type relates to a sludge fuel made of one device, in order to solve the domestic sludge and industrial sludge and so on produce of a carbide treatment of sewage, so as to a recycling of a fuel material, comprise drive device, one end of tube with a feeding port, wherein the tube set with at least three part, is connected with the feeding port of one section is dehydration granulating section, middle section set with drying tube section with the tube discharging port a is section, the discharge tube one end set with flame heating device, the material inlet tube one end set with discharge device. Material crushing degree high, especially for paper making produce a multi fiber sludge valid, the product carbide is high, heat energy utilization rate is high, a effluent is main, the environmental protection and safety treatment to water, the whole device is simple, device manufacturing cost and operation cost is low.
NOVELTY - This utility new type provide a waste heat circulation a one silicon dioxide of biomass pyrolysis device, it comprise spiral feeding device, stirrer preprocessing, pyrolysis device, a combustion device, a cyclone separator and calcining device. The biomass raw material through spiral feeding device is sent to preprocessing stirrer. Rear stir of biomass raw material is connected with the cyclone separator produce one part of rear heat waste gas mix entering into pyrolysis device. Pyrolysis device out of a combustion gas entering into the combustion device. Combustion device combusting a produce of a smoke pneuma enter into cyclone separator. The other part tail pneuma emptying cyclone separator of produce. A separate ash with the cyclone separator of pyrolysis device lower ash discharging port, entering into a calcining device in calcining device produce heat smoke pneuma of the pyrolysis device. This utility new type cyclone separator produce by using waste heat of exhaust gas for biomass raw material heating drying preprocessing process, a utilization efficiency of a system increase, at the same time, obtain a amorphous silicon.
NOVELTY - This utility new type claims a banana and one crushing fuel molding machine. It is set with a inclined feeding mechanism (1), a feeding mechanism (1) set with back inclined set of multi-level dehydration mechanism, a multi-stage dehydrating mechanism lower part set with water collecting tank (22), and a (7) rear part set with beater (8) and cutting platform (21) and hob cutting mechanism (11), cutting mechanism (11) of lower part and set with crushing mechanism (14), and crushing mechanism (14) set with under hopper (15), hopper (15) lower part set with screw extrusion molding mechanism (16), a screw rod extrusion moulding mechanism (16) of discharge hole end set with one cutting device (18). This utility new type can be a banana process for dehydrating, crushing, extruding and molding organic combine together, it can complete a banana for a completely disposable processing so that processing a banana is process of finish the automatic fuel, at the same time, the banana volume, and it is convenient to be transported.
NOVELTY - This utility new type claims a circulation upper one a water processing water hyacinth and a marsh gas collecting device, comprise a cylindrical processing tank, a processing tank is set with a feeding port and a discharge tube, a tank by an upper cover, a tank body and lower body, the lower top end of the tank body is set with an upper cover, a tank body of bottom end set with enclosure, with floating bracket set in part of the tank body, the tank body and the floating bracket and a lower enclosure between a circulation clapboard set, compared with the existing technology, this utility new type not only has simple structure, smart design, and of a decomposition of a plant to generate marsh gas a supply domestic heat energy, generating and lighting, and the can be used for fish culture, economic benefit prospect conversion, purification and improve the water quality and so on.
NOVELTY - This utility new type inner claims a one organic matter solid bulk fermentation and sterilizing and heat exchange integrated device, the fermentation room and sterilizing room mounting there are multiple layers, each layer multi-group of temperature, pressure, two edge CO2 and NH3 sensor, inner room for mounting air inlet and discharging control device, sterilizing room bottom mounting with a discharging device, the discharging device of the discharging spiral roller B of uniform distribute with a feeding spiral roller B of the same number, distribute the feeding spiral roller B of the discharging spiral roller B with a rotating end, a feeding spiral roller B reverse rotation shell and centre of spiral conveying tube of heat exchange device with a U-type steam channel; the steam interlayer channel quantity electromagnetic valve A through a high temperature steam source, quantity through a pneuma source electromagnetic valve B, a outer wall of sterilizing room of different end are filled with heat exchange medium. This utility new type a short time, a high efficiency, a low cost, stable and reliable quality, which saves a large amount of aritificial, small floor area and transportation device, eliminate the environment pollution.
NOVELTY - This new utility model relates to a kind of marsh gas engineering and one detection and control system, a marsh gas engineering device comprises one of ferment reacting furnace, the detecting and controlling system comprises an ARM processor, parameter detection mechanism and executing mechanism, detection mechanism of setting parameter in fermentation reaction furnace of the heat resistor temperature sensing device, industrial grade PH value sensing device, gel redox electrode and electromagnetic flow sensor device one, executing mechanism comprises two multi-centrifugal pump and solenoid valve, each sensor device of said parameter detection mechanism is separately connected with power and the ARM processor, the signal output end of the ARM processor connected to executing mechanism of centrifugal pump and electric motor car valve. Parameter change by controlling the marsh gas ferment reaction process of important fermentation reaction using normal processing, so as to increase marsh gas reaction speed, with high marsh gas yield and quality.
NOVELTY - Producing straw mushroom, comprises (a) sterilizing straw mushroom with formaldehyde to obtain straw mushroom material, cultivating the straw mushroom material to obtain straw mushroom culture material, (b) evenly spreading bacteria on mushroom cultivation material surface and then seeding and covering by a plastic film, maintaining the temperature of the cultivation material to 33-36 degrees C and then drying, (c) spraying the water on the mushroom culture material, (d) seeding the culture material to centrifuge, and (e) collecting the mushroom in a refrigerator and then packing.    USE - The method is useful for producing straw mushroom (claimed).    ADVANTAGE - The method is capable of rapidly producing the straw mushroom with improved yield and less energy consumption.    DETAILED DESCRIPTION - Producing straw mushroom, comprises (a) sterilizing 15 g of straw mushroom with 40% of formaldehyde to obtain straw mushroom material, and cultivating the straw mushroom material having a thickness of 10-15 cm and amount of 7.5-10 kg/m2 to obtain straw mushroom culture material including 40-60 pts. wt. bagasse, 20-30 pts. wt. corn residue, 10-20 pts. wt. mulberry stem, 5-8 pts. wt. wheat bran, and 3-5 pts. wt. fishmeal, (b) evenly spreading bacteria on a mushroom cultivation material surface and then seeding for 3 days and covering by a plastic film, maintaining the temperature of the cultivation material to 33-36 degrees C and then drying until the moisture content is 90-95%, (c) spraying the water on the mushroom culture material, and keeping the temperature of the sprayed mushroom culture material to 33-35 degrees C, (d) seeding the culture material for 5-6 days and then centrifuging to obtain supernatant liquid, adjusting a pH value of the supernatant liquid to 8-9, and (e) collecting the mushroom in a fresh-keeping refrigerator at temperature of 10-15 degrees C and then packing.
NOVELTY - This utility new type provide a one garbage treatment device. This utility new type of garbage processing device, comprise the compost cabin body, the compost cabin body set with a filter plate, the filter plate set with an air supply pipeline, air supply pipeline connecting the heat exchanger, the filter plate lower part set with a water collecting groove, the collecting groove through pipeline connecting the waste water tank, the compost cabin body a discharge tube, a discharge tube of a washing tower, washing tower through the pipeline a. carbon absorbing bed, the compost cabin body set with one group checking sensor, stack a part of the fertilizer cabin body set with a water supply. This utility new type of waste pneuma washing tower through a rear active carbon absorbing bed by absorbing poisonous and harmful other, which avoids the compost fermentation process in the environment for a secondary pollution of garbage composting processing of expansion and application range, it changes waste into valuable.
NOVELTY - The assembling device has an artificial marsh tank (2) which is provided with a water inlet tube. The upper side (1-a) of artificial wetland tank (1) is set with a water collecting groove (7) set with a convex port. The bottom wall of the artificial wetland tank is set with a convex tank. The upper wall of the artificial wetland tank is set with a convex opening groove which is connected to convex tank and convex port. The inner wall of artificial marsh tank is mounted with heat preservation layer (16) and steel plate to form inner cavity in which heat preservation cotton is added.    USE - Artificial wetland assembling device for sewage purification.    ADVANTAGE - The inner wall of artificial marsh tank is mounted with heat preservation layer and steel plate to form inner cavity in which heat preservation cotton is added, by which combined processing of microorganism and organic waste are performed. The sewage processing efficiency is ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the artificial wetland assembling device.    Artificial wetland tank (1)    Upper side of artificial wetland tank (1-a)    Artificial marsh tank (2)    Water collecting groove (7)    Heat preservation layer (16)
NOVELTY - Sewage treatment device comprises an artificial marsh tank, a water inlet pipe, an aeration device, a water outlet unit and an immobilized microorganism plate that is equipped at upper side of an artificial wetland. A gravel layer is set with water inlet pipe. A water tube is provided with a water inlet pipe. A filter head is mounted at the water outlet unit.    USE - Sewage treatment device.    ADVANTAGE - The sewage treatment device ensures simple structure.
NOVELTY - A one new-type straw coal molding machine, include a motor, a motor belt wheel, a belt I, a speed reducer input belt wheel, a speed reducer, a rear rack, a speed reducer output belt wheel, a speed reducer output belt wheel, a belt II, extruding screw rod belt wheel, extruding screw rod shaft, a rear bearing, a feeding port, an extruding expansion cylinder, a bracket cross beam, a bracket, the exit, front machine frame, pedestal, spiral blade, an extruding screw rod front bearing. Motor, front and back machine frame and a speed reducer are mounting on a pedestal, power motor by a belt I is transmitted to the speed reducer by belt II and then is transmitted to the extrusion screw. Extruding screw rod on front and back bearing mounting the front rear machine frame a, extruding a coating on the periphery of the extruding screw rod through a mounting bracket on the beam of bracket, exit die head through a screw thread is screwed on the front end of pressing expansion cylinder, the feeding port set on the rear end of pressing expansion cylinder, a rear crushing straw to aritificial mode from the feeding port in is sent to the machine.
NOVELTY - Bidirectional machine comprises box body (1) and turning main shaft (2), where turning main shaft is located in box body. Middle part of turning main shaft is set with material shifting blade (4) and spiral stirring blade (3). Material shifting blade and upper part of box body is connected with with material conveying blades (5) that is set with transmission conveying device (7), material conveying blade of front box body and material input window (6).    USE - Bidirectional machine used for turning organic fertilizer (claimed).    ADVANTAGE - The bidirectional machine ensures effective use of land resources in cost-effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of bidirectional machine.    Box body (1)    Turning main shaft (2)    Spiral stirring blade (3)    Material shifting blade (4)    Material conveying blades (5)    Material input window (6)    Transmission conveying device (7)
NOVELTY - Preparing water-soluble fertilizer, comprises mixing urea, potassium dihydrogen phosphate, potassium nitrate, biochemical fulvic acid and washing liquid with biogas slurry.    USE - The method is useful for preparing water-soluble fertilizer (claimed).    ADVANTAGE - The method produces product: which meets the agriculture industry standards NY1106-2010 requirements, having less toxicity, and has stable quality; and utilizes wastes; does not produce toxic materials during seed germination, and improves the seed germination index when diluted to 400-times; has simple operation procedure, and easily controllable conditions.
NOVELTY - Water-soluble fertilizer comprises biogas slurry, urea, potassium dihydrogen phosphate, potassium nitrate, biochemical fulvic acid, and washing liquid.    USE - Water-soluble fertilizer.    ADVANTAGE - The water-soluble fertilizer has less toxicity, and improves seed germination index .    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing water-soluble fertilizer, comprising adding urea, potassium dihydrogen phosphate, potassium nitrate, biochemical fulvic acid and washing liquid to the biogas slurry and then uniformly stirring to completely dissolve.
NOVELTY - Selenium-enriched fertilizer composition comprises 5-10 wt.% selenium fermentation broth extract, 10-20 wt.% biological microbial inoculum, 40-55 wt.% natural organic compound, 15-25 wt.% urea, 2-4 wt.% urease inhibitor and 5-15 wt.% nitrogen, phosphorus and potassium complex fertilizer. The broth extract is prepared by crushing and milling selenium-enriched mineral, soaking the formed powder in alkali solution for 1 week, removing the slag, adjusting the pH to 5-6 using diluted acid and excess alkali, adding effective microorganism (EM) enzyme preparation and fermenting for 6-12 days.    USE - Used as selenium-enriched fertilizer composition.    ADVANTAGE - The fertilizer composition: improves the soil micro-environment; decomposes pollutants; and utilizes the raw materials which are mostly plant sources, thus the composition is environmentally friendly and does not cause any secondary pollution; comprises beneficial microflora having nitrogen-fixing and phosphate-solubilizing functions; provides amino acids, vitamins and various active enzymes.
NOVELTY - Fertilizer comprises 60-80 pts. wt. vegetable stump pulverized product, 10-20 pts. wt. bamboo charcoal ash, 3-4 pts. wt. shell powder, 8-15 pts. wt. vinegar, 5-15 pts. wt. humic acid, 2-10 pts. wt. microelement, 10-15 pts. wt. seaweed powder, 10-15 pts. wt. Staphylococcus aureus, 8-12 pts. wt. lignin, 10-15 pts. wt. silicon, 16-25 pts. wt. calcium bentonite, and trace element including agricultural rare earth, borax, copper sulfate, manganese sulfate and zinc sulfate heptahydrate according to a weight ratio of 2:1:1:1:1.    USE - Fertilizer.    ADVANTAGE - The fertilizer has high chlorophyll content, and maintains soil fertility and microorganism environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing fertilizer comprising cutting vegetable stump into blocks having a length of 0.5-1.2 cm, then adding bamboo charcoal ash, shell powder, humic acid, trace element, lignin, diatomite and calcium bentonite, uniformly stirring the mixture, adjusting carbon/nitrogen ratio, the water content and the pH range of the mixture to 25, 60% ad 6.2, respectively, then adding vegetable stump pulverized product wotj viable count of more than 2x 109 colony-forming unit/g, then adding other remaining components and piling, and reducing the temperature to 30 degrees C.
NOVELTY - Producing fertilizer containing humic acid comprises adding raw material in a reverse reaction kettle, holding the raw material at temperature of 40-50 degrees C, fully stirring the material for 2 hours, washing the raw material using an alkali, water and inorganic nutrient. The inorganic nutrient comprises 15-30 wt.% of alkali, 15-30 wt.% of water, 24-43 5 wt.% of urea, 0-10 wt.% of monoammonium phosphate and 6-20 wt.% of potassium sulfate.    USE - The method is useful for producing fertilizer (claimed) for crop.    ADVANTAGE - The method is capable of simply and rapidly producing the fertilizer with high utilization ratio and balanced nutrients, and without damage to crops.
NOVELTY - Synthesizing dichloropropanol involves reacting pyridine, catalytic biodiesel byproduct glycerol and hydrogen chloride in the presence of Bronsted acid as catalyst at 70-130 degrees C for 5-20 hours to obtain dichloropropanol. The obtained material is discharged with sodium hydroxide.    USE - Method for synthesizing dichloropropanol (claimed).    ADVANTAGE - The method enables to synthesize dichloropropanol in cost-effective and simple manner, and with less byproducts.
NOVELTY - Synthesis of dichloropropanol comprises using quat. ammonium type Bronsted acid ionic liquid as catalyst, catalytically reacting biodiesel oil by-product i.e. glycerol and hydrogen chloride gas under heating condition, to obtain dichloropropanol, and discharging sodium hydroxide solution after ensuring safe discharge.    USE - Synthesis of dichloropropanol (claimed).    ADVANTAGE - The method has low cost, high conversion rate, dichloropropanol selectivity, 100% conversion rate of raw material glycerol, and dichloropropanol total yield of 92.16%.
NOVELTY - Mango special fertilizer comprises 35-50 pts. wt. animal excrement, 25-40 pts. wt. crop straw, 15-30 pts. wt. vegetable leaves, 2-10 pts. wt. lime, 12-20 pts. wt. plant ash, 18-30 pts. wt. diammonium phosphate, 15-30 pts. wt. urea, 8-15 pts. wt. zinc phosphate, 10-20 pts. wt. potassium chloride, 3-10 pts. wt. vermiculite, 1-8 pts. wt. biological enzyme, and 5-12 pts. wt. organic fertilizer leaven.    USE - Used as mango special fertilizer.    ADVANTAGE - The fertilizer can satisfy the nutritional requirement of mango, promotes the growth of mango, reduces soil compaction and hardening phenomenon, and reduces the cost.
NOVELTY - Modified urea preparation involves soaking pea, mung bean and corn in ratio 1-3:1-3:1-3 in water at 30-60 degrees C for 5-20 hours. The obtained material is filtered, and then adding buffering liquid to maintain pH of the obtained material to 5-7. The obtained material is fermented for 1-5 days. The obtained material is passed through cation exchange resin and eluent is collected. The obtained material is dried to obtain the finished product.    USE - Method for preparing modified urea (claimed).    ADVANTAGE - The method enables to prepare modified urea, ensures improved crop growth without producing side effecct, improve absorption of urea.
NOVELTY - Preparing hydroxylamine derivatives of anthranilic acid comprises adding o-nitroaniline as raw material with alcohol solvent including methanol, ethanol and isopropyl alcohol, normal solvent including tetrahydrofuran and acetone, nitrogen containing solvent including N,N-dimethyl formamide, dimethyl sulfoxide and pyridine as auxiliary agent and noble metal catalyst including platinum carbon, palladium-carbon, rhodium carbon and ruthenium carbon to obtain mixture, heating the mixture at a pressure of 0.05-0. 1 MPa and then re-crystallizing.    USE - The method is useful for preparing hydroxylamine derivatives of anthranilic acid (claimed).    ADVANTAGE - The method is capable of preparing the hydroxylamine derivatives of anthranilic acid in an eco-friendly manner with high yield and good quality.
NOVELTY - Preparation of esomeprazole sodium (I) involves carrying out Grignard reaction of chiral compound (VI) and Grignard reagent (III), and carrying out salt-forming reaction of obtained esomeprazole (VII).    USE - Preparation of esomeprazole sodium (claimed).    ADVANTAGE - The method enables economical preparation of esomeprazole sodium with purity of 90% or more and high yield, by simple and environmentally-friendly process.    DETAILED DESCRIPTION - Preparation of esomeprazole sodium of formula (I) involves carrying out Grignard reaction of chiral compound of formula (VI) and Grignard reagent of formula (III), and carrying out salt-forming reaction of obtained esomeprazole of formula (VII).    M=magnesium or zinc, preferably magnesium;and    X=halo, preferably chloro.
NOVELTY - Preparation of esomeprazole (I) involves reacting benzimidazole-containing chiral compound (II) and Grignard reagent (III).    USE - Preparation of esomeprazole (claimed).    ADVANTAGE - The method enables preparation of esomeprazole having high purity with high yield of 90%, by simple, economical and environmentally-friendly process.    DETAILED DESCRIPTION - Preparation of esomeprazole of formula (I) involves reacting benzimidazole-containing chiral compound of formula (II) and Grignard reagent of formula (III).    M=magnesium or zinc;and    X=Cl, Br or I.
NOVELTY - The method comprises introducing penicillin crude product into a column chromatography, dissolving the product in an acid aqueous solution containing an organic solvent to obtain a penicillin solution, and separating purified product from the solvent. The penicillin is prepared by pre-treating non-pretreated fermentation solution containing penicillin, concentrating the treated solution by nanofiltration to obtain a concentrated liquid, and separating penicillin crude product.    USE - The method is useful for purifying penicillin (claimed).    ADVANTAGE - The method is capable of economically providing the penicillin with high purity and yield in an environmentally-friendly manner.    DETAILED DESCRIPTION - The method comprises introducing penicillin crude product into a column chromatography, dissolving the product in an acid aqueous solution containing an organic solvent to obtain a penicillin solution, and separating purified product from the solvent. The penicillin is prepared by pre-treating non-pretreated fermentation solution containing penicillin, concentrating the treated solution by nanofiltration to obtain concentrated liquid, and separating penicillin crude product. The pre-treatment step comprises separating mycelium from the fermentation solution using a solid-liquid separation method. The nanofiltration step is carried out using a DK or DL nanofiltration membrane or a carbon filter.
NOVELTY - 2,4-Dimethylbenzene-1-thiol (IV) is subjected to coupling reaction with 1-bromo-2-iodobenzene (III) in cuprous iodide in presence of chiral ligand and a base, to obtain 1-((2-bromophenyl)sulfanyl)-2,4-dimethylbenzene (IIa). The obtained 1-((2-bromophenyl)sulfanyl)-2,4-dimethylbenzene (IIa) is reacted with piperazine (IIb) in cuprous iodide in presence of chiral ligand and a base, to obtain 1-(2-((2,4-dimethylphenyl)sulfanyl)phenyl)piperazine (I).    USE - Preparation of 1-(2-((2,4-dimethylphenyl)sulfanyl)phenyl)piperazine used as pharmaceutical raw material.    ADVANTAGE - The method enables simple preparation of 1-(2-((2,4-dimethylphenyl)sulfanyl)phenyl)piperazine having high purity using readily available raw material with reduced by-products.    DETAILED DESCRIPTION - 2,4-Dimethylbenzene-1-thiol of formula (IV) is subjected to coupling reaction with 1-bromo-2-iodobenzene of formula (III) in cuprous iodide in presence of chiral ligand and a base, to obtain 1-((2-bromophenyl)sulfanyl)-2,4-dimethylbenzene of formula (IIa). The obtained 1-((2-bromophenyl)sulfanyl)-2,4-dimethylbenzene (IIa) is reacted with piperazine of formula (IIb) in cuprous iodide in presence of chiral ligand and a base, to obtain 1-(2-((2,4-dimethylphenyl)sulfanyl)phenyl)piperazine of formula (I).
NOVELTY - Preparing asenapine derivative (I), comprises reacting 3-(2-chloro-5-phenoxy-phenyl)-1-methyl-pyrrolidine-2,4-dione (II) in an anhydrous system with an acid anhydride under dehydration catalyst.    USE - (I) is useful for treating schizophrenia.    ADVANTAGE - The method is carried out in a simple, cost efficient and environmentally friendly manner with process stability to obtain high yield product.    DETAILED DESCRIPTION - Preparing asenapine derivative of formula (I), comprises reacting 3-(2-chloro-5-phenoxy-phenyl)-1-methyl-pyrrolidine-2,4-dione of formula (II) in an anhydrous system with an acid anhydride under dehydration catalyst. An INDEPENDENT CLAIM is also included for asenapine derivative (I), which is obtained by the above mentioned method.
NOVELTY - Method of converting mushroom fungal residue into bioorganic fertilizer, involves obtaining edible fungus mushroom residue, adding fermented chicken manure, inoculating secondary fermentation material, then adding silt, drying, crushing the mixture, adding viable cells, mixing, granulating the mixture, packaging the granules and obtaining the finished product.    USE - The method is useful for converting mushroom fungal residue into bioorganic fertilizer (claimed).
NOVELTY - Liquid fertilizer comprises 1 pts. wt. radix sophorae flavescentis, 2-8 pts. wt. calcium propionate, 1-5 pts. wt. salicylic acid, 6-10 pts. wt. zinc chloride, 4-8 pts. wt. manganese sulfate, 8-12 pts. wt. ferric sulfate, 1-5 pts. wt. magnesium oxide, 1-5 pts. wt. vitamin C and 40-60 pts. wt. organic matter.    USE - The liquid fertilizer is useful for fruit trees (claimed), killing pests, and preventing spoilage of fruits.    ADVANTAGE - The liquid fertilizer has stable property, no toxic and side effects, and good performance during fruit tree plantation; and increase fruit trees production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the liquid fertilizer, comprising (i) crushing organic matter, placing in a fermenter, adding microbial inoculum, fermenting at 30-40 degrees C for 3-7 days, and taking out the fermenting liquid; and (ii) dissolving radix sophorae flavescentis, calcium propionate, salicylic acid, zinc chloride, manganese sulfate, ferric sulfate, magnesium oxide and vitamin C by adding pure water, mixing with the fermenting liquid, and allowing to stand for 12-24 hours, and filtering to obtain the finished product.
NOVELTY - Sludge processing device, comprises a drive device, which is provided with a feeding port (1) at one end, a cylindrical body with at least three sections comprising a dewatering granulating section (3) connected with the feeding port, a middle section provided with drying section (5), and a carbide section (7) connected with a tube discharging port which is provided with a flame heating device, at the discharge end of the cylindrical body and an exhaust device (2) at the inlet end of the cylindrical body.    USE - Used as a sludge processing device.    ADVANTAGE - The sludge processing device: is cost efficient, environmental friendly; has high material crushing degree and high heat energy utilization rate; and exhibits simple construction and less operation cost.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of sludge processing device.    Feeding port (1)    Exhaust device (2)    Granulating section (3)    Drying section (5)    Carbide section (7)
NOVELTY - The method involves obtaining a biological diesel oil raw material. Alkali is added into the biological diesel oil raw material at 30-100 degrees Celsius. Electrolytic process is performed to obtain long carbon chain alkane at normal pressure range from 300-450 degrees Celsius. Catalytic cracking process is performed at normal pressure range from 220- 350 degrees Celsius. Cutting temperature of an aviation fuel blending component is about 105-240 degrees Celsius. An anode material is made of platinum, glassy, graphite and stainless steel.    USE - Biological diesel oil aviation liquid fuel preparation method.    ADVANTAGE - The method enables simplifying process, ensuring stability, reducing energy consumption and increasing production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating biological diesel oil aviation liquid fuel preparation method.'(Drawing includes non-English language text)'
NOVELTY - Preparing biodiesel, comprises (i) adding experimental oil, methanol and solid alkali catalyst into a three-necked bottle, and reacting by placing in a condensation reflux unit of a temperature-controlled reactor; and (ii) centrifuging, and layering, separating the product, carrying out acid pickling, and washing salt to obtain the product.    USE - The method is useful for preparing biodiesel (claimed).    ADVANTAGE - The method has high yield then traditional catalytic and heating processes; has high efficiency catalytic reaction; shortens the reaction time; recycles catalyst; is economical, and environmental friendly; and overcomes the problems of traditional method of producing large amount of waste acid, waste alkali, and shortcomings of corrosion of equipment.
NOVELTY - Method for improving salinity of soil involves using soil conditioner in an amount of 300-400 kg/hm2. The soil conditioner comprises 45-50 pts. wt. mixture of humic acid and phosphogypsum, 8-10 pts. wt. natural zeolite, 10-15 pts. wt. straw powder, 15-20 pts. wt. vermicompost, 15-25 pts. wt. mixture of Spartina alterniflora and sheep manure and 5-8 pts. wt. diatomite.    USE - Method for improving salinity of soil in North China (claimed).    ADVANTAGE - The soil salinity improvement method improves organic substance content to 60-70% and crop yield by 8.5-17.2%, and reduces pH by 0.85 or more.
NOVELTY - Biomass pyrolysis furnace comprises a furnace body, a pyrolysis chamber, an exhaust gas port, a gas recovery inlet, a charcoal outlet and a stirrer device and a recovery device. The furnace body is set with the pyrolysis chamber. The pyrolysis chamber is set with the gas exhaust port and gas recovery inlet. The lower part of the pyrolysis chamber is set with the charcoal outlet. The stirrer is set in the pyrolysis chamber. The gas exhaust port is connected to the recovery device.    USE - Used as a biomass pyrolysis furnace.    ADVANTAGE - The biomass pyrolysis furnace: has compact structure, low energy consumption effect and high oil production rate; is convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biomass pyrolysis furnace.
NOVELTY - The method involves filling a methanol raw material into a catalyste contact reactor. Pneuma liquid and gas-liquid are separated by a reaction product. The gas-liquid is entered into a fluidized bed reactor. A catalyste contact reaction is performed in the fluidized bed reactor, where the temperature of the fluidized bed reactor is about 350 to 480 degrees Celsius. The pneuma liquid is passed into a reaction product condenser. The methanol raw material is heated by a methanol raw material heating furnace.    USE - Methanol petrol preparing method.    ADVANTAGE - The method enables ensuring high production efficiency and high petrol quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a methanol petrol preparing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a methanol petrol preparing device.
NOVELTY - Fuel methanol and additive are synthesized by preparing 5% additive by mixing 1% ferrocene dissolved in toluene, 1% acetone, 1% 90# gasoline, and 2% refined camphor with small amount of methanol, mixing additive with 75% methanol, mixing with circulation pump, adding 20% water, and mixing with circulation pump to completely dissolve.    USE - Synthesis of fuel methanol and additive (claimed).    ADVANTAGE - Fuel methanol and additive has improved heating value, and synthesis is simple and low-cost and has good effect.
NOVELTY - A micro-element nano-hydrogen fuel, comprises: 55-65 wt.% hexane, 25-35 wt.% methanol and 5-15 wt.% water.    USE - As micro-element nano-hydrogen fuel (claimed).    ADVANTAGE - The micro-element nano-hydrogen fuel and hydrogen fuel generator, are energy saving; and provide environmental protection.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for micro-element nano-hydrogen fuel generator (1) comprising: a reaction groove (20) having a reaction space, where the reaction space is for containing raw material; feed inlet (30) connected to the reaction space; air supply module (40) with air inlet part, connecting tube and discharge part, where second end of the connecting tube connected with the inlet part and the discharge part and the discharge part is set in the reaction space, and is formed with multi-holes and the gas hole is connected with the connecting tube connected; and fuel output part (50), which is set in the reaction groove and connected in the reaction space, and the fuel output part is higher than the air supply module.    DESCRIPTION OF DRAWING(S) - The figure shows a three-dimensional view of the micro-element nano-hydrogen fuel generator.    Micro-element nano-hydrogen fuel generator (1)    Reaction groove (20)    Feed inlet (30)    Air supply module (40)    Fuel output part (50)
NOVELTY - A Chinese fir fuel comprises mixed and extruded 85-95 pts. wt. Chinese fir chips and 5-15 pts. wt. Mason pine resin.    USE - A Chinese fir fuel for smelter, school, and hotel boilers.    ADVANTAGE - Chinese fir fuel is environment-friendly, easy to light, smoke-less, and low-cost and has high efficiency and combustion value, less combustion ash, and simple preparation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of Chinese fir fuel which involves drying Chinese fir chips to moisture content of 35-40%, heating Mason pine resin to fully dissolve into viscous for, mixing with dried Chinese fir chips, extrusion-molding with pressure of 60-80 T for 3-10 minutes, drying, packaging, and storing.
NOVELTY - Bioreactor comprises a carriage (1-1), an air stream vibrating broken arch (1-2), a discharge carriage (1-3), a flat bottom surface (1-4), and an air outlet tube (1-5), which is guarded by a valve (1-7). The bioreactor comprises an upper and lower flat cross-sectional area, and they in turn are attached to the air stream vibrating broken arch.    USE - Bioreactor used for performing solid-state fermentation (claimed).    ADVANTAGE - The eco-friendly bioreactor is widely applicable in industries, and effectively perform dry fermentation process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a bioreactor, which comprises a flat bottom surface attached to a feed pipe material, the air stream vibrating broken arch, and the broken arch carriage to carry materials, which are fed from top to bottom of the bioreactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a bioreactor.    Carriage (1-1)    Air stream vibrating broken arch (1-2)    Discharge carriage (1-3)    Flat bottom surface (1-4)    Air outlet tube (1-5)    Valve (1-7)
NOVELTY - Multiple trapezoidal biogas digester comprises a flow-water biogas generating pool, which is respectively set with two baffles, and a limiting biogas space for not letting gas leakage.    USE - The digester is useful for producing biogas.
NOVELTY - An Achromobacter sp. strain W143 (CCTCC NO: M2014154), is new.    USE - The Achromobacter sp. strain W143 is useful for degrading polycyclic aromatic organic contaminants chosen from polycyclic aromatic hydrocarbon, preferably phenanthrene, naphthalene, fluorene, and fluoranthene (all claimed) in soil.    ADVANTAGE - The Achromobacter sp. rapidly degrades pollutants, has excellent adaptability to wide range of pH, salinity and temperature, and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for degrading organic pollutant, which involves contacting polluted sample with the Achromobacter sp. strain W143.
NOVELTY - An energy-saving and environment-friendly fuel oil, comprises 10-20 parts by mass biological diesel oil, 10-40 parts by mass coal oil, 20-40 parts by mass plant grease, 5-10 parts by mass microbial grease, 3-6 parts by mass vegetable oil acid or ethanol amine, 10-25 parts by mass methanol, and 10-40 parts by mass steam oil, where the steam oil is obtained by distillation of waste oil and/or diesel and/or trench oil.    USE - As fuel oil (claimed) for applicable to all types of diesel combustion of fuel oil, and used in ceramics, lime kiln, drying furnace, steam boiler, incinerator, melting furnaces, melting furnaces, sintering furnace, smelting furnace and all kinds of heavy-industrial furnaces and power generation equipment.    ADVANTAGE - The fuel oil is energy-saving and environment-friendly fuel oil; has high calorific value, emissions cleanliness and stable property; is non-toxic and tasteless; is capable to fully reach the ignition temperature of use requirements to dispose of waste oil properly; and also saves energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fuel oil involving (i) first mixing biological diesel oil, plant grease, coal oil, microbial grease and steaming oil together, and stirring uniformly; (ii) then adding methanol, and vegetable oil acid or ethanol amine simultaneously and stirring to give the finished product.
NOVELTY - The system comprises a mash liquid tank, an anaerobic fermentation device, a marsh gas desulfurization purifier, a gas filter, a gas mixer, a drying gas turbocharger, a fire arrestor, an electromagnetic valve, a constant voltage device, an air storage tank and a biogas electric generator. The biogas electric generator is connected with the mash liquid tank through a pipeline. The air storage tank is connected with a methane generator. The mash liquid tank is adjusted to a temperature of 30-35 degrees C and connected with the anaerobic fermentation device.    USE - Marsh gas power generation system.    ADVANTAGE - The system economically generates the marsh gas with low emission and high performance in an eco-friendly manner.
NOVELTY - The system has a nitrogen-enriched pyrolysis sub-system that is connected with a coke nitrogen-doped sub-system, a nitrogen introducing sub-system and a nitrogen-enriched gas condensing system. An exogenous nitrogen subsystem is used for introducing nitrogen into nitrogen-enriched pyrolysis sub-system and coke nitrogen-doped sub-system. The nitrogen-enriched pyrolysis sub-system is used for lowering biomass and exogenous nitrogen to promote the reaction. The rear circulation of combustion gas into hot solution subsystem is performed to provide thermal heat.    USE - Nitrogen-enriched biomass pyrolysis system for cogeneration of nitrogen chemicals and nitrogen-doped coke.    ADVANTAGE - The efficient conversion of biomass is achieved. The operation reliability and stability are improved. The utilization rate is improved and environment pollution is reduced. The heat exchanging effect is improved. The increase in yield is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the nitrogen-enriched biomass pyrolysis system.    Wet ammonia spray tower (23)    Water circulation pump (24)    Amine water cooling tower (25)    Water absorption liquid reflux pump (26)    Amine mix water tank (27)
NOVELTY - Environment-friendly industrial fuel oil comprises 10-20 pts. wt. biodiesel, 20-40 pts. wt. vegetable fats and oils, 3-6 pts. wt. vegetable acid oil or ethanolamine, 10-25 pts. wt. methanol and 10-40 pts. wt. steam oil. Steam oil is composed of waste oil, diesel oil and/or drainage oil obtained after distillation.    USE - Environment-friendly industrial fuel oil.    ADVANTAGE - The product is non-toxic and non-volatile and has high heat value and good stability performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of environment-friendly industrial fuel oil comprising stirring biodiesel, vegetable fats and oils and steam oil, adding vegetable acid oil or ethanolamine and methanol and stirring.
NOVELTY - Degradation agent comprises microbial agents and wheat bran in a weight ratio of 1:5-10, where the microbial agents comprises 20 wt.% Cellulomonas sp., 20 wt.% Phanerochaete chrysosporium, 18 wt.% Bacillus cereus, 15 wt.% Pseudomonas aeruginosa, 10 wt.% Aspergillus niger, 7 wt.% Streptomyces hygroscopicus, 7 wt.% Rhodococcus and 3 wt.% Paracoccus denitrificans.    USE - The degradation agent is useful for degrading straw powder (claimed) e.g. rice and corn straw.    ADVANTAGE - The degradation agent provides bioorganic fertilizer, and is environmentally-friendly and hence it is safe.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the agent, which involves activating above-mentioned microbes, where the number of viable cell in the agent is 2-4x 108, mixing the activated microbial culture, adding wheat bran to the mixture, drying mixture, testing and packaging mixture.
NOVELTY - Production of biogas involves mixing sludge and straw pretreated using sodium hydroxide solution, obtaining mixed substrate, inoculating with methanogenic sludge, and subjecting to anaerobic digestion treatment.    USE - Production of biogas (claimed).    ADVANTAGE - The method enables environmentally-friendly, effective and stable production of biogas by effective disposal of rice straw, with high energy recovery.
NOVELTY - Producing a lower fatty acid, comprises allowing the sewage sludge to settle in a tank, discarding the supernatant to obtain sludge samples, mixing the sludge samples with an alkyl glycoside surfactant and then fermenting under anaerobic environment.    USE - The method is useful for producing a lower fatty acid (claimed).    ADVANTAGE - The method efficiently removes nitrogen and phosphorus from sewage, and improves the ability to produce organic acids in the sewage, thus enabling easy processing of sludge reduction.
NOVELTY - This new utility model relates to one kind of grain production safe plant insulating micro-ecological preparation system. It can effectively increase production efficiency of soil microorganism repairing, and to the utmost extent and guarantee the activity, is full of organic substance and supplementary soil, soil microorganism area system form, especially suitable for grain crops for production use, to soil improvement, increase yield, which ensures quality and effect. Device, a reaction kettle, a cutting pump, high pressure homogenizer, high pressure impact machine, processing ultra-structure, micro-nano particle coating process and HyM strain target temperature of this new utility model can regulate and control machine box to strain variation control tank connected in turn, with is connected with the induction device between temperature in all regulate and control system and HyM strain tank.
NOVELTY - Above this utility new type claims a biomass carbonizing kiln purification dust removing device, wherein the device comprise kiln body (1), a smoke pneuma exit (4), steel wire network (5), layer (6) and water tube (7), a kiln body (1) of one side set with a kiln body door (3), kiln body (1) upper part is set with smoke pneuma exit (4), a smoke pneuma exit (4) is set with a steel wire network (5), steel wire network (5) is set with a smoke absorbing layer (6), a smoke absorbing layer (6) is set with a nozzle (8), a spray head (8) connecting water tube (7). This utility new type to solve technology problem provide a biomass carbonizing kiln one purification dust removing device, a smoke in the device can be valid to biomass carbonization kiln burning charcoal purification process, avoids the pollution of the environment.
NOVELTY - The method involves calculating a size of a lead selenium (PbSe) quanta point. A multi-wavelength near infrared LED (1) of a wave length unit is determined. A wave length number is selected according to an actual quantity. A tested gas absorbing spectrum is determined. The lead selenium quanta point is dissolved in chloroform mix solution and UV glue mix solution. An ultrasonic processing operation is performed. A gallium nitride (GaN) chip is fixed with an excitation light source. Lead selenium quanta point multi-wave length near infrared LED preparing process is performed.    USE - Lead selenium quanta point multi-wave length near infrared LED preparing method.    ADVANTAGE - The method enables detecting multi-gas, improving preparing sensitivity and preparing stability, increasing fluorescent yield and reducing processing cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a lead selenium quanta point multi-wave length near infrared LED gas detecting method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an lead selenium quanta point multi-wave length near infrared LED.'(Drawing includes non-English language text)'    Multi-wavelength near infrared LED (1)    Convex lens (2, 4)    Pneumatic air inlet room (3)    Infrared spectrograph (5)
NOVELTY - This utility new type relates to a one via LNG for preparing and purifying H2 of device, wherein the LNG for preparing and purifying H2 of device, comprise the hydrogen unit, the heat exchange unit, auxiliary refrigeration unit, separate unit, conveying pipeline of the LNG storage tank after heat exchange unit rear connecting to the hydrogen unit, unit hydrogen of hydrogen crude product conveying pipeline after exchanging unit rear connecting to auxiliary refrigeration unit, auxiliary refrigeration unit a separate unit, separate hydrogen output pipeline and by-product conveying pipeline of output end a connecting unit and by-product to the hydrogen storage device. Two parallel separate group unit in the auxiliary refrigeration unit output end. Separate unit of a pipeline and by-product hydrogen conveying pipeline after exchanging unit a connect rear and side product to the hydrogen storage device. The device can make full use of LNG cold energy so as to save energy, a purpose of protecting the environment.
NOVELTY - This utility new type provide the one using a micro-algae biogas purification process of light biological reactor. It solves the problem that the existing for a micro-algae light biological reactor sewage treatment process in the claims, in real time monitoring a lack of each data index of a. The a biogas purification of by microalgae light biological reactor comprise a liquid storage tank for storing biogas, inner liquid storage tank into the feeding tube and the discharge tube, a liquid storage tank is set with discharge valve, further inserted with CO2 air inlet tube, the pH sensor, illumination sensor and liquid sensor inner inner surface at the bottom of the liquid storage tank is set with lighting device, a liquid storage tank set with sterilizing device, a liquid storage tank. This utility new type by microalgae process of efficient biogas purification Item has a important breakthrough, the method is simple, a low cost, a simple and convenient operation, reliable action, and has an excellent market promotion, for slurry waste water solves the problem of a has very important meaning.
NOVELTY - This utility new type claims a one biomass thermal cracking furnace, comprise a furnace body, the inner of the furnace body from the upper to lower a sequence in turn are connected set with a storage bin, a cracking chamber, activate cavity and carbon chamber, a cavity wall of a storage bin set with flue, upper cavity wall of said cracking cavity set with air inlet, oxygen inlet and an ignition hole, a cavity wall of said cavity is set with steam tube and activate activate, a cracking cavity set with inner carbon crushing mechanism, said inner cavity is set with activate activate stir scraping mechanism, bottom of said carbon chamber set with the carbon outlet, and the carbon plate set with the inner carbon. This utility new type of structure design, it can produce high heat value combustible gas, and it can prevent the coking and blocking, at the same time, able to crack or large volume biomass fuel of length, good efficiency, which greatly increase energy utilization rate, saves resource of biomass variety has good adaptability, is suitable for wide range, which is good for wide popularization and application.
NOVELTY - This utility new type claims a one animal excrement and organic garbage comprehensive processing device, the fermentation device comprise part set with the colony under a fermentation tank, fermenting tank side wall of a part in a set with a garbage inlet and excrement inlet, the fermentation tank is set with one with the pneuma pump connecting a gas inlet tube, inner surface of the fermentation tank is coated with one layer of cement coating, a cement coating with one layer set with anti-seepage layer, in marsh gas tank comprise tank body, the tank body lower part and the lower part in the fermentation tank through one of inclined feeding port connected fermentation tank connect with one tank body connected with a air channel, middle part of tank body with one block floating board mounting a limit coarse slag, tank body top part of a marsh gas output tube in turn set with dryer and desulfurizer, tank body side wall in lower part through one of a channel and the inclined slag groove connecting the top of discharging groove with one mounting a seal plate. The poultry excrement and organic garbage comprehensive processing device solves the problem that the livestock excrement and organic garbage is difficult to complete decomposition of.
NOVELTY - This new utility model provide a kind of one novel biological decomposing inoculant tank, comprising a tank body, a stirring shaft, a feed port, a discharge port, driving motor, marsh gas collecting device, air compressor, upper tank body equipped with feedstock port, a discharging port, the stirring shaft is set with in tank body, and the driving motor and connected with the upper stirring shaft provided with stirring paddle leaf big, small stirring paddle leaf, large stirring paddle leaf and the small stirring paddle leaf are vertical placed, inner tank body wall provided with wear-resisting layer, wear-resisting layer set with heating layer outside the tank body top set with marsh gas collecting device, is set with side inside the tank body top part in the spray device through the liquid outlet port pipe and activate liquid generator is connected and set with air inlet on upper part of tank body one side, through pipeline and air compressor connected. This new utility model for stirring and crushing the material mixing effect obvious, the marsh gas and material through the marsh gas collecting device collecting, energy is full use, this utility new type has simple structure, using suitable operation, and high efficiency.
NOVELTY - This utility new type claims a negative pressure discharge one kitchen garbage processing device, comprise machine frame, a fermenting cabin, heating interlayer, stir shaft, stir motor, a speed reducer, an electric control system, heat discharge pipeline, filter and seal box, at least one deodorizing absorbing layer and centrifugal fan, a fermenting cabin mounting the machine frame a, heating interlayer is set at the bottom of the fermentation bin, a stir shaft rotate in a fermenting cabin inner, a speed reducer two end is fixedly connected with one end a stir shaft and a stir electric machine, heat discharge pipeline seal in the fermentation bin and a seal filter deodorizing box, centrifugal fan and stir motor are connected with the electric control system, centrifugal fan and the filter and box seal, seal and absorbing layer seal set on the filter deodorization box in seal, the bottom seal filter deodorizing tank is set with a drain valve and drain valve. The negative pressure discharge kitchen garbage processing device capable of preventing odour water steam leakage volatilized, so as to avoid a sub-atmospheric pollution.
NOVELTY - This utility new type claims a humidity level one negative pressure discharge kitchen garbage processing device, comprise machine frame, a fermenting cabin, heating interlayer, stir shaft, stir motor, a speed reducer, a set with a humidity controller and a timing module of electric control system, dry and wet detecting module, a timing module, heat discharge pipeline, filter and seal box, at least one deodorizing absorbing layer and centrifugal fan, heat discharge pipeline seal in the fermentation bin and a seal filter deodorizing box, centrifugal fan and stir motor are connected with the electric control system, centrifugal fan and the filter and box seal, seal and absorbing layer seal set on the filter deodorization box in seal, wet and dry detection module mounting on the input end of said centrifugal fan and the deodorizing box air outlet humidity controller is electrically connected with the timing module and the humidity controller is electrically connected. The humidity level negative pressure discharge kitchen garbage processing device to dry and wet is a reference process, thus it is more valid of a heating drying.
NOVELTY - This new utility model relates to one of ultrasonic wave counter-current extracting taxol is non-toxic production system, the production system includes extracting device comprises, detoxification device, recycling device and cooling device, the production system after taking red bean shirt plant through cleaning crushing treatment of crude product as raw material, first carrying out counter-current extraction with ultrasonic wave ultrasonic wave extraction tube, then using dryer for oxidation detoxification is detoxication method purifying, the whole production system arranged wash cooling device on line, further optimizing of extracting process, no pollute to the target is high purity extraction.
NOVELTY - This utility new type claims a one for biomass raw material a machine-made charcoal of carbonization device, wherein the device comprise, tube, a tail pneuma conveying pipeline, heat preservation heat insulation device, wherein it further comprise oxygen detection device, oxygen conveying pipeline, circulation water cooling device, a heat insulation heat preservation device mounting furnace outside the furnace is provided with a combustion plate of multi-through hole is divided into a carbonizing room and the oxygen supply room, set with an ignition device and a device inner oxygen in the carbonizing room, a furnace tail pneuma exit and the tail pneuma conveying pipeline connecting the inner oxygen supply room set with a oxygen conveying pipeline. This utility new type to solve technology problem to be solved is the device for a uniform oxygen supply of carbonizing room, increase quality and carbonizing the carbon rate, cooling a tail pneuma and prolongs the use life of fan, the system not only shortens the production period, further increase the carbonization quality, realize efficient production and combine a energy-saving and environment-friendly.
NOVELTY - This utility new type claims a biomass gas for one device, comprise the gasification furnace body, a rotary grate, interaction material level meter, reducing cabin door control mechanism, feeding mechanism, discharging mechanism and coke dust-removing system, a gasification furnace top centre position set with material inlet, bottom set with a slag discharging mechanism and the outlet is connected with the feeding mechanism and the material inlet is connected, reducing cabin door control mechanism set on the feeding mechanism and a part of, interaction material level meter set on the top surface of gasification furnace, a rotary grate set in the gasification furnace body inner, coke dust-removing system and the gasification furnace body is connected, the utility model is new type of structure design, reasonable structure, easy to realize, valid of reducing manufacturing cost, through a rational structure design to make the fuel burn fully, the gasification efficiency greatly increase energy utilization rate, saves resource, and the working stability is good, the material is a high precision, good effect, good adaptability and variety, which is good for wide popularization and application.
NOVELTY - This utility new type claims a one the hydropower station water surface garbage into fuel of a, through transmission belt in turn comprise of a garbage stacking chamber, sterilizing room, a cutting system, mix stirrer, a compressor, a drying room, a granulator, and a finished product bin, further comprise combustion material, adhesive material, water collecting pool, a high temperature crucible, biological degrading tank, a test chamber and discharging. This utility new type garbage becomes the new fuel, not only the requirement of sanitary production, purification and subsequent environment of garbage treatment, forming fine fuel of uniform specification, changes waste into valuable, solves the problem that the waste caused by the accumulation of a secondary pollution, which is good for protecting the environment, but also get of the seepage water of a water sterilizing room and a duration of fuel resource, has wide social value and economic value, the form of a stacking process, solves the water seepage problem of second pollution environment.
NOVELTY - A one-rich hydrogen water reaction device, include a device main body, the device main body has a holding cavity for holding a reaction liquid, the inner containing cavity set with a hydrogen generator, further comprise a pedestal, in part of pedestal set with a splicing part, device main body of the bottom set with the inserting part inserting match of. hydrogen generator comprise a power joint, electric joint set in the slot and a part connecting with the splicing, splicing part set with electric conduction sheet, electric conduction sheet and a power joint; further set with switch with a pedestal, electric conduction with the electric connecting switch. This utility new type is provide the pedestal, and set with a splicing part, a part in a pedestal set with electric conduction sheet, so the pedestal with electric conduction function. A hydrogen generator set with through electric joint, electric joint and the electric conduction piece a contact a, set with a conducted through pedestal for hydrogen generator, the hydrogen generator to the commercial power grid of a directly, increase the utility new type of use.
NOVELTY - Method for biologically converting municipal sludge to humus, involves adding complex comprising Bacillus subtilis, Aspergillus niger and lipase (weight ratio of (3-5):(2-4):(2-4)) to municipal sludge and straw, and carrying out solid state fermentation.    USE - The method is useful for biologically converting municipal sludge to humus (claimed) of Q/BJZZT0004-2014 (industrial standard).    ADVANTAGE - The method is performed in a short period of time, and does not generate peculiar odor during fermentation.
NOVELTY - This utility new type claims a one can be a indigenous microbial expanding culture device of continuous pollutant, the device comprise the expanding culture cavity and storage cavity, mounting with a liquid level controller and a lifting pump and a tube of a channel. The river. indigenous microbe cultivation process in, the liquid level controller control the opening and closing of the lifting pump, then the expanding culture is added to the dirt in the river indigenous microbe through a tube and the lifting pump. The device being introduced into a nanofiltration sewage body in rear of the indigenous microbe number and activity in river environment obviously increase, so as to achieve a pollutant of entering into a continuous. The device is not using the outer adding nutrition agent from a river sludge is a source, and the water in a river has rich nutrition, low in the condition of proper temperature, dissolved oxygen, a proliferation and cultivation of the indigenous microbe, has the characteristics of safety and cost.
NOVELTY - This new utility model relates to one of farm waste water treatment system, comprising orderly provided with the solid liquid separating device, regulating pre precipitation pool, Anaerobic reaction pool, the first reaction sediment pool, a biochemical pool, the second reaction pool and precipitate pond. Anaerobic reaction pool and air water separator connected, gas water separator through desulfurization device and gas storing tank connected, gas water separator, a desulfurizing device, and gas composed of methane using system; regulation pre precipitation pool, Anaerobic reaction pool, the second reaction sediment pool respectively connected and concentrated pool, pool and concentrate filter connected; between the first reaction sediment pool and regulating pre sink pool form the first circulation system, the second reaction sediment pool between biochemical pool and form the second circulation system, between the second reaction sediment pool and regulating pre sink pool form the third circulation system. This new utility model set waste water discharge, sludge treatment and use in integrated marsh gas, to reasonable effective using resource and target.
NOVELTY - This utility new type claims a environment-friendly one chicken manure processor, include: drying machine, air purifier, the structure is set with hot air furnace the dryer front end, set with a inner the dryer, and inner set with a crushing shaft, set with feeder at a front end, set with a discharging port on the rear end a, rear machine end set with spray-type air purifier set with tube in the air cleaner connected upper part, tube connected the other end set with draught fan, set with circulation water tank at the bottom of air purifier set with the air inlet tube of the air purifier, a Venturi tube one end set with water pump, water pump front end set with circulation water tank, overflow tube on the side set with a circulation water tank, set with taking ash bucket at the bottom of the circulation water tank. This utility new type has a structure design is reasonable, the volume is small, environment protection, no pollution and no pollution to the environment a peculiar smell, convenient operation, clean efficiency is high and so on.
NOVELTY - This utility new type relates to a chrysanthemum straw to decay fast fermenting tank, one category agro-horticultural waste comprehensive utilization field, to be solved technology problem provide a one structure is simple, convenient and fast operation of fresh chrysanthemum straw fermenting tank, using a technology solution is as follows: a one pole chrysanthemum to ferment tank, bottom comprise front wall, a left side wall, back wall, right side wall and tank, a front wall, a left side wall, back wall, right side wall and pool bottom is square fermentation tank of non-; said fermenting tank of tank top with film; a front wall set with a movable door plate, a rear upper wall of the fermentation monitoring port, the bottom of said tank bottom is set with a circulation channel, a heat circulation channel tank bottom to the top, a heat circulation channel close to one front side wall is provided with a heating port, a heat circulation channel relative to the heating port of far end set with an air outlet.
NOVELTY - This utility new type claims a vehicle one organic waste fast recycling a enzyme processing device, comprise transport vehicle, and a cylinder type reaction kettle, water storage tank transport vehicle body a, the fermentation liquid tank, a first electric machine, a speed reducer and a transmission device, a reaction kettle transverse set and matched with a paddle stirrer, the stirrer blade through transmission device in turn with the speed reducer and a motor, the top of inner reaction kettle is further set with a nozzle, the nozzle through pipeline with the water tank and the fermentation tank is a liquid, and an outer wall of the reaction kettle is embedded with a flexible plate is also set with heat preservation layer outer flexible electro-thermal plate, tail end of reaction kettle set with a feeding port, the bottom is set with a discharging port. Three function This utility new type organic solid waste of a collecting, transporting and processing thremal enzyme of set so as to increase processing efficiency and flexibility of organic waste.
NOVELTY - This utility new type relates to one a biomass pyrolysis device, a biomass pyrolysis of one device, at least composed by tube, , support device, driving device, front tube is divided into two a rear part, the front part set with inner , with the coaxial tube, rear part tube inner wall set with a staggered arrangement of; front rear tube set with seal cover. And the fixed-bed pyrolyzing reactor compared greatly increase the heat efficiency of the circulation fluid-bed pyrolyzing reactor, cancels the carrier, reduces the energy consumption, and cone rotate a solution reactor, biomass pyrolysis completely, a quantity a a large scale reactor.
NOVELTY - This utility new type relates to a one biomass increase heating uniformity and efficiency of a baking system, comprise biomass dryer, a biomass feeding screw baking unit, a burner, a gas circulation system, product collecting unit, cooling the product a, a screw rod baking unit comprise screw roaster, the external part at least roaster with a jacket, the jacket and the burner through the burner flue gas pipeline connected, the roaster is provided with screw, the screw pole of roaster shaft is hollow shaft, hollow shaft fixed with a smoke pneuma tube one, the roaster heat jacket exit tube and smoke collector connected. The utility model increase the uniformity of valid screw roaster according to temperature, of a baked product quality, but also increase the heat transfer efficiency reduces the heat loss. Valid combine smoke, baking product is cooled and a biomass dryer of a burner, futher increase the system efficiency.
NOVELTY - This utility new type claims a one kitchen garbage of anaerobic digestion device, an anaerobic digestion device of reactor main body inner set with solid phase reaction area and liquid phase reaction area, reactor top part set with an air outlet, a return water inlet, and measuring, low water return water inlet part set with spray head, the liquid phase reaction area set with a water outlet, the bottom of reactor set and water inlet pipe. The time for a kitchen garbage anaerobic digestion, through immersion-type anaerobic digestion and shower filter. alternately operation of mode, can make the solid phase and liquid phase residue waste liquid of kitchen garbage is fully anaerobic digestion reaction, to the kitchen garbage is a maximum, a maximum resource processing.
NOVELTY - The automatic remote control enzyme reactor has an organic solid waste treatment system which is provided with a parameter sensor, a code brake device, a programmable logic controller (PLC) and 3G industrial intelligent gateway. The PLC is connected with a remote monitoring centre through the 3G industrial intelligent gateway. A mobile terminal is used for login the remote monitoring centre.    USE - Automatic remote control enzyme reactor for processing industrial organic solid waste.    ADVANTAGE - The strength of the reactor is reinforced, and the production process for different organic solid wastes is performed, and the effective quality control of reactor is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the automatic remote control enzyme fast processor. (Drawing includes non-English language text)
NOVELTY - This utility new type claims a hydrogen cooled machine one a hydrogen generating system, belonging to the field of energy utilization technology field. This utility new type hydrogen purification system with the oxygen system is connected with a hydrogen-oxygen fuel cell group, fuel cell group through the chopper and the lithium ion power battery group, hydrogen purification system, hydrogen-oxygen fuel battery group, a chopper, a lithium ion power battery group are connected with the control system connected with the hydrogen purification in a deoxidizing device, a cooler, a drying device, filter, hydrogen and hydrogen storage tank in turn a compressor, entrance end of deoxidizing device and hydrogen cooled machine set hydrogen outlet is connected with exit end of hydrogen storage tank through a valve and the nagetive hydrogen-oxygen fuel cell group. This utility new type can be used for cooling the waste hydrogen recovery, purification a rear set of process, and then the rear process of hydrogen as hydrogen source of hydrogen-oxygen fuel cell, which greatly saves the energy, and reduces the environment pollution.
NOVELTY - The artificial sewage processing system has an artificial wetland tank (1) equipped with a solar energy plate (14) on top, and an immobilized microorganism plate (5). A sand layer (2) is formed on top of the microorganism plate while an artificial mix matrix layer (3) and a gravel layer (6) are provided respectively at the lower part of the tank after the microorganism plate. A water branch tube (13-b) penetrates in the gravel layer while an aeration tube (13-a) penetrates tank and provided between microorganism plate and artificial mix matrix layer.    USE - Artificial sewage processing system.    ADVANTAGE - Improves efficiency of sewage processing by combining use of artificial wetland and solar energy to enhance microbiological effect while occupying small floor area and requiring low investment cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the artificial sewage processing system.    Artificial wetland tank (1)    Sand layer (2)    Artificial mix matrix layer (3)    Immobilized microorganism plate (5)    Gravel layer (6)    Aeration tube (13-a)    Water branch tube (13-b)    Solar energy plate (14)
NOVELTY - Preparing combination oral liquid, by extracting Astragalus, fried Atractylodes, dried orange peel, Ophiopogon root, radix scutellariae, hawthorn and semen raphani using water, passing the extract through ultrafiltration membrane, concentrating supernatant to obtain clear paste, mixing clear paste and honey, adding potassium sorbate and purified water to the mixture, and passing the mixture through tubular membrane ultrafiltration having molecular weight cutoff value of 10000-200000 at 0.1-0.4 MPa, 0-40 degrees C and 50-300 l/m2.hour.    USE - The method is useful for preparing combination oral liquid which is useful for promoting digestion in athletes (claimed).    ADVANTAGE - The method is suitable for industrial production, cost-effective and consumes less time and energy.    DETAILED DESCRIPTION - Method for preparing combination oral liquid, involves (a) extracting Astragalus, fried Atractylodes, dried orange peel, Ophiopogon root, radix scutellariae, hawthorn and semen raphani using water, (b) passing the extract through ultrafiltration membrane having pore size of 20-200 nm at 0.1-0.4 MPa and 15-85 degrees C, collecting supernatant, and concentrating the supernatant, or passing the extract through ultrafiltration membrane having pore size of 20-200 nm at 0.1-0.4 MPa and 15-85 degrees C, collecting supernatant, passing the supernatant through tubular membrane ultrafiltration having molecular weight cutoff value of 10000-200000 at 0.1-0.4 MPa, 0-40 degrees C and 50-300 l/m2.hour, and concentrating the filtrate to obtain clear paste, and (c) mixing the clear paste obtained in step (b) and honey, adding potassium sorbate and purified water to the mixture, and passing the mixture through tubular membrane ultrafiltration having molecular weight cutoff value of 10000-200000 at 0.1-0.4 MPa, 0-40 degrees C and 50-300 l/m2.hour.
NOVELTY - Raney nickel catalyst having nickel content of 86-95 wt.%, and specific surface area of 85-180 m2/g, is claimed.    USE - The Raney nickel catalyst is useful for fixed bed methanation (claimed).    ADVANTAGE - The Raney nickel catalyst: has uniform grain diameter, high machinery strength and high and catalytic activity; and can be prepared in a method that is suitable for large-scale production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the Raney nickel catalyst, comprising: (a) grinding nickel-aluminum alloy to 40-120 mesh granules, soaking in an organic solvent for 5-60 minutes, then soaking in absolute ethanol for 5-10 minutes, then washing with deionized water for 2-3 times, drying at 70-110 degrees C for 1-4 hours, and cooling to room temperature, (b) placing a stainless steel vessel containing sodium hydroxide solution in a constant temperature water bath, installing a magnetic field generator in the constant temperature water bath, adjusting magnetic field strength, adding the dried nickel-aluminum alloy powder to the sodium hydroxide solution with stirring, heating with stirring at 10-60 degrees C for 2-12 hours, and after the completion of the reaction, removing the upper layer, and (c) re-adjusting the magnetic field strength, repeatedly washing with deionized water until the pH is neutral, and rinsing with anhydrous ethanol for 2-5 times to obtain Raney nickel catalyst; and    (2) using the Raney nickel catalyst in a fixed bed methanation, comprising adding the Raney nickel catalyst to the fixed bed reactor containing syngas having a molar ratio of hydrogen:carbon monoxide of 3-3.5, where the reaction carried out under a pressure of 1-4 MPa, at 400-650 degrees C, and volume space velocity of 7000-9000 l/hour-kg.
NOVELTY - Recycling combustible solid wastes involves squeezing household wastes and dehydrating, crushing, separating first light-weight and heavy-weight materials, finely crushing, magnetic separation of first heavy-weight materials, finely crushing and winnowing, magnetic separation of second light-weight materials, finely crushing and winnowing, mixing first, second and third light-weight materials and crushing, sorting and crushing other combustible solid wastes, mixing obtained fist and second crushed materials with auxiliary agents and then passing to a molding machine.    USE - The method is useful for recycling combustible solid wastes to produce refuse derived fuel (claimed).    ADVANTAGE - The method is capable of rapidly recycling the combustible solid wastes in a cost effective and eco-friendly manner.    DETAILED DESCRIPTION - Recycling combustible solid wastes comprising household wastes and other combustible solid wastes including waste obtained from industrial recycling process, industrial waste and hazardous waste, involves (a) squeezing household wastes and dehydrating, crushing, separating first light-weight and heavy-weight materials and then finely crushing, magnetic separation of the first heavy-weight materials and finely crushing and winnowing for 2 times to obtain second light-weight and heavy-weight materials, (b) magnetic separation of the second light-weight materials, finely crushing and then winnowing to obtain third light-weight materials, (c) mixing the first light-weight material, second light-weight and third light-weight materials and crushing to obtain first crushed materials, (d) sorting and crushing the other combustible solid wastes to obtain second crushed materials, (e) mixing the first crushed materials and second crushed materials with auxiliary agents, and (f) passing the mixed material to a molding machine to form predetermined shape of refuse derived fuel.
NOVELTY - This utility new type claims a one temperature control of a sow, include body, a guardrail, a excrement-leaking plate, fermenting pad, crib, corridor, mounting water curtain machine a corridor on one end wall, the other end wall mounting a fan, time passage two of side wall are set with a movable shielding, need cooling, the movable shielding unfolded and put down, the sow one form a relative closed space, of a one end wall of a water curtain machine and the other end wall of the fan is opened, a cold wind cooling. Upper wall of corridor two side are set with a water tube, the water tube is provided with a draining hole, for a sow casting water shower cooling. This utility new type has simple structure, for a sow adjust temperature, cooling or heat preservation effect is good, the sow and piglet not easy to sick, which ensures healthy growth of sow and piglet.
NOVELTY - Special fertilizer comprises 2-6 pts. wt. potassium chloride, 8-12 pts. wt. oil cake, 12-20 pts. wt. urea, 4-10 pts. wt. fermentation microorganisms, 2-6 pts. wt. calcium carbonate, 4-8 pts. wt. monoammonium phosphate, 1-3 pts. wt. calcium sulfate, 2-6 pts. wt. potassium dihydrogen phosphate and 1-6 pts. wt. zinc sulfate.    USE - As special fertilizer for watermelon (claimed). The fertilizer is useful for promoting growth of watermelon.    ADVANTAGE - The fertilizer enhances taste and increases yield of the watermelons.
NOVELTY - Processing mixed plant waste involves (a) grinding plant waste using a grinder, stirring ground mixture, and filtering dried mixture using a filter, (b) disinfecting obtained granules, drying disinfected granules to obtain mixed plant granules, (c) adding wheat bran, fertilizer, urea, rapeseed meal, and clay to the mixed plant granules, stirring the mixture, adding sodium alginate solution to mixture, stirring the mixture to obtain culture substrate for mushroom, and (4) drying mushroom culture substrate, and adding wheat bran, fertilizer, urea, rapeseed meal, and clay.    USE - The method is useful for processing mixed plant waste. The plants include silver grass, bamboo, and switchgrass (all claimed).    ADVANTAGE - The method turns waste into treasure, saves resources, and is cost-effective.    DETAILED DESCRIPTION - Processing mixed plant waste involves (a) grinding the plant waste using a grinder, stirring the ground mixture, placing the stirred mixture in a cool place, drying the cooled mixture naturally until the moisture content reaches 10-15%, and filtering the dried mixture using a filter of particle size of 0.5-0.6 mm, (b) disinfecting the obtained granules at a temperature of 130-150 degrees C by placing the granules in a glasshouse, drying the disinfected granules for 10-15 minutes to obtain mixed plant granules, (c) adding 10-14 wt.% wheat bran, 1.5-3 wt.% fertilizer, 1-1.2 wt.% urea, 4-9 wt.% rapeseed meal, and 0.5-0.8 wt.% clay to the mixed plant granules, stirring the mixture, adding 60-75% sodium alginate solution to the mixture, stirring the mixture until the moisture content of the mixture reaches 20-30% to obtain culture substrate for mushroom, and (4) drying the mushroom culture substrate, and adding 35-40 wt.% wheat bran, 60-80 wt.% fertilizer, 120-130 wt.% urea, 150-160 wt.% rapeseed meal, and 70-85 wt.% clay.
NOVELTY - Synthesizing 3-(2-ethoxyphenoxy)-2-hydroxy-1-(4-nitrophenylcarbonyloxy)-3-phenylpropane (III), comprises reacting (2R,3S)-3-(2-ethoxyphenoxy)-3-phenylpropane-1,2-diol (I) and p-nitrobenzoyl chloride (II) at 15-45 degrees C in presence of dimethyl tin dichloride as a catalyst, and crushed and dried potassium carbonate or sodium carbonate as acid-binding agent in C3 halogenated or ethyl acetate as solvent.    USE - (III) is useful as reboxetine mesylate intermediate (claimed).    ADVANTAGE - The method: is simple and environmentally friendly; utilizes mild reaction conditions; consumes low energy; and is suitable for large-scale industrial production.    DETAILED DESCRIPTION - Synthesizing 3-(2-ethoxyphenoxy)-2-hydroxy-1-(4-nitrophenylcarbonyloxy)-3-phenylpropane of formula (III), comprises reacting (2R,3S)-3-(2-ethoxyphenoxy)-3-phenylpropane-1,2-diol of formula (I) and p-nitrobenzoyl chloride of formula (II) at 15-45 degrees C in presence of dimethyl tin dichloride as a catalyst, and crushed and dried potassium carbonate or sodium carbonate as acid-binding agent in C3 halogenated or ethyl acetate as solvent.
NOVELTY - Preparing ecabet sodium (I) comprises dehydrogenating (R)-7-isopropyl-1,4a-dimethyl-1,2,3,4,4a,9,10,10a-octahydro-phenanthrene-1-carboxylic acid (III) using fuming sulfuric acid to obtain (R)-7-isopropyl-1,4a-dimethyl-6-sulfo-1,2,3,4,4a,9,10,10a-octahydro-phenanthrene-1-carboxylic acid (II), and adding (II) with sodium salt agent in an aqueous solvent and then reacting to obtain ((8R)-8-carboxy-2-isopropyl-4b,8-dimethyl-5,6,7,8a,9,10-hexahydrophenanthren-3-yl)sulfonyloxysodium (III).    USE - The process is useful for preparing ecabet sodium (claimed).    ADVANTAGE - The process is capable of preparing ecabet sodium with high yield and selectivity in simple, safe and environmentally-friendly manner.    DETAILED DESCRIPTION - Preparing ecabet sodium (I) comprises dehydrogenating (R)-7-isopropyl-1,4a-dimethyl-1,2,3,4,4a,9,10,10a-octahydro-phenanthrene-1-carboxylic acid of formula (III) using fuming sulfuric acid to obtain (R)-7-isopropyl-1,4a-dimethyl-6-sulfo-1,2,3,4,4a,9,10,10a-octahydro-phenanthrene-1-carboxylic acid of formula (II), and adding (II) with sodium salt agent in an aqueous solvent and then reacting to obtain ((8R)-8-carboxy-2-isopropyl-4b,8-dimethyl-5,6,7,8a,9,10-hexahydrophenanthren-3-yl)sulfonyloxysodium of formula (III).
NOVELTY - Preparing N-formylphenothiazine comprises adding formic acid and phosphorus pentachloride into a reaction container, grinding to uniformity, adding phenothiazine, grinding continuously and reacting to obtain product, placing statically, filtering, washing the filter cake, drying, and re-crystallizing, where the molar ratio of formic acid, phosphorus pentachloride and phenothiazine is (1-1.2):(1-1.2):1.    USE - The method is useful for preparing N-formylphenothiazine (claimed).    ADVANTAGE - The method: utilizes solid-phase solvent-free synthesis method, realizes direct grinding of reactants, and ensures mild reaction conditions in short time; is simple, safe, economical and environmentally friendly, utilizes simple device and has convenient operation; and produces more than 95% product yield.
NOVELTY - Method for preparing organic fertilizer, involves mixing biogas residue and chopped straw, performing solid-liquid separation, stirring, adding ash or lime, performing secondary fermentation, obtaining fermentation product, mixing the fermentation product with activated carbon and binder and drying to obtain product.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The method prepares fertilizer which does not contain any chemicals, increases yield and quality of crops and improves soil, utilizes the agricultural waste and reduces greenhouse gas emission.
NOVELTY - Bio-organic fertilizer comprises 15-20 pts. wt. chicken manure, 10-15 pts. wt. dairy manure, 20-30 pts. wt. pig manure, 4-6 pts. wt. Prunella vulgaris leaves, 6-8 pts. wt. plant straw, 3-5 pts. wt. edible leftovers, 4-6 pts. wt. slaughtered animal waste, 20-30 pts. wt. water and 3-5 pts. wt. yeast.    USE - The bio-organic fertilizer is useful for promoting plant growth.    ADVANTAGE - The fertilizer does not cause pollution, and enables rapid absorption of nutrients by plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the bio-organic fertilizer, which involves (a) mixing the chicken manure, dairy manure, pig manure, P.vulgaris leaves, plant straw, edible leftovers, slaughtered animal waste, water and yeast to obtain mixture, (b) fermenting the mixture at 30-40 degrees C for 1-3 days, and (c) drying and sterilizing fermented product for 2-4 days, and granulating obtained product.
NOVELTY - The device has a pre-processing unit that is connected with a stir straw crushing device (1). A raw material transmitting device is connected with high temperature processing unit. A storage drying device is connected with a biological fertilizer processing unit. A pre-processing unit is connected with grab bucket device (5) and slag pumping pump. A spraying device is connected to upper portion of fermentation groove. The biological fertilizer processing unit is connected with solar energy plate and solar energy hot water circulation pipeline.    USE - Device for preparing biological medical fertilizer.    ADVANTAGE - The biological fertilizer processing unit is connected with solar energy plate and solar energy hot water circulation pipeline, thus the processing efficiency for preparing medical fertilizer is improved. The energy consumption and transport cost for preparing medical fertilizer is reduced. The fermentation efficiency for preparing medical fertilizer is increased. Stable operation for preparing medical fertilizer is ensured. The generation of the agricultural waste and pollution during preparing the medical fertilizer is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the structure of the device for preparing biological medical fertilizer.    Stir straw crushing device (1)    Straw (2)    Animal mix stir box (3)    Raw material preparing tank (4)    Grab bucket device (5)
NOVELTY - Synthesizing glycidyl methacrylate comprises: mixing methacrylic acid with modified acidic zeolite socony mobil-5 (ZSM-5) as a catalyst, and reacting the mixture in the presence of a polymerization inhibitor and then performing a ring-opening esterification process with an addition of epichlorohydrin to obtain 3-chloro-2-hydroxy propyl methacrylate; and mixing 3-chloro-2-hydroxy propyl methacrylate with aqueous sodium hydroxide and then performing a ring closure reaction with an addition of epichlorohydrin and dehydrochlorination process to obtain glycidyl methacrylate.    USE - The method is useful for synthesizing glycidyl methacrylate (claimed).    ADVANTAGE - The method is capable of preparing glycidyl methacrylate in a cost-effective and eco-friendly manner with increased yield of 90-96%.
NOVELTY - Cultivating earthworm, comprises sorting impurities including organic domestic waste, sludge, slag or plant straw, and livestock manure, mixing impurities and crushing, adding earthworm to the obtained mixture in a ridge, expanding ridge width to 8 m, forming 5 m wide earthworm cultivation, then separating earthworm and earthworm manure, passing the manure into two channels through a sieve and then sorting the manure, to obtain pure earthworm manure.    USE - The method is useful for cultivating earthworm, which is useful for preparing organic fertilizer, and as a bait for breeding turtle and fish (claimed).    ADVANTAGE - The method cultivates the earthworm in an eco-friendly manner.    DETAILED DESCRIPTION - Cultivation of earthworm, comprises sorting impurities including 30-50 wt.% of organic domestic waste, 20-40 wt.% of sludge, 5-15 wt.% of slag or plant straw, and 10-30 wt.% of livestock manure, mixing impurities and crushing to reach carbon/nitrogen mass ratio of 25-30%, reducing water content to 50-60%, where the crushed material has a pH value of 6.5-7.5 and a grain diameter of 2-3 cm, adding 1 kg of earthworm having a width of 1.5-2 m and a height of 60 cm to the obtained mixture in a ridge, adding earthworm with a thickness of 10-15 cm for every 10-15 days in the mixture, and stirring for more than 15 times, expanding width of the ridge to 8 m, forming earthworm with 5 m wide, then separating earthworm and earthworm manure, passing the manure into two channels through a sieve and then sorting the manure, to obtain pure earthworm manure.
NOVELTY - The furnace has a furnace body whose lower part is provided with an air supply pipe. An inner part of the furnace body is provided with a deflector rod. A lower part of the deflector rod is provided with a combustion disk. A lower end of the combustion disk is matched with an ash outlet that is formed at an upper end of the furnace body. An inner side lower part of the furnace body is provided with an annular air tube. An outer side of the annular air tube is connected with a connecting pipe. An upper part of the combustion disk is formed with a round hole.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace is energy-saving and environment-friendly, and has a compact structure, high reliability, better adaptability, large quantity, wide range of applications and stable temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasification furnace.
NOVELTY - Preparation of wet thermal biological carbon using organic agriculture and forestry solid waste as raw material by cleaning impurities of raw material using deionized water, drying, pulverizing, sieving; preparing zinc chloride solution; mixing extracts and zinc chloride solution, standing, filtering, absorbing surface water; putting in tube-type atmosphere furnace, with nitrogen as protective gas, three-stage heating cracking; and cooling to room temperature, passing through sieve, washing with deionized water repeatedly until weight is constant, and calculating yield.    USE - Method for preparing wet thermal biological carbon using organic agriculture and forestry solid waste (claimed).    ADVANTAGE - The method is simple, ensures high yield, increases production and reduces production cost. The biological carbon has good absorbing property.    DETAILED DESCRIPTION - Preparation of wet thermal biological carbon using organic agriculture and forestry solid waste as raw material comprises:    (A) cleaning impurities and sand of agricultural organic solid waste raw material using deionized water, naturally drying, pulverizing, sieving through 60 meshes sieve;    (B) weighing zinc chloride reagent, dissolving in deionized water to prepare zinc chloride solution;    (C) mixing extracts of first step and zinc chloride solution, standing for 24 hours, filtering using quantitative filter paper, absorbing surface water using water-absorbing paper;    (D) putting in tube-type atmosphere furnace, with nitrogen as protective gas, three-stage heating cracking at 200 degrees C, 350 degrees C and 40 degrees C for 2 hours; and    (E) cooling to room temperature, passing through 200 meshes sieve, washing with deionized water repeatedly until weight is constant, and calculating yield.
NOVELTY - A photocatalytic hydrogen production electrode material is prepared by taking titanium or titanium alloy substrate as anode and graphite or platinum sheet as cathode, performing anodic oxidation in 0.2-0.7 wt.% hydrofluoric acid aqueous solution at 10-30 V for 20-40 minutes to prepare titanium oxide nanotube array; soaking the titanium oxide nanotube array into 0.1-2 mol/L silver nitrate (AgNO3) aqueous solution for 5-10 minutes, flushing with distilled water, and drying; and heat treating the titanium oxide nanotube array at 450-550 degrees C in air atmosphere for 60-240 minutes.    USE - Method for preparing photocatalytic hydrogen production electrode material.    ADVANTAGE - The method has simple operation and low cost. The obtained electrode material can achieve high photocatalytic efficiency.    DETAILED DESCRIPTION - Preparation of photocatalytic hydrogen production electrode material comprises:    (A) preparing titanium oxide nanotube array by taking titanium or titanium alloy substrate as anode and graphite or platinum sheet as cathode, performing anodic oxidation in 0.2-0.7 wt.% hydrofluoric acid aqueous solution at 10-30 V for 20-40 minutes, taking the substrate out, using distilled water to clean, and drying at room temperature;    (B) dissolving AgNO3 in distilled water to prepare 0.1-2 mol/L AgNO3 solution;    (C) soaking the prepared titanium oxide nanotube array into the AgNO3 solution for 5-10 minutes, taking out, flushing with distilled water, and drying at room temperature; and    (D) sending the titanium oxide nanotube array to a muffle furnace, performing heat treatment at 450-550 degrees C in air atmosphere for 60-240 minutes and then cooling to obtain the electrode material.
NOVELTY - The system has a fuel gas dispersion chamber for distributing and supplying fuel to a set of fuel cells of a fuel cell module. The fuel cells are affixed in an airtight manner by using ceramic adhesive to an affixing unit constituting the fuel gas dispersion chamber and a gas leak suppression portion that suppresses occurrence of cracks caused by shrinkage when the ceramic adhesive is formed around the periphery of the fuel cells by a layer of the ceramic adhesive. A plate covers a part of the ceramic adhesive.    USE - Solid oxide fuel cell system for electricity generation applications.    ADVANTAGE - The system allows ceramic adhesive pools that can be formed on surrounding portions of the fuel cells using a simple structure, thus forming the gas leak suppression portion in a reliable manner. The gas leak suppression portion is formed by using ceramic adhesive around the fuel cells, so that leakage of fuel gas can be reliably suppressed in parts surrounding the fuel cells when gas leakage is most likely to occur and effects of leakage are most serious. The system has a ceramic adhesive layer that is thicker, so that cracks in the ceramic adhesive layer can be reliably suppressed in area surrounding the cell units and more reliable airtightness can be secured.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a housing container for fuel cells in a solid oxide fuel cell system.    Fuel cell housing container (8)    Exhaust collection chamber (18)    Ignition heater (62)    Inside cylindrical unit (64)    External cylindrical unit (66)    Inside cylindrical container (68)
NOVELTY - The method involves inserting an end portion of each fuel cell of multiple fuel cells (16) into respective insertion holes formed in an affixing element. The end portion of each fuel cell inserted into each insertion hole is positioned relative to a fuel cell module (2). Another end portion of each fuel cell is positioned at a predetermined position relative to the fuel cell module. Ceramic adhesive is applied onto the affixing element into which each fuel cell is inserted. The applied ceramic adhesive is hardened. Each fuel cell is affixed to the affixing element.    USE - Method for manufacturing a SOFC apparatus.    ADVANTAGE - The method enables preventing peeling away of an earlier-drying part of the ceramic adhesive from a part which dries and shrinks later, thus suppressing occurrence of cracking. The method enables avoiding risk of reduction in emission performance or abnormal combustion due to airtightness defects in exhaust collection chamber. The method enables performing solvent removal and hardening step in one iteration on ceramic adhesive hardened in multiple locations, thus improving manufacturing efficiency of the SOFC apparatus.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a manufacturing apparatus for a solid oxide fuel cell (SOFC) apparatus    (2) a SOFC apparatus for generating electricity by supplying fuel and oxidant gas to fuel cells housed in a fuel cell module.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a SOFC.    Fuel cell module (2)    Fuel cells (16)    Fuel supply source (30)    Fuel blower (38)    Air supply source (40)
NOVELTY - The instrument (1) has an anode plate and a cathode plate integrated in an insulation state. An electrolysis board (3) is fixed at an inner side of a desired drink container that stores drinking water. The anode plate and the cathode plate are arranged parallel with respect to a bottom face of the drink container. The anode plate and the cathode plate are formed with multiple through-holes (3a). The electrolysis board is provided with an insulating peripheral shielding part (34), which is arranged between the anode plate and the cathode plate.    USE - Portable hydrogen water generator instrument i.e. drinks stirrer, for generating hydrogenous water from drinking water.    ADVANTAGE - The electrolysis board is fixed at the inner side of the desired drink container that stores drinking water so as to generate the hydrogenous water in an easy manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a portable hydrogen water generator instrument.    Portable hydrogen water generator instrument (1)    Electrolysis board (3)    Through-holes (3a)    Insulating peripheral shielding part (34)    Waterproof housing (43)
NOVELTY - The semiconductor cathode (01) has light-active surface areas (04) and dark-active surface areas (05) that are provided, so as to form ohmic contacts with metallic co-catalyst particles (07). The co-catalyst particles are changed by a deformation of atomic structure in the form of stretched or compressed bond lengths or rotated bond angles. The atomic structure of co-catalyst particles is adjusted to the atomic structure of the dark-active surface areas catalytically, so that a voltage application (08) is provided.    USE - Three-dimensionally structured semiconductor cathode for hydrogen production.    ADVANTAGE - Since the co-catalyst particles are changed by a deformation of atomic structure in the form of stretched or compressed bond lengths or rotated bond angles, the yield of three-dimensionally structured semiconductor cathode is improved even at low applied voltage. Thus, the efficiency of hydrogen production is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing three-dimensionally structured semiconductor cathode.    DESCRIPTION OF DRAWING(S) - The drawings show the schematic views of the three-dimensionally structured semiconductor cathode.    Three-dimensionally structured semiconductor cathode (01)    Light-active surface areas (04)    Dark-active surface areas (05)    Metallic co-catalyst particles (07)    Voltage application (08)
NOVELTY - Operating a bioreactor (1) comprising hydrogenotrophic methane bacteria, which produces methane from carbon dioxide and hydrogen, in an aqueous solution (2), and a gas chamber (6), comprises introducing hydrogen without bubbles into the aqueous solution by at least one feed element (8), and controlling the amount of introduced hydrogen over hydrogen concentration in the gas chamber. The amount of introduced hydrogen is reduced, when the measured hydrogen concentration in the gas chamber exceeds a predetermined limit.    USE - The method is useful for operating a bioreactor.    ADVANTAGE - The method ensures conversion of large amount of introduced hydrogen into methane by methane bacteria for avoiding the presence of excess hydrogen gas in the gas chamber, and thus it reduces the risk of explosion.    DETAILED DESCRIPTION - Operating a bioreactor (1) comprising hydrogenotrophic methane bacteria, which produces methane from carbon dioxide and hydrogen, in an aqueous solution (2), and a gas chamber (6), comprises introducing hydrogen without bubbles into the aqueous solution by at least one feed element (8), and controlling the amount of introduced hydrogen over hydrogen concentration in the gas chamber. The amount of introduced hydrogen is reduced, when the measured hydrogen concentration in the gas chamber exceeds a predetermined limit. Hydrogen is introduced in the aqueous solution in such an amount that the molar ratio of hydrogen supply to carbon dioxide supply in the aqueous solution is 0.1-4.8. An INDEPENDENT CLAIM is also included for the bioreactor comprising at least one feed element, a sensor (22) for measuring the hydrogen concentration in the gas chamber, and an electrical controller for carrying out the above mentioned method.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the bioreactor.    Bioreactor (1)    Aqueous solution (2)    Gas chamber (6)    Feed element (8)    Sensor (22)
NOVELTY - The system (100) has an oxidizer for supplying an oxidant stream to a cathode side (106) of a fuel cell unit (102). A cathode exhaust passage is provided for discharging cathode exhaust gas from the cathode side of the fuel cell unit. Two or more fuel cell devices (102a,102b) are coupled to each other or coupled by an anode exhaust gas guide portion (110a) of the fuel cell device (102a). The anode exhaust gas produced in the fuel cell device (102a) is supplied through a fuel feed portion (108b) to other fuel cell device (102b) as a fuel stream of the fuel cell device (102b).    USE - Fuel cell system used in airplane, for the provision of electrical power.    ADVANTAGE - The fuel cell system is operated efficiently and safely. The fuel cell system is utilized efficiently in closed spaces. The damage of the fuel cell system is avoided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for operating a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system.    Fuel cell system (100)    Fuel cell unit (102)    Fuel cell devices (102a,102b)    Cathode side (106)    Fuel feed portion (108b)    Anode exhaust gas guide portion (110a)
NOVELTY - Transparent, electrically semi-conductive plate-shaped interference pigment comprises a layer made of titanium dioxide (I).    USE - The transparent, electrically semi-conductive plate-shaped interference pigment is useful in paints, coatings, printing inks, plastics, sensors, security applications, floor coverings, textiles, films, ceramics, glasses, paper, for laser marking, in thermal protection, as photo semiconductor, in pigmented formulations, pigment preparations and dry preparations, and in security products, which are exposed to the influence of an electromagnetic field, where the interference pigments are used with organic and/or inorganic coloring agents, electrically conductive materials and/or electrically non-conductive effect pigments in the mixture (all claimed).    ADVANTAGE - The plate-shaped interference pigment: exhibits high color strength, high electrical conductivity and low self-absorption; and is produced in a simple manner.    DETAILED DESCRIPTION - Transparent, electrically semi-conductive plate-shaped interference pigment comprises a layer made of titanium dioxide of formula (Ti02-x) (I).    x = 0.001-0.05.    INDEPENDENT CLAIMS are also included for:    (1) producing the interference pigment, comprising thermally treating the transparent plate-shaped interference pigment made of titanium dioxide or the coated transparent, plate shaped support comprising layer made of titanium dioxide on the outer surface in a gas phase with addition of a reducing gas for a period of 5-60 minutes, where the titanium dioxide is converted to (I); and    (2) a security product comprising the interference pigments.
NOVELTY - A mixed waste fermentation biogas slurry formulation comprises: raw material A: straw and bagasse (single or mixed available): 60-85%; raw material B: rice bran, peanut shells, cassava alcohol waste water, bran and whole wheat flour: 15-40%; where the materials can be in dry and wet basis.    USE - A mixed waste fermentation biogas slurry formulation (claimed).    ADVANTAGE - The whole process has no waste water discharge, and can change the waste into valuable resource, and produces clean energy and efficient organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for no biogas production of mixed fermented waste slurry formulations and no biogas, which involves: (1) uniformly mixing raw material A and raw material B into a hydrolysis tank, converting to an organic acid; (2) continuously pumping into biogas fermenter the raw materials from hydrolysis tank, fermentation to produce biogas; (3) after a certain time of fermentation, separation of biogas from the fermentation tank to release some of the solid-liquid, the solid part without dehydration can be directly used as organic fertilizer, liquid portion is recycled to be used in hydrolysis tank for hydrolysis of the ingredients.
NOVELTY - This new type utility claims one vehicle type straw with a self-heating carbonizing integral device, by large truck, a small crusher, spiral inner external multi-tube furnace, the raw material storage hopper, a feeder, a discharging hopper, a generator set. Carbonization is by multi-group of a high temperature resistant stainless steel tube is composed of external furnace body. Said external furnace upper end surface feeding port and the feeder are connected, forming a feeding channel, and the side surface of the discharge hole set with a discharging hopper, the discharging hopper and the discharging port of external-heat carbonization furnace and a connecting cavity with the external-heat carbonization furnace inner connected, forming the discharge channel, said external furnace is multi-stage connected of inner spiral tube shaped structure, said external carbonizing furnace comprise chain wheel transmission device, a furnace body, a multi-parallel distribute conveying auger, a power device and an ignition port. This utility new type treatment efficiency high, carbonization produce a gas of all recovery without pollution.
NOVELTY - This utility new type relates to one a circular type integrated hydrolysis acidification device. This utility new type aims to provide one of a circular type integrated hydrolysis acidification device, low investment and land use area without increasing a front, the hydrolysis acidification effect of stable, reduces the subsequent operation maintenance working quantity. This utility new type of technology solution is as follows: a circular type integrated one hydrolysis acidification device, wherein the device is a circular tank body, the tank body is set in one channel is provided with uniform water distribution hole of circular wall of the pond body is divided into the outside of annular channel and in a radial-flow type sedimentation tank, set with a plurality of low speed submersible water impeller at the bottom of the annular groove, the annular groove is connected with outer wall of the sewage water inlet tube, the inner side of circular wall building with a water outlet weir and set to external of the supernatant water tube, a radial-flow settling basin of center is sedimentation tank bucket, the mud bucket by sludge reflux tube connected on mud collecting well of annular channel. This utility new type is suitable for sewage treatment plant.
NOVELTY - Wood tar extracting box comprises front edge explosion-proof port located at top part of metal body, and a flue gas discharge port. The explosion-proof port is set at the middle part of pressure relief movable metal interlayer door body. The two sides of the explosion-proof port are set with two viewing ports. The lower part of the door body is set with two ignition ports from left and right side. The box body inner wall is a metal steel top and metal keel composed of red brick and earth ramming mixed insulating structure. The inner interlayer door body is filled with an insulating filler.    USE - Used as a wood tar extracting box.    DETAILED DESCRIPTION - Wood tar extracting box comprises front edge explosion-proof port located at top part of metal body, and a flue gas discharge port. The explosion-proof port is set at the middle part of pressure relief movable metal interlayer door body. The two sides of the explosion-proof port are set with two viewing ports. The lower part of the door body is set with two ignition ports from left and right side. The box body inner wall is a metal steel top and metal keel composed of red brick and earth ramming mixed insulating structure. The inner interlayer door body is filled with an insulating filler comprising structure of 2 m width, ladder of 2 m height, a side ladder of 1.2 m, and 0.6 m ladder edge of door body.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the wood tar extracting box.
NOVELTY - Microbial fertilizer comprises 15-23 wt.% urea, 15-18 wt.% ammonium phosphate, 20-30 wt.% potassium sulfate, 30-45 wt.% organic fertilizer, 0.3-0.5 wt.% microbial spore powder, 0.05-0.1 wt.% trace element and 0.005-0.01 wt.% modifier.    USE - As microbial fertilizer for Chinese goosebeery (claimed).    ADVANTAGE - The fertilizer improves the utilization of fertilizer, thus reducing the amount of fertilizer; and solves problem of soil compaction and accumulation of nitrates and heavy metals that increases environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of microbial fertilizer involving mixing 15-23 wt.% urea, 15-18 wt.% ammonium phosphate, 20-30 wt.% potassium sulfate, 30-45 wt.% organic fertilizer, 0.3-0.5 wt.% microbial spore powder, 0.05-0.1 wt.% trace element and 0.005-0.01 wt.% modifier to form mixture; heating the mixture to 40-70 degrees C and converting into granule, drying, cooling, and coating the granule with coating material containing to form microbial fertilizer.
NOVELTY - Manufacture of integrated biomass particles involves drying timber wood using combustion gas, heat-drying such that spontaneous combustion does not occur, processing dried material such that ignition temperature of resultant material is 220 degrees C or more, compressing resultant material and increasing the water-repellent property of compressed material.    USE - Manufacture of integrated biomass particles (claimed).    ADVANTAGE - The method enables efficient manufacture of integrated biomass particles having excellent water resistance with reduced energy consumption.
NOVELTY - Solanaceous vegetable special organic fertilizer comprises 30-45 pts. wt. plant ash extract, 40-50 pts. wt. phytase hydrolyzate, 10-25 pts. wt. protease hydrolyzate and 0.04-0.08 pt. wt. preservative. Phytase hydrolyzate is wheat germ prepared by decomposing organic phosphoric compound at 53-63 degrees C and solid-liquid separating. Protease hydrolyzate is prepared by taking separated solid and decomposing at 30-55 degrees C.    USE - Solanaceous vegetable special organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of solanaceous vegetable special organic fertilizer comprising    (A) taking plant ash, adding water, stirring and filtering;    (B) taking wheat germ, adding water, boiling for 10-20 minutes, cooling, adjusting pH to 4.8-5.2, adding phytase, stirring at 53-63 degrees C for 1.5-3 hours and filtering;    (C) taking enzyme, adding, water, adjusting pH to 6.5-7.5, adding neutral protease, stirring at 30-55 degrees C for 2-5 minutes and filtering; and    (D) mixing extracts, adding preservative, adjusting pH to 6-6.5, mixing and filtering.
NOVELTY - Fertilizer synergistic agent comprises 100-500 pts. wt. powder of manure and dairy manure, 500-1000 pts. wt. corn straw and tobacco straw, 20-80 pts. wt. perlite, 50-100 pts. wt. vermiculite, 50-100 pts. wt. zeolite powder, 100-500 pts. wt. peat, 20-80 pts. wt. polyaspartate, and 30-80 pts. wt. chitosan.    USE - The fertilizer synergistic agent is useful for nursery or greenhouse vegetable cultivation.    ADVANTAGE - The fertilizer synergistic agent has good ion exchange and metal ion adsorption properties and good stability and increased resistance to biological toxicity and oxidation, effectively prevents soil compaction, improves soil structure, and increases fertilizer effect time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer synergistic agent comprising air-drying corn straw and tobacco straw and then grinding to obtain straw powder having a size of 3-5 cm, adding powder of manure and dairy manure and peat to the straw powder and then grinding to obtain a mixture having a size of 2-3 cm, fermenting the mixture at 40-50 degrees C 5-7 days to reduce the water content to 50-60 wt.%, adding 5-ethyl-4-methoxy-2-phenylquinoline to the fermented mixture and then drying at 30-40 degrees C, and adding zeolite powder, perlite, vermiculite, polyaspartate and chitosan to the mixture and then stirring.
NOVELTY - Sandy soil improvement fertilizer comprises 2-4 pts. wt. quick-release organic fertilizer, 2-4 pts. wt. plant matter organic fertilizer and 3-5 pts. wt. water-nutrient fertilizer. Quick-release organic fertilizer is chicken manure, duck manure and/or pig manure. Plant matter organic fertilizer is crop straw and livestock excrement. Water-nutrient fertilizer is coconut husk and/or grass peat.    USE - Sandy soil improvement fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of sandy soil improvement fertilizer comprising taking raw materials, mixing, adding water and microbial fertilizer, piling, stacking, mixing, fermenting for 10-50 days and mixing.
NOVELTY - Improved biodiesel oil comprises biodiesel oil and direct coal liquefied diesel oil, where the direct coal liquefied diesel oil accounts for 5-20% of the total volume of biodiesel.    USE - Used as an improved biodiesel oil.    ADVANTAGE - The oil exhibits low temperature fluidity. The method is simple and quick, has high feasibility, and solves the problem that the current biodiesel oil has poor fluidity at low temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing improved biodiesel oil comprising dissolving biodiesel oil and coal direct liquefied diesel oil, and mixing to obtain mixed liquid, allowing it to stand to obtain improved biodiesel oil, where the coal direct liquefied diesel oil accounts for 5-20% of the total volume of improved biodiesel oil.
NOVELTY - This utility new type claims a one landscape sewage treatment device, comprise: water floating block, a fixed , biological film belt and the aeration disk, a fixed network by a crossed metal bar into a network-shaped, said fixed network a fixed mounting the landscape water tank bottom part, a water surface floating blocks floating on the water surface of a landscape water pool, a water surface floating a landscape planting flower, a biological membrane with a water surface floating and fixing said , said aeration set connected with a gas-transmitting soft tube the landscape water, said aeration, gas-transmitting soft tube through a binding through fixed connecting . This utility new type combination through biological film belt and aerating, the whole landscape sewage treatment device is simple structure, a biological membrane belt can develop microorganism, microorganism for landscape water through inner of a pollutant absorbing and decomposing to recover landscape water body ecological balance and for purification.
NOVELTY - This utility new type provide the one can treat a waste pneuma of sewage, it will not cause waste pneuma leakage, it is more environment-friendly of biological trickling filter. It comprise drop, wherein dropping chamber inlet connect with a pneuma liquid separator, a gas-liquid separator set with sewage inlet, exit and sewage exit foul smell, a gas-liquid separator main body is a cylinder structure lower part with taper-shaped guide flow member is a tapered guide from upper to lower, and the diameter gradually reduced, sewage exit and the chamber is connected with the inlet, exit connecting with foul smell foul smell treatment room, inner foul smell treatment room fill with foul smell absorbing filler, foul smell and exit a room between the foul smell in turn pneuma table and connected with a gate valve, gas is accumulated amount reaches the preset value to output alarm signal of intelligent gas meter, pneuma table electrically connecting with an acousto-optic alarm, a foul smell treatment room through fast joint with the foul smell pipeline.
NOVELTY - This utility new type refers to a mix structure one three-dimensional environment-friendly fermenting system, include a multi-used for conveying conveyor, a ventilation device, a dust removing device, and c, fermenting room, feeding device, clinker conveyor of fermented material, the further comprise three-dimensional layering of concrete frame structure, wherein the concrete structure construction in one frame a sealed fermentation chamber, or the concrete structure around a seal directly with the fermentation room form. the concrete structure comprise a multi-row lengthways upright post and a multi-beam, between each two rows of lengthways upright post form a mounting channel, each two rows of front, rear two strip lengthways between the upright post set with the beam, the conveyor mounting in the mounting channel inner and the support on the machine frame upper beam. This utility new type mix structure of vertical type environment-friendly fermenting system manufacturing cost is low, the use life and operation stability is higher, more use safety.
NOVELTY - This utility new type claims a one greenhouse vegetable seedling matrix, include cotton pole carbon layer, vermiculite layer, cattle and sheep excrement layer, carbon layer. This utility new type a matrix of volume is 0.2-0.7g/cm3, aperture ratio is 1: 1.8-3.9. The utility model is new type of material has wide raw material source, simple operation, rational structure, high air permeability, water, nutrient of enough. it is suitable for the technical field of plant cultivation.
NOVELTY - The system has three level systems that are in a fluidized bed pyrolysis furnace (1). Secondary system waste heat boiler is set to cool the bio-oil to flow into the high temperature flue gas generated by internal combustion engine. High-temperature flue gas heat recovery systems are used for organic Rankine cycle power generation in low-temperature flue gas generated in drying cycle of biomass feedstock. Three systems are used to produce combustible gas materials, after preheating backwater discharge and remaining flue gas is heated to backwater.    USE - System for generating distributed biomass and organic Rankine cycle.    ADVANTAGE - The distributed biomass and organic Rankine cycle can be generated with simple process, so that biomass energy maximum use is obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the distributed biomass and organic Rankine cycle generation system. (Drawing includes non-English language text)    Fluidized bed pyrolysis furnace (1)    High temperature cyclone separator (2)    High temperature electric dust catcher (3)    Waste heat boiler furnace (4)    Steam turbine (5)
NOVELTY - This utility new type inner claims a one organic matter solid bulk fermentation and sterilization integrative device, fermenting room and sterilizing room mounting there are multiple layers, each layer multi-group of temperature, pressure, CO2 and NH3 sensor, inner fermentation room at intervals distance arrangement of mounting the shell set with a one of a or multi-air inlet and a blanking control device I and a one or multi-air inlet and a blanking control device II, the bottom room for mounting with a discharging device, the discharging device distribute the feeding spiral roller B of the discharging spiral roller B with a rotating end, a feeding spiral roller B rotate reversely, the outer wall of a room with a U-type steam sterilizing channel; the steam interlayer channel quantity electromagnetic valve A through a high temperature steam source, through electromagnetic valve B a pneuma source quantity of different end. It can finish organic solid bulk fermentation and sterilizing process in this utility new type inner, fermenting time short, a high efficiency, a low cost, stable and reliable quality, save a lot of aritificial, small floor space and transportation device, eliminate the environment pollution.
NOVELTY - This utility new type claims a one organic matter solid bulk ferment sterilizing integrated device, inner room and sterilizing room for mounting there are multiple layers, each layer multi-group of temperature, pressure, CO2 and NH3 sensor, mounting a space distance arrangement of the shell set with a one of a or multi-air inlet and a blanking control device for inner room, sterilizing room mounting with a discharging device, the discharging device distribute the feeding spiral roller B of the discharging spiral roller B with a rotating end, a feeding spiral roller B rotate reversely, the outer wall of a room with a U-type steam sterilizing channel; the steam interlayer channel quantity electromagnetic valve A through a high temperature steam source, through electromagnetic valve B a pneuma source quantity of different end. It can finish organic solid bulk fermentation and sterilizing process in this utility new type inner, fermenting time short, a high efficiency, a low cost, stable and reliable quality, save a lot of aritificial, small floor space and transportation device, eliminate the environment pollution.
NOVELTY - This new type utility claims one a solid bulk fermentation organic substance and sterilizing device, inner room and sterilizing room for mounting there are multiple layers, each layer multi-group of temperature, pressure, CO2 and NH3 sensor, mounting a space distance arrangement of the shell set with a one of a or multi-air inlet and a blanking control device inner fermentation room, sterilizing room mounting with a discharging device, the discharging device distribute the feeding spiral roller with a rotating discharging spiral roller of the same end, different end a reverse rotation, and an outer wall of a room with a U-type steam sterilizing channel; the steam interlayer channel quantity electromagnetic valve A through a high temperature steam source, quantity electromagnetic valve B through a pneuma source. It can finish organic solid bulk fermentation and sterilizing process in this utility new type inner, fermenting time short, a high efficiency, a low cost, stable and reliable quality, save a lot of aritificial, small floor space and transportation device, eliminate the environment pollution.
NOVELTY - This utility new type relates to the technology field of polluted water, claims for improving pollution of water purification device, include cross-shaped floating component (1), a solar panel (4), an air compressor (3) and aeration tube group (2). The air compressor (3) is set on the cross-shaped floating component (1) centre position. Floating cross component (1) comprise a four floating plate (11), adjacent floating plate (11) set with the solar panel (4). Inner floating plate (11) set with aeration tube connecting hole (12), an aeration tube connecting hole (12) fixed one end of filling, filling the other end connecting with an aeration tube group (2). This utility new type cross floating module lower side through suspended filler aeration tube group to make the process self-purification whole river in aerobic state, the valid improve, beneficial effects of pollution degree of water body, solves the problem that the existing technology in the technology problem of anoxic or anaerobic river.
NOVELTY - A bromoxynil is synthesized by adding 15-16 pts. wt. phosphorus oxychloride, 20-21 pts. wt. 4-bromo-benzoic acid, and 2500-3500 pts. wt. 1,1-diphenylethane in reactor, stirring to mix, purging with ammonia at less than or equal to 60 degrees C until solution is alkaline, purging with nitrogen gas, slowly heating at 260-270 degrees C for 55-65 minutes, cooling, filtering at 8-12 degrees C, separating organic solvent layer and insoluble inorganic chemical, pre-heating insoluble inorganic chemical at 100 degrees C, washing 60 pts. wt. 1,1-diphenylethane, and combining organic solvent layer and washing solution.    USE - Synthesis of bromoxynil (claimed).    ADVANTAGE - Synthesis process is simple, safe, reliable, and environment-friendly. Product has high purity.    DETAILED DESCRIPTION - A bromoxynil is synthesized by adding 15-16 pts. wt. phosphorus oxychloride, 20-21 pts. wt. 4-bromo-benzoic acid, and 2500-3500 pts. wt. 1,1-diphenylethane in reactor, stirring to mix, purging with ammonia at less than or equal to 60 degrees C until solution is alkaline, purging with nitrogen gas, slowly heating at 260-270 degrees C for 55-65 minutes, cooling, filtering at 8-12 degrees C, separating organic solvent layer and insoluble inorganic chemical, pre-heating insoluble inorganic chemical at 100 degrees C, washing 60 pts. wt. 1,1-diphenylethane, combining organic solvent layer and washing solution, adding 60 pts. wt. water and 3.6 pts. wt. alkaline solution of sodium hydroxide, heating at 55-65 degrees C, stirring, performing liquid separation, washing organic layer with 30 pts. wt. water and 0.4 pt. wt. alkaline solution of sodium hydroxide, performing liquid separation, mixing alkaline solutions, adding 35% hydrochloric acid, reacting, packaging, and storing.
NOVELTY - This utility new type provide the a biomass gasification furnace with one of add material device, include storage hopper, feeding car, a guide rail, a material the gasification furnace top, one end of the lower part is a discharging opening, a guide rail mounting the two side gasification furnace top part of, said feeding car is placed in a guide rail, a guide rail two end each set with a guide wheel and a driven wheel, a guide wheel, a driven wheel and the feeding car with a steel wire rope, and the bottom of said feeding car are not seal. Rear continuously add material, stacking more than raw material biomass gasification furnace top feeding car pushes the biomass raw material, the biomass raw material uniform, fill in the gasification furnace, the biomass raw material in a gasification furnace uniform and steady of operation. This utility new type has simple operation, convenient use, strong continuity of add material, at the same time, it compared aritificial feeding mode, which can make uniform distribute inner biomass raw material in the gasification furnace.
NOVELTY - Preparing guaiacol involves: taking o-anisidine, sodium nitrite solution, sulfuric acid and water into diazotization kettle, reacting at 90-100 degrees C for 1.5-2 hours to form a diazonium solution; adding diazonium solution into hydrolysis kettle, and carried out hydrolysis in presence of copper sulfate and water, and then continuously distilling to obtain water and guaiacol mixture; subjecting the water and guaiacol mixture to separation kettle; separating crude guaiacol; continuously distilling obtained residue after removing crude finished guaiacol, and then packaging and storing.    USE - For preparing guaiacol (claimed) which is used for medicine, dye and spice intermediate.    ADVANTAGE - The present method is simple, safe, reliable and environment-friendly; saves the energy; has low cost; provides convenient operation; provides guaiacol with high purity.
NOVELTY - Method for fermentation and conversion of antibiotic residues to humus, involves using composition of microorganism for solid-state fermentation of material. The material comprises antibiotic residues and straw. The composition of microorganism comprises Trichoderma, Bacillus subtilis and B.licheniformis. The weight ratio of the Trichoderma, B.subtilis and B.licheniformis is (3-5):(2-4):(2-4).    USE - The method is useful for fermentation and conversion of antibiotic residues to humus (claimed).    ADVANTAGE - The method consumes less time, does not produce peculiar smell during fermentation, and meets Q/BJZZT0005-2014 standards for degradation of antibiotic residues.
NOVELTY - The system has a power transmission transformer ECU unit, a memory unit and a checking module that are connected together. A detecting module comprises a concentration detection module and a content module. The concentration detection module detects concentration of gas component, where a gas component detection concentration value exceeds a limit value. The ECU unit outputs a warning signal. The memory unit is connected with an ECU unit. The concentration detection module and a hydrocarbon content transformer are connected together.    USE - Transmission transformer control system.    ADVANTAGE - The system is provided with the concentration detection module for detecting concentration of the gas component so as to avoid malfunction.    DETAILED DESCRIPTION - The gas component is selected from a group consisting of hydrogen, methane, ethylene, ethane and ethyne.    DESCRIPTION OF DRAWING(S) - The drawing shows a functional block diagram of a transmission transformer control system. '(Drawing includes non-English language text)'
NOVELTY - Extracting licorice comprises (i) crushing licorice slice; (ii) adopting tissue disruption method for extracting licorice, extracting to obtain the crude extract; (iii) concentrating the crude extract, centrifuging the concentrated solution to obtain the supernatant; (iv) adding concentrated sulfuric acid into the supernatant, stirring and allowing to stand, and filtering to obtain the filtrate and precipitate; (v) neutralizing filtrate, condensing into a thick paste, and then drying to obtain licorice extract; and (vi) washing the resulting precipitate and drying to obtain glycyrrhizic acid.    USE - The method is useful for extracting licorice to obtain glycyrrhizic acid (claimed).    ADVANTAGE - The method is economical, easy to operate, consumes little solvent, has high production efficiency, does not cause environmental pollution, achieves continuous production, produces product with good quality, and improves the utilization value of Chinese herbal medicine.    DETAILED DESCRIPTION - Extracting licorice comprises (i) crushing licorice slice; (ii) adopting tissue disruption method for extracting licorice, using ethanol solution as the extractant, extracting 8-20 times, for 3 times to obtain the crude extract; (iii) concentrating the crude extract to obtain a concentrated solution, centrifuging the concentrated solution to obtain the supernatant; (iv) adding concentrated sulfuric acid into the supernatant, stirring and allowing to stand, and filtering to obtain the filtrate and precipitate; (v) neutralizing the resulting filtrate with lime, condensing into a thick paste, and then drying to obtain licorice extract; and (vi) washing the resulting precipitate with water and drying to obtain glycyrrhizic acid.
NOVELTY - Preparing titanium dioxide from yeast, comprises reacting yeast and titanium tetrachloride by adding water at 100-150 degrees C under pH condition of 4-6, to obtain the product.    USE - The titanium dioxide is useful for removing pollutants from industrial wastewater, and cyanide ions and copper ions from copper cyanide wastewater (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) titanium dioxide prepared as mentioned above;    (2) use of titanium dioxide in the removal of cyanide ions and copper ions from copper cyanide wastewater; and    (3) use method of titanium dioxide, comprising removing cyanide ions and copper ions from copper cyanide wastewater by illuminating UV light under pH condition of 2-8.
NOVELTY - Catalyst comprising a graphite mesoporous carbon as carrier and 41-55 mass% of iron-nickel alloy as active component, is new. The catalyst has specific surface area of 300-600 m2.g-1, pore diameter of 3-15nm, and a pore volume of 0.4-1.5 cm3.g-1.    USE - Biomass gasification tar cracking catalyst.    ADVANTAGE - The eco-friendly catalyst has large specific surface area, uniform aperture and improved durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of catalyst.
NOVELTY - Preparing Raney nickel methanation catalyst comprises mixing nickel powder and molybdenum powder uniformly, immersing the powder in diluted acid solution and then in ethanol, washing the powder with deionized water, drying, immersing aluminum powder in organic solvent, washing, then drying, mixing nickel powder, molybdenum powder and aluminum powder, heating the mixture, cooling, crushing nickel-aluminum alloy powder, mixing nickel-aluminum alloy powder with sodium hydroxide solution, removing the upper layer of the alkali solution, and washing the product to prepare Raney nickel catalyst.    USE - The method is useful for preparing Raney nickel methanation catalyst (claimed).    ADVANTAGE - The method is capable of preparing Raney nickel methanation catalyst having uniform particle size, high mechanical strength and good catalytic activity in high yield.    DETAILED DESCRIPTION - Preparing Raney nickel methanation catalyst comprises uniformly mixing nickel powder and molybdenum powder, immersing the powder in diluted acid solution for 5-60 minutes and then in ethanol for 5-30 minutes, washing the powder with deionized water for 2-4 times, drying at 50-110 degrees C for 1-8 hours, immersing aluminum powder in organic solvent for 5-30 minutes, washing with deionized water for 2-4 times, then drying at 50-110 degrees C for 1-8 hours, mixing nickel powder, molybdenum powder and aluminum powder, heating the mixture in a high-temperature furnace, cooling the mixture at room temperature under the protection of inert gas, crushing the nickel-aluminum alloy powder to a particle size of 40-100 meshes, mixing the nickel-aluminum alloy powder with sodium hydroxide solution in a water tank at 0-70 degrees C for 3-24 hours, removing the upper layer of the alkali solution after completion of the reaction, washing the obtained product repeatedly with deionized water to neutral and then with anhydrous ethanol for 2-4 times to obtain Raney nickel catalyst.
NOVELTY - This utility new type claims a one biomass, comprise the granulating room, a pressing wheel assembly, a drive mechanism. Using the eccentric wheel of a three symmetrical to ensure a uniform stress and it is not easy to be damaged. The die fixing ring mould, to fix and location function. A plate can be stable in a platen and lower pressure disk. Structure change transmission direction of the torque increase, it has small motor drives the large device of effect.
NOVELTY - A sewage is processed by dissolving 0.05-0.5 g/L cationic surfactant in water to obtain mixture in which cationic surfactant is hexadecyltrimethylammonium bromide, dodecyltrimethylammonium chloride, or benzyldimethyldodecylammonium chloride, adding to sewage, adding 0.5-1.5 g/L sodium chloride, stirring at 20-25 degrees C, pH of 6.5-7.5, and speed of 200-300 rpm, and performing electric flocculation using pure aluminum electrode with electrode plate spacing of 0.5-2 cm and electric current density of 1.07-8.52 A/m2.    USE - Processing of sewage (claimed).    ADVANTAGE - Process is short and stable, has increased sewage treatment efficiency and reduced electric energy, and produces smaller hydrogen gas bubbles.
NOVELTY - Treatment of industrial sewage comprises preparing microbial inoculum; carrying out sewage sedimentation; sewage purifying and preparing fertilizer.    USE - Method for treating industrial sewage used for preparing fertilizer (claimed).    ADVANTAGE - The method is simple.
NOVELTY - Crop biological fertilizer comprises soluble phosphorus and phosphorus ore powder fermentation liquid. The phosphorus solubilizing fungi is Aspergillus niger XXR-B1 (KF572126) for corn special biological fertilizer.    USE - Crop biological fertilizer.    ADVANTAGE - The fertilizer avoids environmental pollution and food contamination caused by mineral fertilizer, makes up for the current lack of special type of biological fertilizer deficiencies, and utilizes natural dissolved phosphorus microbial resources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of crop biological fertilizer comprising collecting soil sample, gradient diluting with soluble phosphorus on screening culture medium for 5-10 days at 25-30 degrees c, dissolving phosphorus fungal colonies, culturing with phosphorus-solubilizing bacteria medium at 25-30 degrees c for 3-5 days, separating and purifying; and fermenting soluble phosphorus and phosphate fermentation liquid at 28-30 degrees c for 15-18 days, separating and purifying.
NOVELTY - Vegetable seedling matrix comprises garden greening waste, tea dregs and pig manure. The garden greening waste is deadwood, fallen leaves, herb trash and grass trimmings. The vegetable seedling matrix is prepared by crushing garden greening waste, mixing garden greening waste, tea dregs and pig manure at mass ratio of 4:6:2:2, regulating water content at 55-65% and carbon-nitrogen mass ratio at 25-30, forced ventilating and aerobic composting.    USE - Vegetable seedling matrix.    ADVANTAGE - The matrix has low cost, wide source and easy to get raw materials and stable property. It is environment-friendly and ensures plant survival.    DETAILED DESCRIPTION - Vegetable seedling matrix comprises garden greening waste, tea dregs and pig manure. The garden greening waste is deadwood, fallen leaves, herb trash and grass trimmings. The vegetable seedling matrix is prepared by crushing garden greening waste, mixing garden greening waste, tea dregs and pig manure at mass ratio of 4:6:2:2, regulating water content at 55-65% and carbon-nitrogen mass ratio at 25-30, forced ventilating and aerobic composting. Aerobic composting is done by supplying oxygen by forced ventilation at 200-300 L/hour for 10-15 minutes, stopping for 45-50 minutes, continuing for 30-40 days, turning for once/3 days for 15-20 days, and turning once/7 days for 15-20 days.
NOVELTY - Preparing acetyl salicylic acid comprises mixing salicylic acid and acetyl chloride and then reacting to obtain acetyl salicylic acid and hydrochloric acid.    USE - The process is useful for preparing acetyl salicylic acid (claimed).    ADVANTAGE - The process is capable of easily and economically preparing acetyl salicylic acid with high purity of more than 99.9% and yield of 90% and less energy consumption and without using catalyst.
NOVELTY - Method for preparing bioorganic fertilizer, involves fermenting humic acid, fermented microbial raw material and fermented feedstock, and controlling water content of the fermented product to 45-48%, where carbon and nitrogen ratio in the fermented product is 20-30:1, and the fermented feedstock comprises 500-600 pts. wt. Agaricus residue (3 mesh size), 10-50 pts. wt. sawdust (3 mesh size), 20-30 pts. wt. furfural residue (3 mesh size), 2-8 pts. wt. sucrose, and 10-13 pts. wt. inorganic minerals.    USE - The method is useful for preparing bioorganic fertilizer (claimed).    ADVANTAGE - The method is simple to perform. The prepared bioorganic fertilizer improves fertility of soil, promotes yield and quality of crops.    DETAILED DESCRIPTION - Method for preparing bioorganic fertilizer, involves fermenting humic acid, fermented microbial raw material and fermented feedstock, and controlling water content of the fermented product to 45-48%, where carbon and nitrogen ratio in the fermented product is 20-30:1, and the fermented feedstock comprises 500-600 pts. wt. Agaricus residue (3 mesh size), 10-50 pts. wt. sawdust (3 mesh size), 20-30 pts. wt. furfural residue (3 mesh size), 2-8 pts. wt. sucrose, and 10-13 pts. wt. inorganic minerals. The fermented microbial raw material comprises 0.4-8 pts. wt. Bacillus subtilis having viable count of more than 70 millions/g, 0.4-8 pts. wt. yeast having viable count of more than 60 millions/g, 0.4-0.8 pts. wt. phosphate solubilizing bacteria having viable count of more than 50 millions/g, and 12-20 pts. wt. Azotobacter having viable count of more than 50 millions/g.
NOVELTY - Production of iron-rich organic fertilizer using waste tea residue comprises drying tea residue and dairy manure, crushing, passing by 20 items sieve; taking 20-40 wt.% dairy manure, 60-80 wt.% tea residue, 27-46 wt.% sucrose, 1-3 wt.% antiseptic agent and 15-25 wt.% inorganic iron salt; mixing raw materials with water until water content is 55-65%; aerobic fermenting at 50-70 degrees C for 50-60 days; and naturally drying until the water content is 30%.    USE - Method for producing iron-rich organic fertilizer using waste tea residue (claimed).    ADVANTAGE - The method utilizes waste which helps in protecting the environment, increases effectiveness of inorganic iron fertilizer, and ensure good crop growth.
NOVELTY - Biological enzyme fertilizer comprises 2-100 pts. wt. chicken, 1-100 pts. wt. husk powder, 1-10 pts. wt. enzyme, 1-80 pts. wt. Sorghum straw, 1-20 pts. wt. dicalcium phosphate, 1-3 pts. wt. urea, 1-3 pts. wt. zinc sulfate, 9-20 pts. wt. ammonium sulfate, 15-20 pts. wt. potassium chloride, 1-25 pts. wt. bentonite and 1-30 pts. wt. potassium sulfate.    USE - Biological enzyme fertilizer.    ADVANTAGE - The biological enzyme fertilizer improves soil and increases quality of crops and roots.
NOVELTY - Nutritive soil comprises 30-40 wt.% field topsoil, 20-25 wt.% humus, 10-20 wt.% lees, 15-22 wt.% sand, 10-15 wt.% organic fertilizer, and 2-6 wt.% calcium superphosphate.    USE - The nutritive soil is used in nonwoven fabric pots for growing C.illinoinensis in nursery (claimed).    ADVANTAGE - The nutritive soil is convenient to use, provides nutrients required by C.illinoinensis for a long period of time, promotes seed germination and rooting and rapid growth of C.illinoinensis seedling, and provides C.illinoinensis having resistance with respect to pests and diseases. The method is simple and cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the nutritive soil, which involves (a) weighing above-mentioned components, uniformly mixing the components, (b) adding mixture obtained in step (a) to a bottom layer of pots, compacting the mixture with soil, filling the soil to a height of 3-5 cm in the pots, and sowing seeds of Carya illinoinensis to each pot, and (c) orderly placing the pots, watering the pots, and ensuring whether the seeds of C.illinoinensis are fully integrated with the soil.
NOVELTY - Organic-inorganic special fertilizer comprises 10-13 wt.% nitrogenous fertilizer, 5-7 wt.% phosphate, 7-11 wt.% potash, 40-60 wt.% decomposed organic fertilizer, 0.1-3 wt.% fertilizer synergist, 1-5 wt.% micronutrient, 1-10 wt.% chelating agent and 0.1-2 wt.% pharmaceutical drug. The micronutrient comprises 0.5-2 wt.% calcium nitrate, 0.2-0.5 wt.% borax and 0.5-2 wt.% magnesium sulfate.    USE - Organic-inorganic special fertilizer used for preventing and treating tomato bacterial wilt.    ADVANTAGE - The special fertilizer increases nutrient utilization of crops, and increases quality of tomatoes.
NOVELTY - An organic functional fertilizer comprises 100 pts. wt. straw chips, 0.03-0.004 pts. wt. soil improved with composite microbial inoculum, 0.5-2 pts. wt. phosphate, 6-12 pts. wt. sepiolite, 5-10 pts. wt. peat, 5-15 pts. wt. fly ash, and 5-12 pts. wt. bentonite. The composite microbial inoculum comprises nitrogen-fixing bacteria, Bacillus subtilis, Bacillus thuringiensis, Lactobacillus, and microorganism strain.    USE - An organic functional fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the organic functional fertilizer, comprising crushing straw pole, placing in a corrosion resistant container, adding 2-5% of 0.5 mol/L sodium hydroxide (NaOH) solution, adding 10-15% of water, uniformly mixing, and maintaining at room temperature for 2-4 hour; adding composite microbial inoculum to the pre-processed straw, mixing, sealing at 10-55 degrees C, and fermenting at 10-30 degrees C for 3-5 days; sterilizing the ferment, adding peat, fly ash, bentonite, and phosphate, uniformly mixing, drying, and grinding to 40 meshes powder base material; adding a soluble nitrogen, amino acid fertilizer, and soil improved with composite microbial inoculum; and adding bentonite, and granulating.
NOVELTY - Preparing gluconic acid using bipolar membrane electrodialysis method, comprises removing large particles of suspended solids ( less than or equal to 0.5 mg/l) in sodium gluconate through a bag filter, trapping large molecular weight contaminants through nanofiltration, introducing resulting permeate of sodium gluconate into a bipolar membrane electrodialysis membrane reactor at a reaction temperature of 15-50 degrees C, and recovering alkali compartment of sodium hydroxide and acid compartment of gluconic acid, where a mass fraction of permeate of sodium gluconate is 10-40%.    USE - The method is useful for preparing gluconic acid using bipolar membrane electrodialysis method (claimed).    ADVANTAGE - The method ensures economical and stable preparation of gluconic acid at high recovery rate and low energy consumption.    DETAILED DESCRIPTION - Preparing gluconic acid using bipolar membrane electrodialysis method, comprises removing large particles of suspended solids ( less than or equal to 0.5 mg/l) in sodium gluconate through a bag filter, trapping large molecular weight contaminants through nanofiltration, introducing resulting permeate of sodium gluconate into a bipolar membrane electrodialysis membrane reactor at a reaction temperature of 15-50 degrees C, and recovering alkali compartment of sodium hydroxide and acid compartment of gluconic acid, where a mass fraction of permeate of sodium gluconate is 10-40%. The gluconic acid has a hardness of less than or equal to 30 mg/lm an electrical conductivity of 22-30 millisecond/cm and residual sugar concentration of less than or equal to 0.8%.
NOVELTY - Recovering pregabalin intermediate resolving agents (R)-(+)- alpha -phenylethylamine, comprises (i) adding mother liquor at 30-50 degrees C, and adjusting the pH of mother liquor by adding alkali to be alkaline; (ii) adjusting the pH of system, and extracting for 3-6 times by adding an organic solvent; and (iii) mixing the extracted organic layer at 30-60 degrees C by adding an extracting agent, and distilling under reduced pressure, and extracting, and collecting the fractions, heating at 80-90 degrees C, and distilling under reduced pressure, to obtain distillate-containing resolving agent.    USE - The method is useful for recovering pregabalin intermediate resolving agents (R)-(+)- alpha -phenylethylamine (claimed).    ADVANTAGE - The method increases the utilization rate atomic material in the mother liquid by preventing direct emissions into environment, and thus it is environmental-friendly; and is economical.    DETAILED DESCRIPTION - Recovering pregabalin intermediate resolving agents (R)-(+)- alpha -phenylethylamine, comprises (i) adding mother liquor at 30-50 degrees C, and adjusting the pH of mother liquor by adding alkali to be alkaline; (ii) adjusting the pH of system, and extracting for 3-6 times by adding an organic solvent; and (iii) mixing the extracted organic layer at 30-60 degrees C by adding an extracting agent, and distilling under reduced pressure, and extracting, and collecting the fractions, heating at 80-90 degrees C, and distilling under reduced pressure, to obtain distillate-containing resolving agent. In the step (i), the mother liquor is (R)-(-)-3-(carbamoylmethyl)-5-methylhexanoic acid-(+)- alpha -phenethylamine salt obtained by adding (R)-(-)-3-(carbamoylmethyl)-5-methylhexanoic acid dropwise, and cooling the substance, cooling, crystallizing, and filtering to obtain filtrate.
NOVELTY - Preparing corosolic acid (IV) comprises oxidizing ursolic acid (I) in presence of oxidizing agent comprising 2-iodoxybenzoic acid to form 3-carbonyl ursolic acid (II) and reacting (II) with m-chloroperbenzoic acid to obtain 2 alpha -hydroxy-3-carbonyl ursolic acid (III), and reducing (III) with sodium borohydride, extracting, drying, concentrating and purifying by chromatography.    USE - The method is useful for preparing (IV) (claimed).    ADVANTAGE - The method provides a yield of 55-62% in m-chloroperbenzoic acid oxidation step and reduction step, and total yield of 48-56% (claimed); does not utilize chromium salt oxidizing agent, and benzyl protection groups; does not cause pollution; and is non-toxic, free of heavy metal ions, cost effective, simple, carried out within short period, and suitable for industrial production.    DETAILED DESCRIPTION - Preparing corosolic acid of formula (IV) comprises oxidizing ursolic acid of formula (I) in presence of oxidizing agent comprising 2-iodoxybenzoic acid to form 3-carbonyl ursolic acid of formula (II) and reacting (II) with m-chloroperbenzoic acid to obtain 2 alpha -hydroxy-3-carbonyl ursolic acid of formula (III), and reducing (III) with sodium borohydride, extracting, drying, concentrating and purifying by chromatography.
NOVELTY - Waste wood and sawdust are cleaned, crushed, dried, heated, and subjected to thermoforming process. Furnace is then heated, evaporated and ventilated. Condensation pipe valve is opened, and external heating is terminated, while rod-like material is ignited. Lignin is precipitated and smoke steam condensate is imported to condensate tank, separated and wood tar mixture is collected. Resultant mixture is treated using sodium hydroxide or potassium hydroxide solution, and resultant heated wood tar is distilled to obtain wood tar.    USE - Preparation of wood tar (claimed).    ADVANTAGE - The method efficiently and economically provides wood tar with reduced pressing molding difficulty and increased combustion efficiency of inner furnace.    DETAILED DESCRIPTION - Bark, twigs, mud, stones and other debris are removed from waste wood and sawdust, and crushed to particle size of less than 2 mm. The pulverized wood surface is placed in a drying apparatus, and dried at 100 degrees C for 3-4 hours, such that the moisture content of wood and sawdust is 15% or less, preferably 10-12%. The mixed wood surface is heated at 120-150 degrees C, and subjected to thermoforming process in a molding machine at 120-150 degrees C. The furnace is then heated at 100-120 degrees C for 0.5-1 hour, evaporated and further ventilated, such that the moisture content is 6-8%. Condensation pipe valve is opened, and external heating is terminated, while the rod-like material is ignited. When the temperature of the furnace increases to 200 degrees C or more, lignin is precipitated. Smoke steam condensate from the condenser valve is imported to condensate tank, separated and wood tar mixture is collected. The resultant mixture is then treated using sodium hydroxide or potassium hydroxide solution, and the resultant heated wood tar is distilled to obtain wood tar.
NOVELTY - Preparing biological carbon comprises washing the edible fungus waste to remove impurities and then drying, crushing and sieving, pulverizing the edible fungus waste to 5-10 degrees C/minutes, raising the temperature to 400-600 degrees C to carry out oxygen carbonization reaction for 1.5-2 hours, cooling the edible fungus waste to room temperature and then crushing and sieving to obtain biological carbon.    USE - The method is useful for preparing biological carbon, which is useful as adsorbent for treating ammonia-nitrogen polluted water (all claimed).    ADVANTAGE - The biological carbon has increased ammonia nitrogen absorbing efficiency.
NOVELTY - Methanol gasoline (M25) comprises: 20 mass% of coal-based methanol; 79.94 mass% of gasoline base oil; 0.01 mass% of metal passivating agent; and 0.05 mass% of antioxidant. The gasoline base oil includes 10-18 mass% of light-hydrogenated oil, 10-15 mass% of pentane oil, 20-30 mass% of 7C or 9C organic compound, 0-9 mass% of pentane, 9-14 mass% of raffinate oil, 3-14 mass% of methyl tertiary-butyl ether, 4 mass% of isoamyl alcohol, 1 mass% of octanol, and 0.3 mass% of dioctyl sebacate.    USE - The methanol gasoline (M25) is useful for vehicles (claimed).    ADVANTAGE - The methanol gasoline avoids corrosion and swelling problems of the vehicles.
NOVELTY - Multi-tower string-parallel circulating amine liquid absorbing device comprises a first absorption tower (1) in turn connected with a second absorption tower (2), a third absorption tower (3), a fourth absorption tower (4), a fifth absorption tower (5) and a sixth absorption tower. The first absorption tower through the pipeline is connected with raw material gas inlet and raw gas source. The sixth absorption tower is set with a raw material gas outlet, and further includes poor liquid pump, where the inlet of the poor liquid pump is connected with the absorption tower group.    USE - The device is used for natural gas, synthetic gas and and other gas purification for removing carbon dioxide, hydrogen sulfide and other acidic gas.    DETAILED DESCRIPTION - Multi-tower string-parallel circulating amine liquid absorbing device comprises a first absorption tower (1) in turn connected with a second absorption tower (2), a third absorption tower (3), a fourth absorption tower (4), a fifth absorption tower (5) and a sixth absorption tower. The first absorption tower through the pipeline is connected with raw material gas inlet and raw gas source. The sixth absorption tower is set with a raw material gas outlet, and further includes poor liquid pump, where the inlet of the poor liquid pump and the poor amine liquid source outlet through pipeline is connected with the absorption tower group. The part of amine liquid inlet is connected to the absorption tower. The absorption column group and the rich solution outlet of the absorbing tower are connected through pipeline and liquid outlet pipeline.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the multi-tower string-parallel circulating amine liquid absorbing device (Drawing includes non-English language text).    First absorption tower (1)    Second absorption tower (2)    Third absorption tower (3)    Fourth absorption tower (4)    Fifth absorption tower (5)
NOVELTY - Preparation of organic fertilizer from juice of white wine precipitate comprises filtering juice of white wine precipitate in vacuum drum filter, where filtered liquid is used for wine production, and filter cake is used for manufacturing organic fertilizer; uniformly mixing filter cake with lees, mud stacking, in which fermentation water content is 60-70%, turning once every 2-3 days, and fermenting for 15-20 days to obtain the organic fertilizer.    USE - Preparation method of organic fertilizer from juice of white wine precipitate.    ADVANTAGE - The prepared fertilizer has organic matter content of 62.5%, and nitrogen, phosphorus and potassium total amount of more than 10.5%,. The white wine precipitate juice can be made into the required refined organic fertilizer, can increase the soil organic matter, improves soil structure for crops, fruit trees and vegetation, and provides good yield.
NOVELTY - Carbonization dry distillation kettle, comprises a kettle body (5) whose upper part is set with a kettle cover (1). The kettle cover is provided with 1-4 discharge holes. The inner part of a discharge tube (2) is set with a least one discharge hole. The bottom part of the kettle body along the longitudinal direction is opened with 1-4 first flow guide channels (6). The bottom part of the kettle body along the transverse direction is provided with 1-3 second flow guide channels (8).    USE - The kettle is useful for carbon-based biomass system (claimed).    ADVANTAGE - The kettle uniformly heats biomass, exhibits rapid carbonization rate, can shorten the production time, reduces the production cost, comprising the kettle body remains intact even after repeated use, effectively controls the deformation rate of the kettle body, extends the service life of the reactor body, has good sealing property between the kettle body and the kettle cover, does not allow easy passage of air into the reaction system, and produces high quality product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the carbonization dry distillation kettle.    Kettle cover (1)    Discharge tube (2)    Kettle body (5)    First flow guide channels (6)    Second flow guide channels (8)
NOVELTY - The structure has a furnace body provided with a reaction room. The reaction room is divided into a drying layer, a solution layer, a reducing layer and an oxide layer. The furnace body is formed with a feeding port, a gasification medium entrance and a gas exit. A furnace bar is arranged in an inner part of the furnace body. An end of a gas channel is fixed with the reducing layer. Another end of the gas channel is connected with the gas exit. The reducing layer is formed by high-temperature pyrolysis material. The furnace body is connected with a water tank.    USE - Furnace body clamping layer structure for a coke biomass gasification furnace.    ADVANTAGE - The structure is easy to maintain, and reduces tar content ratio, and can form a furnace body structure construction channel to increase flow rate of air inlet/outlet pneuma.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a furnace body clamping layer structure.
NOVELTY - Synthesizing a natural gas product involves: (1) increasing pressure of yellow phosphorus tail gas to be 50-70 kpa; (2) purifying tarry impurities contained in the phosphorus using a purifier; (3) performing an oxidation process of a phosphorus exhaust to remove hydrogen sulfide; (4) washing the obtained product using a concentrated sulfuric acid and a base, then neutralizing, and contacting the neutralized mixture with an alkaline solution to remove an acidic substance; and (5) removing arsenic, fluorine, oxygen and carbon monoxide using temperature swing adsorption technique.    USE - The process is useful for synthesizing a natural gas product (claimed).    ADVANTAGE - The process is capable of effectively synthesizing the natural gas product with high purity.    DETAILED DESCRIPTION - Synthesizing a natural gas product involves: (1) increasing a pressure of yellow phosphorus tail gas to be 50-70 kpa; (2) purifying tarry impurities contained in the yellow phosphorus tail gas using a purifier; (3) performing oxidation process of a phosphorus exhaust in the yellow phosphorus tail gas to remove hydrogen sulfide; (4) washing the product obtained in the step (3) using a concentrated sulfuric acid and a base, then neutralizing, contacting the neutralized mixture with an alkaline solution to remove the acidic substance, where the pressure of the yellow phosphorus tail gas is increased to be 2.5-3 MPa; (5) removing arsenic, fluorine, oxygen and carbon monoxide using temperature swing adsorption technique at room temperature of 100-150 degrees C, then carrying out deoxygenation reaction, which is operated at a temperature of 60-150 degrees C, and a gas space velocity of 5000-10000 hour-1; (6) cooling, decarburizing, drying and ultra-fine purifying obtained deoxygenation reaction product with water; and (7) performing methanation reaction of the purified mixture and then cooling and drying to obtain the synthesis natural gas product.
NOVELTY - The distillation device comprises a tower body having an outlet at a top. The tower body is provided with a residual liquid outlet. A side wall of the tower body is provided with a source connected with a raw material feeding port. An upper part of the feeding port is provided with a baffle tower disk. A lower part of the feeding port is provided with a spiral shaped heating plate. A peripheral edge of the heating plate is attached to an inner side wall of the tower body along axial direction, where the heating plate has an angle of 10-15 degrees .    USE - The distillation device is useful for biodiesel purification.    ADVANTAGE - The distillation device ensures that heating process is continuous using the heating plate, hence its performance is improved.    DETAILED DESCRIPTION - The distillation device comprises a tower body having an outlet at a top. The tower body is provided with a residual liquid outlet. A side wall of the tower body is provided with a source connected with a raw material feeding port. An upper part of the feeding port is provided with a baffle tower disk. A lower part of the feeding port is provided with a spiral shaped heating plate. A peripheral edge of the heating plate is attached to an inner side wall of the tower body along axial direction, where the heating plate has an angle of 10-15 degrees . The device further comprises a detection unit provided with a control unit, where the detection unit detects working parameter of the distillation device. The control unit controls vaporizing condition of the distillation device. The detection unit includes: a probe for detecting inner pressure of the tower body and pressure signal transmitted to the control unit; a probe for detecting temperature at top and inner side of the tower body and temperature signal transmitted to the control unit; and a probe for detecting flow quantity of the feeding port and flow signal transmission rate of the control unit.
NOVELTY - Complex microorganism liquid silicon fertilizer comprises algal microorganism, fungal microorganism, livestock manure, actinomycetes, nitrogen-fixing bacteria, silicate bacteria, Bacillus subtilis, Paenibacillus polymyxa, Trichoderma, microzyme, photosynthetic bacteria, and polyaspartic acid.    USE - Used as complex microorganism liquid silicon fertilizer.    ADVANTAGE - The fertilizer: can break soil plate structure; enables deep fertilization to promote root growth; and easily supplies nutrients to the crops to promote root growth.