NOVELTY - Microbial inoculum comprising green Trichoderma and Saccharomyces cerevisiae, is new.    USE - The microbial inoculum is useful in preparing organic fertilizer for improving plant yield, preferably cucumber and pepper yield after being applied to the soil (claimed).    ADVANTAGE - The microbial inoculum: increases cucumber and pepper yields by respectively 21.98% and 19.71%. The method recycles the waste, thus improving the utilization rate of the rural organic wastes; has simple and easy fermentation process; and is suitable for application in rural area.    DETAILED DESCRIPTION - Preparing organic fertilizer, comprising composting crop straw, livestock and poultry excrement and rural domestic waste, fermenting the compost, mixing with the microbial inoculum, stacking, carrying out stack fermentation to obtain organic fertilizer; and #an organic fertilizer, prepared by the above mentioned method.
NOVELTY - Producing erythromycin antibiotic through bacterial mutagenesis involves: (a1) culturing erythromycin producing bacteria on an inclined upper surface of a culture medium at 34 plus minus 1 degrees C for 6-7 days to obtain fresh and mature spores; (b1) preparing suspension of spores in a cell volume of 1x 106 cells/ml, placing it on inclined upper surface of culture medium containing plate, then irradiating, and diluting the plates after mutagenesis; and (c1) performing ion beam radiation mutagenesis at 25 degrees C and dosage of 50Gy, and then screening by fermentation using a culture medium.    USE - For producing erythromycin antibiotic (claimed) which is useful against broad-spectrum bacteria (e.g. penicillin-resistant Staphylococcus aureus, amoeba, trichomoniasis); and for treating rickettsia, and mycoplasma.    ADVANTAGE - The present method provides erythromycin antibiotic in an improved yield, improved product quality and purity; and is cost-effective and environment-friendly.    DETAILED DESCRIPTION - Producing erythromycin antibiotic through bacterial mutagenesis involves: (a1) culturing erythromycin producing bacteria on an inclined upper surface of a culture medium at 34 plus minus 1 degrees C for 6-7 days to obtain fresh and mature spores; (b1) preparing suspension of fresh and mature spores in a cell volume of 1x 106 cells/ml, placing 5 ml spore suspension on inclined upper surface of culture medium containing plate, then irradiating at 15 W UV lamp with fixed distance of 20 cm for 2 minutes, and diluting culture medium plates immediately after mutagenesis; and (c1) performing ion beam radiation mutagenesis at 25 degrees C and dosage of 50Gy, performing initial mutagenesis on a gradient dilution coating culture medium plate, selecting single bacterial colony from slanted culture medium, culturing at 34 plus minus 1 degrees C for 6-7 days, and then screening by a fermentation using a culture medium to obtain high yield of erythromycin.
NOVELTY - Velvet beans as raw material is crushed, extracted using acidic solution, filtered, impurity removing agent is added, and filtered, to obtain preliminary purification solution. The pH of solution is adjusted to 1-4 using an agent, and processed in an electrodialysis device, to obtain liquid material. The pH of resultant liquid is adjusted to 3.5, filtered, precipitate is collected, pH value of solution is adjusted to 1-3 using purified water, heated to dissolve, filtered, crystallized, precipitated, filtered, washed with anhydrous ethanol, and dried, to obtain levodopa.    USE - Preparation of high-purity levodopa (claimed).    ADVANTAGE - The method economically and environmentally-friendly provides levodopa having high purity, within a short period of time.    DETAILED DESCRIPTION - Velvet beans as raw material is crushed, extracted using acidic solution, filtered, impurity removing agent is added, and filtered, to obtain preliminary purification solution. The pH of solution is adjusted to 1-4 using an agent, and processed in an electrodialysis device, to obtain liquid material. The pH of resultant liquid is adjusted to 3.5, cooled to 0-4 degrees C, filtered, precipitate is collected, pH value of the solution is adjusted to 1-3 using purified water, heated to dissolve, stirred for 5 minutes, filtered, cooled to 0-4 degrees C, crystallized, precipitated, filtered, washed with anhydrous ethanol, and dried at 50 degrees C or less, to obtain levodopa.
NOVELTY - Sugar for bio-alcohol production is produced by degrading bioorganic matter containing lignocellulose to generate greater than or equal to 1 sugar from lignocellulose and degraded bioorganic residue and forming plant growth medium from degraded bioorganic residue.    USE - Production of sugar for bio-alcohol production (claimed).    ADVANTAGE - The method improves the economic viability of processing bioorganic matter containing lignocellulose.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for kit used for producing sugar comprising vessel for subjecting bioorganic matter to conditions capable of melting, hydrolyzing, and/or solubilizing lignocellulose in bioorganic matter, such as steam explosion apparatus, vessel for forming bio-alcohol from greater than or equal to 1 sugar by fermentation, bioorganic matter containing lignocellulose, microbial agent capable of forming bio-alcohol from greater than or equal to 1 sugar by fermentation, and instructions for performing sugar production.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the process of producing sugar for bio-alcohol production.
NOVELTY - This utility new type bottom provide one with a NBF nano-composite biological filler of sewage treatment device, comprising a grating regulating pond, the inclined tube sedimentation tank, filter tank and a weir, wherein the sewage through the total water inlet tube flows into the said grid regulating pool, a grid regulating tank part is provided with a sewage to the sewage of the said inclined tube sedimentation tank, sewage through the weir of the overflow weir is set on the said upper sloping-pipe precipitated pool, flows a filter tank is set above of, a downflow weir and a weir connected, a filter tank is provided with a NBF nano-composite biological filler layer, sewage by a NBF nano-composite biological filler layer is formed by the main water outlet tube. The device has simple structure, stable, it does not need management is easy to realize automatic control.
NOVELTY - Culture substrate comprises 2-5 vol.% of dairy manure, 1-6 vol.% of edible fungi waste and 1-5 vol.% of perlite.    USE - The culture substrate is useful for capsicum seedling in winter and spring season (claimed).    ADVANTAGE - The culture substrate utilizes agricultural waste, protects the rural environment, reduces the breeding cost and improves the quality of seedlings.
NOVELTY - This utility new type belongs to the field of biochemical using device technology field, especially relates to one production bio-diesel catalyst using a biomass material of full-manual mixer, comprising a rack set with universal wheel of the bottom, one end of the rack is convenient to set with pushing handrail of walking, to the horizontal direction rack is set on the upper part of cylinder, the cylinder and the rotating connecting rack, the cylinder one end of in part set with first feeding port, in part of the other end set with second feeding port, the upper tube set with discharge hole and a switch discharge hole of discharge hole cover, annular array of mixing cylinder upper cylinder wall of several handle; it only needs to aritificial operation time without other power device, set with a universal wheel, the bottom of two end of mixing cylinder in part set with two feed inlets can be a single feeding and continuous feeding, solving the mixer is not suitable for biomass material mixing of problem and can be convenient and fast to carry, does not consume energy can be valid of reducing production cost.
NOVELTY - Electrochemical desulfurization comprises (i) preparing a saturated solution of halogen element of sodium salt or potassium salt, (ii) electrolyzing the saturated solution to obtain absorption solution; (iii) spraying the absorption solution into a sulfur dioxide absorption tower containing sulfur dioxide gas and allowing for complete contact; and (iv) recycling absorption solution.    USE - The method is useful for producing sodium sulfate and potassium sulfate. The sodium sulfate crystal is useful for producing sodium silicate, sodium sulfide and sulfate pulp cooking agent. The potassium sulfate is used as precipitating agent in glass industry, and as agricultural fertilizer (all claimed).    ADVANTAGE - The method has sulfur dioxide absorption rate of more than 97%, ensures quick absorption and does not produce solid waste.
NOVELTY - The method involves placing a medical waste treatment system in a gasification furnace. High temperature steam and high temperature air are produced by a heat accumulating type heat interchanger for performing medical waste sterilizing and degrading gasification treatment process. Soft water is produced by a gasified gas heat exchange boiler and a heat exchanging boiler gasification furnace during gas-water spraying process. The gasified gas heat exchanging boiler is entered into a gasified gas purification system to obtain hydrogen-rich gas purifying gas.    USE - Medical waste high temperature steam-gasification air disinfecting and degrading method.    ADVANTAGE - The method enables reducing volume of medical waste and gasification gas tar cracking rate to about 99%, discharging product without second dioxin and realizing medical waste external inquiry process with zero energy consumption, zero pollution and zero discharge.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a medical waste treatment system.
NOVELTY - This utility new type relates to a one pulse biological selector, comprising a pulse water distributor and biological selecting tank, a pulse water distributor is set in the said biological selecting tank, a pulse water distributor comprises a pulse device and perforated tube water distributor, a pulse device comprises a bell jar, a siphon tube, a siphon damage tube, a pulse water distributor further comprises a sewage inlet and a reflux sludge inlet, sewage through sewage inlet entering into pulse device, reflux by reflux sludge inlet entering into pulse device, sewage and sludge mixed in the bell jar of pulse device, a siphon through the siphon tube of the mud-water mixture in the bell through hole tube water distributor to the biological selecting tank in, siphon breaking tube damage siphon tube for working a need of siphon condition so that the siphon damage tube is in the pulse intermittent working status. The sludge-water mixed with good effect, biological high selectivity, no energy consumption, small floor area, convenient for daily of good effect of operation, maintenance and management.
NOVELTY - This utility new type claims a one wood stack channel and gate integrated purifying water of device, the device comprising a wood stack channel and multi-biological grid, a biological grid comprising a base, a float grass type fish groove and net-shaped component, a float grass type of multi-water grass type blade, the bottom end of each water grass type blade fixed on the said upper base, and the top end of each water grass type blade set with one small hole, each small holes with the net member connecting with the multi-rope microorganism carrier filler, the bottom of said wood stack channel set with multi-beam channel, the bottom of each beam is welded with a fixing ring, a fixing ring and the mesh member connecting with a rope. This utility new type the wood stack channel underwater space and biological grid technique can solve the valid biological grid technology landscape is not strong, the problem of the traditional landscape facility comprises a water purifying function, it can valid improve the municipal water quality purification system of landscape, treatment of municipal scenic water provide technical support.
NOVELTY - A hot circulating heating of one soft marsh gas pool, mainly comprising a heat collecting hot circulating heating tube and soft biogas fermentation bag, wherein the upper soft biogas fermentation bag body hot circulating heating tube inlet and hot circulating heating tube outlet, the lower part of the bag body is provided with a hot circulating heating tube, hot circulating heating tube by one tube of hot water circulating heating tube inlet device the other one hot water return pipe through the hot circulating heating tube outlet of hot device, the upper water return tube set with pipeline booster pump. Pipeline booster pump of the hot water circulating flow in the heat collecting device entering into hot circulating heating tube, hot exchange for of material liquid in the soft biogas fermentation bag repeatedly and circularly heating, accelerate organic decomposition causing fast produce marsh gas. This utility new type high yield, but also can reach the temperature generating temperature time is too low, the soft marsh gas pool of full year;
NOVELTY - The bentonite-based sludge preparation method involves mixing 1-5 wt.% bentonite, 5-20 wt.% sludge obtained by filter pressing dehydration, 10-25 wt.% fine sand, 35-50 wt.% aggregate, 15-25 wt.% cement, and 2.5-10 wt.% water as base material, adding 0.5-1.0 wt.% water reducing agent, stirring, and mixing uniformly. The mixed material is extruded to form concrete mold. The concrete mold is stood under normal condition and maintained for 28 days to obtain the finished product.    USE - Preparation method for bentonite-based sludge of concrete used for e.g. side slope, desert greening, road greening.    ADVANTAGE - Provides economical and environment-friendly concrete by ensuring saving resources and eliminating problem of sludge incinerating ash discharge of subsequent processing.
NOVELTY - A Bacillus stratosphericus strain SC-12 with preservation number CGMCC 7622 is new.    USE - A Bacillus stratosphericus strain SC-12 with preservation number CGMCC 7622 for producing acetyl-coenzyme A carboxylase enzyme, promoting plant growth, and growing solanaceous vegetable in greenhouse (all claimed).    ADVANTAGE - The Bacillus stratosphericus strain SC-12 with preservation number CGMCC 7622 improves ability of plants to adapt adverse environments, and increase pollution.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) application of Bacillus stratosphericus strain SC-12 with preservation number CGMCC 7622 in growing solanaceous vegetable in greenhouses which promotes adverse environment; and (2) preparing growth-promoting fertilizer which involves inoculating 1x 108/ g Bacillus stratosphericus strain SC-12 with preservation number CGMCC 7622 in pig manure composting straw stack.    DESCRIPTION OF DRAWING(S) - The drawing shows a transmission electron microscope image of Bacillus stratosphericus strain SC-12 with preservation number CGMCC 7622.
NOVELTY - This utility new type claims a film carrying one hydrogen tail gas in recycling methane of device, comprising a purifying unit, a compression unit, liquefied unit and a storage unit, wherein the purifying unit, the raw material gas for process operation, and the rear of purifying gas to liquefied unit, compressing unit, for taking the nitrogen pressurizing cooling operation, and rear refrigeration by expansion of low temperature gas to the liquefaction unit, liquefaction unit, of LNG for the raw material gas from the purifying unit of and receive from the compressed unit of low temperature gas, rear control raw material gas at low temperature gas cooling process separating operation, and the separating and conveying to the storage unit, the storage unit, the liquefied unit for output of LNG storage. This utility new type can be the film in extracting hydrogen tail gas recycling a large amount of methane can be valid energy-saving measure of enterprise, reduces the resource consumption of the energy of the enterprise.
NOVELTY - Genetically engineered cyanobacteria involves utilizing genes of the cyanobacterium Anabaena sp. strain PCC 7120, where the upstream primer has 22 nucleobases (SEQ ID NO: 2) and downstream primer has 19 nucleobases (SEQ ID NO: 3). pRL-489 plasmid is inserted in reverse shuttle of Escherichia coli. Vector is added in BGll culture medium containing nitrogen screening transformants.    USE - Genetically engineered cyanobacteria used for preparing biological diesel oil and essential fatty acid.    DETAILED DESCRIPTION - An upstream primer has 22 nucleobases i.e. gatgggcaagccacaaaagacc (SEQ ID NO: 2) and downstream primer has 19 nucleobases i.e. aggatccgcgggacgagaac (SEQ ID NO: 3).
NOVELTY - A hydrogen storage electrode alloy contains magnesium, titanium, nickel, aluminum, silicon, and multi-rare earth element than lanthanum e.g. samarium, yttrium, neodymium, and/or praseodymium in which atomic ratio of rare earth elements other than lanthanum is 0.4-0.6.    USE - A hydrogen storage electrode alloy for nickel-MH secondary battery (claimed).    ADVANTAGE - Corrosion resistance and electrochemical cycle stability of alloy are improved while maintaining electrochemical capacity, protection of inert gases can be suppressed, and preparation process is easy and avoids increase in investment of device. The secondary battery has high capacity and long life.    DETAILED DESCRIPTION - A hydrogen storage electrode alloy contains magnesium, titanium, nickel, aluminum, silicon, and multi-rare earth element than lanthanum e.g. samarium, yttrium, neodymium, and/or praseodymium according to formula RE1-xMgxTiyNizAlmSin in which atomic ratio of rare earth elements other than lanthanum is 0.4-0.6.    x=0.2-0.3;    y=0.02-0.08;    z=3-3.5; and    m, n=0.05-0.15.    An INDEPENDENT CLAIM is included for preparation of hydrogen storage electrode alloy which involves performing induction heat-melting of alloy under inert gas, placing molten alloy directly into water-cooled copper mold under inert gas in a furnace to cool to room temperature to obtain alloy ingot, and homogenizing by heat-treating in vacuum furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows an X-ray diffraction spectrum of the hydrogen storage electrode alloy after annealing and quenching. (Drawing includes non-English language text).
NOVELTY - A cefatrizine propylene glycol is prepared by adding water and/or organic solvent in cefatrizine methanol adduct, adding salt-forming agent which is metal (M) compound, dropwise adding solvent (A) to obtain cefatrizine M salt A adduct, dissolving in acid, adding water, adding decolorizing solubilizer (A), adjusting pH using alkali to obtain cefatrizine A adduct, dissolving cefatrizine A adduct or cefatrizine M salt A adduct in acid and water, adding 1,2-propylene glycol, and adjusting pH using alkali.    USE - Preparation of cefatrizine propylene glycol (claimed).    ADVANTAGE - Cefatrizine propylene glycol has high purity, good quality, and high yield. Process is simple, convenient, low cost and environment-friendly.
NOVELTY - A paraffin is manufactured by reductive reaction which advances olefin and hydrogen in gaseous-phase state in presence of reduction catalyst in catalyst tank (11) in which reduction catalyst contains catalyst area (13C-13E) containing diluted medium in which catalyst particles which have catalyst activity do not have catalyst activity, and arranging catalyst area that it may go downstream from upstream of the flow of gas in catalyst tank and blend ratio of diluted medium may fall in steps.    USE - Manufacture of paraffin e.g. ethane and propane.    ADVANTAGE - The method manufactures paraffin when reducing a high concentration olefin with hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the paraffin manufacturing apparatus.    Hydrogen cylinder (1)    Pressure reduction valve (2)    Flowmeter (3)    Catalyst tank (11)    Catalyst area (13C-13E)    Paraffin manufacturing apparatus (X2)
NOVELTY - Producing an aquatic protein hydrolyzate with enzyme hydrolysis, comprises adding a natural antioxidant comprising a marine algae extract to the protein enzyme reaction mix, before or during the hydrolysis reaction.    USE - The process is useful for producing an aquatic protein hydrolyzate, which is useful: in a product including food product, a food supplement, pet food, animal feed, fish feed, fertilizer, cosmetic products, pharmaceutical preparations, nutraceutical preparations and medicaments, and in cosmetics such as creams, lotions, shampoos, gels, pastes and masks; and for enhancing or suppressing appetite (all claimed) and preventing or treating hypertension or high blood pressure, thrombosis, immune system disorder, degenerative diseases, diabetes and cancer. Test details are described but no results given.    ADVANTAGE - The process prepares aquatic protein hydrolyzate with improved organoleptic properties and quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an aquatic protein hydrolysate produced by the process, where the protein hydrolysate comprises a natural antioxidant comprising marine algae extract such as Fucus vesiculosus extract.
NOVELTY - Device contains an inertial accumulator connected mechanically to an electric engine-generator and a thermal engine connected mechanically to the second electric generator; a gasifying unit included into a machine for solid domestic waste sorting, a machine for solid domestic waste drying, a machine for solid domestic waste grinding, a machine for solid domestic waste charging and a gasifier for solid domestic waste. The latter has an output for gasification product and a discharge port for slag removal; it contains a sealed enclosure of the gasifier with one or several plasma guns installed in its wall. The gasifier also includes a compressor connected to the output for gasification product and a storage tank for gasification product connected to the compressor output. Fuel feed input of the thermal engine is connected to the output of the storage tank for gasification product; the electric engine-generator through a frequency converter is connected electrically in parallel to the second electric generator and in parallel to the output terminals of the device.    USE - Electricity.    ADVANTAGE - Improved operation speed.1 dwg
NOVELTY - A renewable heating fuel oil composition comprises a) a first component comprising a bio-oil derived from the thermochemical conversion of biomass, where the bio-oil contains: i) an oxygenated component having an oxygen content of at least 5 wt.%, and ii) a non-oxygenated component having an aromatic content of at least 25 wt.%; b) a second component comprising an oxygenated acyclic component comprising open chain molecules having greater than or equal to 12 carbon atoms per molecule.    USE - As renewable heating fuel oil composition used as a fuel for a furnace, boiler, combustor, thermal oxidizer, turbine, or stove (claimed).    ADVANTAGE - The stable and valuable bio-oil produced from biomasses has sufficient heating value and stability to be useful as heating oil, alone or in combination with an oxygenated acyclic component, without the need to hydrotreat the bio-oil or use a similar deoxygenating process. The renewable heating fuel oil composition has a heating value of at least 14000 (preferably at least 15000, especially at least 16000) Btu/lb; and stability parameter of less than 15 (preferably less than 10) centipoises/hour (cp/hour). The thermochemical conversion of the biomass to produce the bio-oil does not include an oxygen-removing hydrotreatment step. At least 50 (preferably at least 60) wt.% of the renewable heating fuel oil composition has a boiling point of 180-380 degrees C.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of renewable heating fuel oil composition involving a) converting at least a portion of the biomass in an oxygen-poor environment in the presence of a catalyst material at 200-1000 degrees C to produce a reaction product stream containing the bio-oil; and b) separating the bio-oil from the reaction product stream, where the steps (a) and (b) do not include an oxygen-removing hydrotreatment step.
NOVELTY - Processing (m1) a biomass within an apparatus comprising a heat transfer fluid in a closed-loop heat transfer circuit, involves: torrefying the biomass utilizing heat by extracting heat from the heat transfer fluid, where the torrefying produces a torrefaction gas and the biofuel; exothermically reacting the torrefaction gas; and heating the heat transfer fluid from the reacted torrefaction gas.    USE - For processing biomass within apparatus having heat transfer fluid in closed-loop heat transfer circuit, and converting biomass into a coal-like biofuel (claimed).    ADVANTAGE - The method is inexpensive to implement and produces a fuel that is compatible with apparatus that use conventional solid fuels. The biofuel thus produced may have an energy density superior to lower grade fossil coals, and physical properties, such as density, grindability, or water tolerance, that are compatible with industry needs. The method overcomes the disadvantages of the prior art by utilizing the energy content in gasses driven off during torrefaction to operate the biomass-to-biofuel process, resulting in a self contained fuel production facility, requiring only biomass for steady state operation. Specifically, torrefaction typically produces low energy value gas products, i.e. acetic acid and methanol, which contain energy which has been lost to the solids. The method recovers the thermal energy in the gas and/or converts the gas to electrical energy in a heat engine.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for converting (m2) a biomass into a coal-like biofuel, involving: drying the biomass to form steam; and providing heat from the steam to a heat engine.
NOVELTY - Producing (M1) an organic liquid fuel involves: providing an organic compound selected from alkanes, alkenes, alkynes, and aromatics to an anode electrode comprising a metal oxide catalyst disposed on an anode side of an electrolyte membrane, producing an organic liquid fuel and electrons on the anode side; and conducting the electrons to a cathode electrode disposed on a cathode side of the electrolyte membrane, thus transforming water provided to the cathode side to hydrogen gas and hydroxide ions, where the steps are carried out at less than or equal to 160 degrees C.    USE - For producing organic liquid fuel preferably alcohol selected from methanol, ethanol, propanol and butanol; aldehydes and organic acids (claimed).    ADVANTAGE - No organic compound separation is needed, especially at the anode, because the high oxidative oxygen is generated on site, the reaction temperature is less than 160 degrees C and is as low as room temperature, the cathode produces hydrogen, which is also a fuel for low temperature fuel cells or for blending with methane for combustion to reduce NOx emissions, the system is either an alkaline or acidic environment, the anode catalyst is a metal oxide, which is regenerated by an electrolysis process, and the entire cell structure is easy to scale-up.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing (M2) hydrogen involving: providing the organic compound to the anode electrode comprising the metal oxide catalyst disposed on the anode side of the electrolyte membrane and oxidizing the organic compound, producing the electrons on the anode side; and conducting the electrons to a cathode electrode disposed on a cathode side of the electrolyte membrane; providing water to the cathode side of the electrolyte membrane; and transforming the water to H2.
NOVELTY - Pre-treating lignocellulosic biomass comprises chemical oxidation of biomass with combined action of alkaline hydrogen peroxide at a concentration of between 0.1 and 10% and using high pressures and moderate temperatures.    USE - The method is useful for pre-treating lignocellulosic biomass; delignifying lignocellulosic biomass or lignocellulosic material prior to the enzymatic hydrolysis in order to produce fermentable sugars; for optimizing results of enzymatic hydrolysis, with a view to the production of ethanol; and for delignifying recalcitrant lignocellulosic biomass, such as agro waste products, rice husk, sugarcane bagasse, wheat straw, grape pomace, citrus peels, and bagasse beet (all claimed).    ADVANTAGE - The method is used to partially delignify the substrates, thus improving the accessibility to enzymatic attack for producing fermentable sugars, and obtaining hydrolysis yields close to 100%.
NOVELTY - The method involves gasifying waste resin material (1) including organic components and radioactive agents at temperature between 600 to 950 degree Celsius in a reactor e.g. fluidized bed reactor (2), to form a gaseous material (3). The gaseous material is cooled by a water quenching unit (4), so that the temperature is reduced between 300 to 500 degree Celsius after the cooling. Solid fraction (8) including radioactive agents is removed from the gaseous material to form treated gaseous material (7).    USE - Method for treating waste material. Uses include but are not limited to a resin from nuclear power plant, industrial protective clothing, a contaminated wood and a contaminated vegetable matter e.g. corn, straw and hay.    ADVANTAGE - The method allows a user to treat the contaminated waste material in an easy, cost-effective and energy-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for treating waste material.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an apparatus for treating waste material.    Waste resin material (1)    Fluidized bed reactor (2)    Gaseous material (3)    Water quenching unit (4)    Treated gaseous material (7)    Solid fraction (8)
NOVELTY - A composite substance comprises: particles of a metal or an oxide of the metal dispersed in a porous silica matrix.    USE - For oxidizing a fuel; for methanol synthesis and reforming, steam and CO2 reforming of methane, Fischer-Tropsch synthesis, CO oxidation, catalytic biomass tar decomposition, SO2 oxidation, NO reduction, methane oxidation and chemical looping combustion (all claimed).    ADVANTAGE - The method is inexpensive, readily scalable and use moderate temperatures and pressures. The oxide of the metal may be usable as an oxidant in chemical looping combustion. The composite substance is prepared by a simple and efficient method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparing (M1) a composite substance comprising particles of an oxide of a metal dispersed in a porous silica matrix involves: preparing a solution comprising a soluble salt of the metal and a surfactant; adjusting the solution to a basic pH at which a hydroxide of the metal precipitates from the solution; preparing an aqueous suspension of the hydroxide of the metal, where the suspension is at pH greater than 7; adding to the suspension, with agitation, an alkoxysilane, so as to form composites comprising the hydroxide of the metal at least partially coated with silica; and calcining the composites obtained in fourth step so as to produce the composite substance; and    (2) oxidizing (M2) a fuel involving: exposing the fuel to a composite substance at sufficient temperature for combustion of the fuel.
NOVELTY - Producing hydrogen involves: contacting a nanoparticle and a metal complex catalyst in an aqueous medium to form a mixture in the presence of a source of electrons; and exposing the mixture to electromagnetic radiation having at least a wavelength in the absorption profile of the nanoparticle, where upon exposure to the electromagnetic radiation the nanoparticle generates an electron that can reduce, in the presence of the catalyst, a proton in the aqueous medium, and the source of electrons reduces the nanoparticle after reduction of the proton, such that hydrogen is produced.    USE - For producing hydrogen (claimed), useful as clean-burning fuel.    ADVANTAGE - The method provides an active and robust aqueous system for the photogeneration of hydrogen from water using nanoparticles, e.g. CdSe nanocrystals, as a photosensitizer and a catalyst e.g. Ni2+ thiolates. This system generates over half a million turnovers of H2 with no deterioration of activity (event if the nanoparticles agglomerate), and thus has promise for incorporation into full artificial photosynthetic systems. The method uses the combination of semiconductor nanoparticles as light absorbers and simple, solution-based, and earth-abundant metal catalysts for the photogeneration of hydrogen exhibiting the observed durability and activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composition for producing hydrogen comprising the nanoparticle; the metal complex catalyst; the source of electrons; and the aqueous medium, where the nanoparticle, metal complex catalyst, and aqueous medium are present as a mixture.
NOVELTY - A heat insulating material has contraction of 4% or less, when heated at 1000 degrees C for 3 hours, heat conductivity of 0.1 W/mk or less at 600 degrees C, pore volume of 27 vol.% or more, and pore diameter of 100 nm or less.    USE - Heat treatment furnace is used for insulation of furnace for steel manufacture, ceramic manufacture, and fuel cell. Uses include but are not limited to ladle furnace, glass melting furnace, cement kiln, carburizing furnace, metal sintering furnace, holding furnace, fuel heating furnace, non-ferrous metal furnace, induction treatment furnace, heat treatment furnace, etc.    ADVANTAGE - The heat treatment furnace has excellent heat resistance even at 1000 degrees C, and is stably manufactured with ensured strength.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of heat insulating material.
NOVELTY - A Rhodobacter azotoformans strain DS-EBN-CJY33 (KCTC 12275BP), is new.    USE - The R.azotoformans strain DS-EBN-CJY33 is useful for preparing organic fertilizer (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) organic fertilizer comprising R.azotoformans strain DS-EBN-CJY33 or supernatant of culture solution which is obtained by culturing the R.azotoformans strain; and (2) method for preparing the organic fertilizer involves isolating the R.azotoformans strain DS-EBN-CJY33, culturing the isolated strain in culture medium, and preparing organic fertilizer by adding the cultured solution into a centrifuge and obtaining a strain and culture supernatant by isolating the culture solution into the strain and the culture supernatant.
NOVELTY - Disclosed is a high-speed compost preparation method using an AT-18 enzyme composition, including: adjusting the carbon/nitrogen ratio and the water content of an organic waste, placing it into a fermentation machine, heating from 25 DEG C to 80 DEG C in 1 hour inside the fermentation machine, keeping for 3 hours at the temperature of 80 DEG C and cooling the fermentation machine down to the temperature of 55 DEG C for 15 hours, adding an AT-18 enzyme composition whose amount is 1% to 5% of total amount of the organic waste and the AT-18 enzyme composition to the fermentation machine, stopping heating of the fermentation machine, and using a mechanical agitation manner to continuously carry out agitation and/or using a mechanical ventilation to increase oxygen supply for about 18 hours so as to decompose and mature the organic waste to be an organic fertilizer.
NOVELTY - This invention relates to a facultative fermentation treatment method for kitchen waste and its system, in which a kitchen waste treatment step, a waste water treatment step, and a waste gas treatment step are used correspondingly with a pretreatment unit, an automatic oil/water separator, and a fermentation collection unit, so as to achieve the effect of automatic massive treatment of kitchen waste and production of solid fertilizer and liquid fertilizer, in which an effective microbe colony is added to shorten the fermentation cycle and reduce the odor; in addition, a biological deodorizing filter tower is used to remove the odor in the waste gas before discharge, thereby minimizing the effect to the environment during the treatment of the kitchen waste effectively.
NOVELTY - This invention relates to a liquefied organic substance decomposition device and more particularly to a liquefied organic substance decomposition device with high efficiency and homogeneous treated substance. It mainly consists of a vertical cylindrical tank which has at its bottom a liquid drainage valve connected with a liquid backflow pipe, on which a water pump is disposed. The terminal portion of the liquid backflow pipe is further connected with a water spraying unit disposed at the top of the tank interior. With the above-mentioned design, this invention can rapidly perform decomposition of a large amount of organic substance and increase the uniformity of decomposition, without causing the environmental problems such as odor and mosquitoes/insects; in addition, it can be useful with a smaller decomposition site, so as to greatly increase its economic benefits.
NOVELTY - The invention relates to a process and an installation for controlled inoculation of a liquid mycelium into plastic bags filled with sterilized compost, intended for the culture of edible and therapeutical mushrooms. According to the invention, the process consists in inoculating liquid mycelium by automatically making, using an effector of a robot, successive and progressive in-depth breakthroughs into some cylindrical plastic bags filled with sterilized compost, during inoculation the operation time of a membrane pump being correlated to the injection flow rate, in order to provide the desired amount of inoculum, as to achieve a homogeneous distribution thereof in each bag, provided with a distribution network with tree-like structure. The installation, as claimed by the invention, comprises an effector, a distribution-dosing system (3) and an accessory support (8), where the effector consists of an intermediate reservoir (1) provided with a stirrer (2) driven by an electric motor (3) and a worm reducer (4), the distribution-dosing system (3) consisting of a membrane pump (2), a three-way flow divider (6), a hose network (7) and three injectors (9) in connection whereof a covering system is mounted, said system comprising a flap (10) covering the injectors (9), entrained by some levers (14) actuated by a coil (15).
NOVELTY - Crude glycerin purification involves preparing aqueous solution containing 70-85 % of glycerol which is derived from transesterification of biodiesel. Two operation units are provided for physical adsorption and evaporation pretreatment. The formed crude glycerin is catalyzed by acidifying with acetone and 1,2,3-propanediol for forming (2,2-dimethyl-1,3-dioxolan-4-yl)methanol under vigorous stirring. The formed dioxolan solution is treated through solid-liquid separation and chemical adsorption.    USE - Method for purifying crude glycerin.    ADVANTAGE - The method provides purified glycerin with high yield and high purity in a simple manner by facilitating perfect precipitation of organic and inorganic salts, usually that are difficult to remove. The liquid phase can be hydrolyzed concomitantly with evaporation of acetone to allow recovery of the starting material.    DETAILED DESCRIPTION - Crude glycerin purification involves preparing aqueous solution containing 70-85 % of glycerol which is derived from transesterification of biodiesel. Two operation units are provided for physical adsorption and evaporation pretreatment. The formed crude glycerin is catalyzed by acidifying with acetone and 1,2,3-propanediol for forming (2,2-dimethyl-1,3-dioxolan-4-yl)methanol under vigorous stirring. The formed dioxolan solution is treated through solid-liquid separation and chemical adsorption. The formed reaction product is hydrolyzed which includes (2,2-dimethyl-1,3-dioxolan-4-yl)methanol or 1,2,3-propanediol and acetone by simultaneous evaporation of acetone and by adding water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the crude glycerin purification method. (Drawing includes non-English language text).
NOVELTY - The conversion system comprises an ion conductive membrane to separate oxygen in the air, a burner for combusting the oxygen separated from the membrane, and a dry-reformer for converting carbon monoxide and hydrogen to methane by performing oxy-combustion in a combustor. The conversion system further comprises a synthesizer for converting hydrogen to methanol, ketone or carbonate, and a mixer for mixing oxygen generated in electrolytic purification and oxygen separated from the ion conducting membrane. The mixer is connected with a tri-reformer.    USE - The conversion system is useful for converting carbon dioxide (claimed) into a fuel or a useful chemical substance.    ADVANTAGE - The conversion system affordably converts the carbon dioxide into the fuel in an efficient manner.    DETAILED DESCRIPTION - The conversion system comprises an ion conductive membrane to separate oxygen in the air, a burner for combusting the oxygen separated from the membrane, and a dry-reformer for converting carbon monoxide and hydrogen to methane by performing oxy-combustion in a combustor. The conversion system further comprises a synthesizer for converting hydrogen to methanol, ketone or carbonate, and a mixer for mixing oxygen generated in electrolytic purification and oxygen separated from the ion conducting membrane. The mixer is connected with a tri-reformer. A turbine of an oxyfuel burner discharges exhaust gas discharged from winding, and is connected to a generator for producing electricity. A heat exchanger is connected to a rear end of the oxyfuel burner.
NOVELTY - The apparatus has counter electrode (52) that is spaced apart from base material (15) and arranged in an inner side of a film-forming chamber (20). Voltage application portion (50) is connected to base material and counter electrode to apply voltage between base material and counter electrode inside film-forming chamber so as to generate plasma. The electric potential of frame (30) installed below grounding potential is made higher than electric potential of base material, when voltage is applied by voltage application portion between base material and counter electrode.    USE - Apparatus such as film-forming apparatus used for manufacturing separator for fuel cells.    ADVANTAGE - Since the frame is provided in the film-forming chamber, the in-plane temperature distribution of the base material can be homogenized during film-forming and the thickness of carbon thin film can be homogenized and adhesiveness can be improved. Since the non-uniformity of in-plane temperature distribution can be suppressed in the base material, the deformation of the undesirable base material resulting from local temperature rising can be suppressed. Since the electrical-connection portion is formed of the metal material, the connection state of the frame to grounding potential is ensured by the electrical-connection portion.    DETAILED DESCRIPTION - The base material is accommodated in the inside of film-forming chamber formed with midair so as to form the carbon containing thin film into a preset film. The frame is spaced apart from the outer periphery of the base material surrounded in the interior of film-forming chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the film-forming apparatus. (Drawing includes non-English language text)    Base material (15)    Film-forming chamber (20)    Frame (30)    Voltage application portion (50)    Counter electrode (52)
NOVELTY - A catalytic transfer hydrogenation of biodiesel is performed by carrying out ester exchange reaction using base-catalyzed process, adding methanol and rapeseed oil in glass flask with ratio of 6-10, adding sodium hydroxide as catalyst, controlling temperature at 55-60 degrees C, stirring rate to 600-800 rpm, and time to 90 minutes, carrying out liquid separation, washing with water, filtering, drying, purifying, refining, placing in 250 ml glass flask with reflux condenser, adding hydrogen donor, Raney nickel (Raney-Ni) as catalyst, and aqueous solvent as reaction medium, and reacting at 85-90 degrees C.    USE - Catalytic transfer hydrogenation of biodiesel (claimed).    ADVANTAGE - Process improves oxidation stability.    DETAILED DESCRIPTION - A catalytic transfer hydrogenation of biodiesel is performed by carrying out ester exchange reaction using base-catalyzed process, adding methanol and rapeseed oil in glass flask with ratio of 6-10, adding sodium hydroxide (NaOH) as catalyst, controlling temperature at 55-60 degrees C, stirring rate to 600-800 rpm, and time to 90 minutes, carrying out liquid separation, washing with water, filtering, drying, purifying, refining, placing in 250 ml glass flask with reflux condenser, adding hydrogen donor, Raney nickel (Raney-Ni) as catalyst, and aqueous solvent as reaction medium, reacting at 85-90 degrees C with stirring speed of 800 rpm, adding excess Webster's reagent in biodiesel samples, adding carbon tetrachloride (CCl4) solvent, reacting for 1 hour, adding excess potassium iodide (KI) and iodine trichloride (ICl3) to convert into iodine, titrating using standard sodium thiosulfate (Na2S2O3) solution, and carrying out blank experiment.
NOVELTY - Pre-processing method for production of fuel ethanol using cassava, involves (a) washing cassava, drying, smashing, passing by 60-100 meshes sieve, sealing and drying product, and (b) mixing cassava powder with 1-5% acid solution in a solid-to-liquid ratio of 1:10-1:15, and processing mixture at 40-50 degrees C for 10-15 hours.    USE - The pre-processing method is useful for production of fuel ethanol using cassava (claimed).    ADVANTAGE - The method reduces crystallization status of cellulose and raw material for enzyme hydrolysis of resistance to improve fermentation rate of ethanol.
NOVELTY - Method for producing biodiesel using lipase and waste oil, involves weighing mesocellular foam (MCF) and lipase, adding phosphoric acid buffer solution, stirring and mixing solution, performing centrifugal separation, collecting precipitate, washing precipitate using phosphoric acid buffer solution, drying precipitate, sealing and storing tube in refrigerator, performing waste oil conversion reaction, mixing waste oil and methanol, adding obtained mixture into flask, adding loaded lipase and preservative film, and performing magnetic force stirring reaction.    USE - The method is useful for producing biodiesel using lipase and waste oil (claimed).    ADVANTAGE - The method provides stability, improves tolerance ability, and prolongs service life.    DETAILED DESCRIPTION - Method for producing biodiesel using lipase and waste oil, involves (a) weighing 0.5 g mesocellular foam (MCF) and 0.5 g lipase, adding 100 ml phosphoric acid buffer solution, stirring and mixing solution by magnetic force at room temperature, maintaining solution for 10-12 hours, performing centrifugal separation at 5000 revolutions per minute (rpm) for 5 and 10 minutes, collecting precipitate, washing precipitate using phosphoric acid buffer solution to at least 2 times, drying precipitate at room temperature in vacuum drier for 20-24 hours, adding 20 ml to tube, sealing and storing tube in refrigerator at 4 degrees C, and (b) performing waste oil conversion reaction, mixing waste oil and methanol in a mass ratio of 6-8, adding obtained mixture into 50-100 ml flask, adding 0.1-0.2 g loaded lipase and preservative film, and performing magnetic force stirring reaction at room temperature for 48-60 hours.
NOVELTY - Method for preparing mosquito attractant involves freezing soaking solution, and divided into ten equal parts in natural environment, and adding distilled water, maintaining the mixture at 20-25 degrees C, comparing the soaking solution and selecting valid solution, screening Burkholderia strain by selecting positive interaction of solution, adding different concentration from high to low order of acetone, and xylene to the solution and adding deionized water, and increasing the attracting force by adding the acetone and xylene process.    USE - The method is useful for preparing mosquito attractant (claimed).    ADVANTAGE - The method enables to prepare product simply, environmentally-friendly, and causes fewer side effects.
NOVELTY - The device has a self-maintaining reactor (2) which is located at downstream of tank main portion containing micro-algae. A heterotrophic reactor (4) is arranged in downstream and is connected with self-maintaining reactor for heterotrophic growth of micro-algae and accumulation of lipid. A micro-algae concentration control system is configured to monitoring the concentration of micro-algae concentration in light heterotrophic reactor to control light at dilution ratio.    USE - Micro-algae culture device for preparing algae used for bio-diesel.    ADVANTAGE - The high growth rate and high lipid concentration can be achieved. The investment and the operation cost are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of micro-algae culture device.    Feeding control valve (1)    Self-maintaining reactor (2)    Micro-algae concentration sensor (3)    Heterotrophic reactor (4)    Micro-algae concentration controller (5)
NOVELTY - This utility new type relates to one for a biogas nutrient liquid of preparation device, comprising a first-stage anaerobic fermenting tank, second level anaerobic fermentation tank and nutrient solution preparing tank, a first-stage anaerobic fermenting tank, second level anaerobic fermentation tank and nutrient solution allocation pool according to sequence through the corresponding pipeline of connecting process, a nutrition regulating pool according to sequence is divided into filter tank, extracting tank and diluting pond, a filtering pond is provided with a liquid inlet, a liquid inlet through the corresponding pipeline of connecting to a second level anaerobic fermentation tank and right lower middle part of side a positon filter tank and the extraction tank is connected to the top part of is provided with a first liquid flow port, a leaching tank and left side of side of connected of diluting pond lower positon middle part to the top part is provided with a second liquid flow port, a liquid inlet, a first liquid flow port and upper port is provided with a corresponding second liquid circulation filtering device. The device has simple structure, easy construction, nutrient solution preparation effect is good.
NOVELTY - This utility new type of belt seal feeding tube of methane tank, comprising a tank body with an inner cavity of the tank body and adjacent of water pressure, a tank body upper part of the inner cavity of lower part of the inner cavity of gas storage room, the tank body of fermentation room, said upper tank body is provided with a feeding channel, a discharging port and gas-guide tube, said inlet channel is set in the seal connecting with the feeding channel of the feeding tube. Feeding port of said feeding tube is set at upper part and big lower of one round seal cover, upper feeding tube near the inlet positon feeding tube surrounding one ring of annular groove. A feeding tube is connected with the feeding channel seal connecting the place of reinforcing tightness, the feed port is set one seal device, the feeding port of better. In addition, following a feeding tube entering into the tank body of the material liquid in the liquid level in the fermentation room, so that feeding of marsh gas raw material entering into the bottom of biogas slurry, it can make the process more fully of fermentation, improves.
NOVELTY - An Ochrobactrum anthropi 5753rd generation deposited as CCTCC: M2013549 is new.    USE - The O.anthropi is useful for preparing microbial fuel cell (claimed).    ADVANTAGE - The O.anthropi is capable of transferring an electron to extracellular electron acceptor under anaerobic condition, utilizes xylose as sole carbon source and produces electric energy with strong power generating activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of O.anthropi for preparing microbial fuel cell.
NOVELTY - Invention relates to agriculture. Method of obtaining biomineral fertilisers includes combination of dry or liquid mineral fertilisers and meliorants with microbial biomass; in the first version as microbial biomass used is microbiological fertiliser or preparation, created on the basis of agronomically useful microorganisms in form of dry fine-disperse powder with titre 102-105 kl/g, which is applied on dry mineral fertiliser or meliorant or introduced into liquid mineral fertiliser in dose 2-6 kg/t; in the second version, as microbial biomass used is microbiological fertiliser or preparation, created on the basis of agronomically useful microorganisms in liquid form with titre 104-107 kl/g, which is applied on dry mineral fertiliser or meliorant by fine-disperse spraying or is introduced into liquid mineral fertiliser in dose 1-4 kg/t.    USE - Chemistry.    ADVANTAGE - Invention makes it possible to increase efficiency of application of introduced into soil mineral fertilisers by crop plants to increase their productivity.2 cl, 15 tbl, 4 ex
NOVELTY - Preparation of mitiglinide calcium dihydrate involves reacting (S)-2-benzyl succinic anhydride with cis-octahydroisoindole in aromatic hydrocarbon solvent, heating at 45-50 degrees C to get clear solution, cooling the solution to 20-30 degrees C, separating unwanted regioisomer by filtration, adding aqueous alkaline solution to filtrate; separate the aqueous layer, treating aqueous layer with calcium chloride solution, and isolating mitiglinide calcium dihydrate.    USE - For the preparation of mitiglinide calcium dihydrate (claimed) which is used for the treatment of type 2 diabetes mellitus.    ADVANTAGE - The method is highly cost effective and industrially feasible in large scale production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the recovery of S-benzyl succinic acid, cis-octahydroisoindole from regioisomer (r1) involving reacting regioisomer (r1) in aqueous acid, heating to get clear solution, distilling out the acid, followed by addition of water, adjusting pH and recovering the S-benzyl succinic acid by filtration, basifying the filtrate, adding aromatic hydrocarbon solvent and distilled out completely, adding tetrahydrofuran solvent, adjusting pH with an acid, and recovering the cis-octahydroisoindole.
NOVELTY - The line has a gasification section comprising a tubular shaped gasification reactor provided with an outer heater to heat a carbonization product. An in-line cleaning section includes a first stage to remove hot crude gas in light hydrocarbon, and a second stage to condense the light hydrocarbon and water contained in biogases. The cleaning section comprises an outlet to output contaminants, where the cleaning section is connected to one branch of a recycling conduit connected to back side of a carbonation section.    USE - Line for processing waste containing predominantly plastics and cellulose.
NOVELTY - The system has a wood gas generator provided with a wood gas outlet that is connected to a wood gas cleaning unit. A wood gas inlet is connected to a cogeneration unit. The wood gas cleaning unit is coupled to a process water purification system.    USE - System for generating energy using wood chips.
NOVELTY - Detoxification of hydrolyzed lignocellulosic materials, involves obtaining hydrolyzate lignocellulosic material from biomass of hydrolysed product obtained from chemical treatment processes. The obtained material is treated by advanced oxidation and bioconversion, which are performed by acid hydrolysis with inorganic acids (0.1-75%) or enzymatic complex or polysaccharides fractions present in cellulose and hemicelluloses containing biomass. The obtained material is treated by advanced oxidation and bioconversion is performed at 30-280 degrees C for 1-120 minutes.    USE - Method for detoxification of hydrolyzed lignocellulosic materials.
NOVELTY - Tobacco stems treatment involves collecting tobacco stems, then crushing, and then performing high temperature and high pressure separating process. Tobacco stems, nutrient source and auxiliary materials are mixed in mass ratio of 70-75:10-20:10-20 with water (50-60%). Fermentation is carried out in fermentation tank maintained at 75 degrees C for 10 days and stirred twice in a day, then fermentation carried out at 45-55 degrees C for 5-10 days. The fermented material is dried to obtain final product.    USE - Method for treating tobacco stems (claimed) used for inhibiting pathogenic bacteria and virus.    ADVANTAGE - The tobacco stem treatment provides a product that promotes soil granule structure and fertility, improves soil microbial activity and tobacco yield and quality and prevents soil-borne disease.
NOVELTY - Preparing imatinib mesylate alpha-crystal involves reacting 4-((4-methylpiperazin-1-yl)methyl)-benzoic acid dihydrochloride (I) and thionyl chloride. The obtained reaction mixture is cooled to 10 degrees C and then filtered to obtain 4-((4-methylpiperazin-1-yl)methyl)benzoyl chloride dihydrochloride (II).    USE - Method for preparing imatinib mesylate alpha-crystal (claimed).    ADVANTAGE - The method enables to prepare stable and high yield imatinib mesylate alpha-crystal in simple, economic and eco-friendly manner.    DETAILED DESCRIPTION - Preparing imatinib mesylate alpha-crystal involves reacting 4-((4-methylpiperazin-1-yl)methyl)-benzoic acid dihydrochloride of formula (I) and thionyl chloride. The obtained reaction mixture is cooled to 10 degrees C and then filtered to obtain 4-((4-methylpiperazin-1-yl)methyl)benzoyl chloride dihydrochloride of formula (II). The obtained compound is reacted with N-(5-amino-2-methylphenyl)-4-(3-pyridyl)-2-pyrimidine-amine of formula (III) and pyridine. Water is added to reaction mixture and then evaporated under reduced pressure to obtain solid. Ethyl acetate is added to obtained solid and pH is adjusted to 7.5-8.0 with aqueous ammonia (25 %). Obtained reaction mixture is stirred overnight and then filtered to obtain imatinib of formula (IV). Imatinib and methanesulfonic acid is added in absolute ethyl alcohol. The reaction mixture is stirred, filtered and then crystallized to obtain imatinib mesylate crystal of formula (V).. An INDEPENDENT CLAIM is included for a method for preparing pharmaceutical composition, which involves:    (A) drying silica glue, microcrystalline cellulose and crospovidone at 105 degrees C to reduce water content to 1.0;    (B) sieving by 60 mesh sieve;    (C) weighing imatinib mesylate crystal, silica glue, microcrystalline cellulose, cross-linked povidone and magnesium stearate; and    (D) mixing uniformly to obtain water content of 1.5-2.0 to fill in capsule.
NOVELTY - Method for concentrating hydrogen iodide involves introducing concentrated sulfuric acid solution produced by Bunsen reaction into one side of the separation membrane in a membrane separation module, and introducing concentrated hydroiodic acid solution into another side of the separation membrane, such that the water in the hydroiodic acid solution is transmitted to other side of separation membrane module under osmotic pressure.    USE - Method for concentrating hydrogen iodide during thermochemical water-splitting hydrogen production process (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for concentrating hydrogen iodide.
NOVELTY - This new type utility claims one kind of poultry excrement fermentation tank excrement cleaning machine, comprising a front beam, a rear beam and the left and right side plate and several reinforcing support is composed of a rectangular frame, two ends of the frame is equipped with a roller, a front beam and rear beam square tube, multiple rotary shafts are uniformly installed on the front beam, the lower end of each rotating shaft is belt pulley, the upper end impeller, the impeller rotating diameter external front and back baffle plate, the impeller to rotate between the front baffle and rear baffle plate, welding a plurality of bolt set up on the front beam, a locker is used for traction of locking ring is welded on the bolt set up of two sides of the shovel plate and the ground form an angle of 20 degrees -40 degrees of spading, time using up the excrement cleaning machine two ends of idler wheel set of the two sides of the fermenting tank, the upper traction device of traction rope bolt buckle up the retaining ring, the electric motor is started, impeller rotating clockwise and counter-clockwise, the excrement cleaning machine is pulled slowly forward to push the excrement pushing, the impeller of centrifugal force produce, poultry excrement is throwing channel of the two sides of the upper cage frame and excrement cleaning machine, it saves labour, personal safety is ensured, and high.
NOVELTY - Preparing triazole fungicide compounds (III), comprises e.g. (i) adding mercaptomethane compounds (IV) into dimethyl carbonate, then adding tetrabutylammonium bromide catalyst, and reacting at 20-100 degrees C (preferably 60-80 degrees C) for 1-10 hours to obtain onium salt, (ii) adding the onium salt and an alkali into ketone compounds (I), and reacting at 30-120 degrees C (preferably 60-80 degrees C for 2-20 hours to obtain epoxy compounds (II), (iii) adding 1,2,4-triazole and an alkali into (II), and reacting at 60-200 degrees C (preferably 100-140 degrees C) for 2-20 hours (preferably 8-12 hours) to obtain final product.    USE - (I) are useful in agriculture (claimed).    ADVANTAGE - The method: has simple process, high safety, and high product yield; is a continuous two-step reaction process or one-pot synthesis; is environment-friendly and suitable for large scale production.    DETAILED DESCRIPTION - Preparing triazole fungicide compounds of formula (III), comprises (i) adding mercaptomethane compounds of formula (RSCH3) (IV) into dimethyl carbonate, then adding tetrabutylammonium bromide (TBAB) catalyst, and reacting at 20-100 degrees C (preferably 60-80 degrees C) for 1-10 hours (preferably 2-4 hours) to obtain onium salt, (ii) adding the onium salt and an alkali into ketone compounds of formula (I), and reacting at 30-120 degrees C (preferably 60-80 degrees C for 2-20 hours (preferably 5-10 hours) to obtain epoxy compounds of formula (II), (iii) adding 1,2,4-triazole and an alkali into (II), and reacting at 60-200 degrees C (preferably 100-140 degrees C) for 2-20 hours (preferably 8-12 hours) to obtain final product.    R = phenyl, chlorophenyl or alkyl;    R1 = phenylalkyl group of formula (a);    X = halo;    n = 0-2; and    R2 = 1-6C alkyl, halophenyl or 1-cyclopropylethyl.
NOVELTY - Preparation of N-(phosphonomethyl)iminodiacetic acid (PMIDA) involves reacting iminodiacetic acid, hydrochloric acid, and phosphorous acid with formaldehyde, separating the iminodiacetic acid and phosphorous acid, separating mother liquor of PMIDA, mixing rear and refluxing, and reacting for at least 30 minutes, at 100 degrees C, distilling to remove water, separating distillation residue and rest part of N-(phosphonomethyl) iminodiacetic acid with hydrochloric acid at 105-125 degrees C, and recycling the remaining solution.    USE - For preparing N-(phosphonomethyl)iminodiacetic acid used as herbicide intermediate (claimed).    ADVANTAGE - The method reduces waste water discharge, energy consumption and material consumption from the source, thus saves the investment and processing cost; and produces high yield of N-(phosphonomethyl)iminodiacetic acid.    DETAILED DESCRIPTION - Preparation of N-(phosphonomethyl)iminodiacetic acid (PMIDA) involves reacting iminodiacetic acid, hydrochloric acid, and phosphorous acid with formaldehyde at 105-125 degrees C, where mol ratio of iminodiacetic acid, hydrochloric acid, phosphorous acid and formaldehyde is 1:0.03-0.07:0-1.2:0-1.5, separating the iminodiacetic acid and phosphorous acid, separating mother liquor of PMIDA, mixing rear and refluxing, and reacting for at least 30 minutes, at 100 degrees C, distilling to remove water, separating distillation residue and rest part of N-(phosphonomethyl) iminodiacetic acid with hydrochloric acid at 105-125 degrees C, and recycling the remaining solution.
NOVELTY - A process for the production of biodiesel from microalgae Chlorella species in-situ involves: a) extracting the type of microalgae Chlorella species, and simultaneously subjecting to transesterification process; b) preparing a solution of potassium methoxide; c) separating the biomass from biodiesel filtrate; d) separating biodiesel from residual reactants and solvents; and e) forming microalgae biodiesel product.    USE - For the production of biodiesel from microalgae Chlorella species in-situ (claimed), where biodiesel is used as alternative energy source and as a substitute for fossil fuels; in the preparation of products of fine chemicals, in food additives element for humans and animals, for biosorption of heavy metals, and for carbon dioxide fixation.    ADVANTAGE - The extraction and transesterification processes take place simultaneously, so that the production process of biodiesel from microalgae is more efficient and economical. The method provides more efficient method to produce biodiesel from microalgae Chlorella species type, where the process of oil extraction and biodiesel production processes take place simultaneously and biodiesel yield values are obtained at 37.77%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a product of biodiesel obtained by the method, which has a dominant methyl ester, which is methyl palmitate (20.83%) and methyl palmitoleic acid (19.63%).
NOVELTY - Biofertilizer comprises mycorrhizal fungi and Bacillus sp. strain B46.    USE - The biofertilizer is useful for improving soil fertility and controlling diseases in agricultural crops, forest plants and various other plantations (all claimed) and disease causing pathogens, and improving disease resistance in plants chosen from soybean and chili.    ADVANTAGE - The biofertilizer is cost-effective, as the materials are easily available, and does not pollute crops, and hence is environmentally-friendly and safe, and plant products produced from the plants are safe for consumption, and thus the biofertilizer enables performing sustainable agriculture. The biofertilizer increases availability of nutrients to the plants and suppresses soil borne pathogens. The biofertilizer significantly reduces requirement of chemical fertilizers and pesticides. The biofertilizer has multifunctional and synergistic effects of both the fertilizer and pesticide, and hence has wider markets prospects among the farmers.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned biofertilizer, which involves (a) mixing the mycorrhizal fungi and Bacillus sp. strain B46 as biopesticide in a ratio of 32:26, and (b) adding carrier comprising natural materials chosen from kaolin, andosol and calcium carbonate mixed in a ratio of 2:1:1 to mixture obtained in the step (a) in a ratio of 49:51, where the biofertilizer has 15% moisture content, and is in the form of granules having diameter of 2 mm.
NOVELTY - Preparation of a bio-fertilizer comprises mixing local isolates of symbiotic microbes (such as Rhizobium leguminosarum, Rhizobium phaseoli, or Rhizobium japonicum), and non-symbiotic (such as Azotobacter chroococum, Azospirillum brasiliensis, Bacillus megaterium, Pseudomonas fluorescens, or Saccharomyces cerevisiae) with arbuscular mycorrhizal fungi (such as Gigaspora, Acaulospora, Glomus etunicatum, or Glomus manihotis).    USE - Method for the preparation of a bio-fertilizer used for non-legume crops (such as corn, spinach, or peppers), and legumes (such as soybeans, green beans, or lentils including Canavalia ensiformis) (claimed).    ADVANTAGE - The bio-fertilizer is microbes friendly and safe for the environment, increases productivity of plants, and has no toxic chemicals.
NOVELTY - Terrimonas ferruginea strain having a preservation number of KCTC 12269BP is new.    USE - The Terrimonas ferruginea strain is useful in a microbial agent for promoting growth and flocculation activity of microalgae such as Chlorella, preferably Chlorella vulgaris and for producing bio-diesel (all claimed).    ADVANTAGE - The Terrimonas ferruginea strain improves the growth rate of microalgae, and allows stable, mass production of biomass in an economical manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) promoting growth of microalgae comprising co-culturing the microalgae and the Terrimonas ferruginea strain; (2) promoting the flocculation activity of microalgae comprising adding mixed culture of microalgae and the Terrimonas ferruginea strain to a culture fluid; and (3) producing bio-diesel comprising co-culturing Terrimonas ferruginea strain and microalgae for producing a fatty phase, and converting fatty phase into bio-diesel.
NOVELTY - Integrated preparation of potash fertilizer using Baiyunebo potassium-rich slate comprises (a) selecting potassium-enriched slate, (b) pre-processing in a microwave, and (c) microbial leaching.    USE - The method is useful for integrated preparation of potash fertilizer using Baiyunebo potassium-rich slate (claimed).    ADVANTAGE - The method: is economical, has good economic benefit and does not cause pollution; utilizes microbial leaching and microwave pre-treatment, thus improving the efficiency and leaching rate; is short; and recycles the waste including tail ore base and potassium-rich slate in Baiyunebo region, thus enabling economic development.
NOVELTY - Trichoderma asperellum strain having the precipitation number of KCTC12231BP, is new.    USE - The Trichoderma asperellum strain is useful for producing ethanol (claimed).    ADVANTAGE - The strain can economically produce the bioethanol from the fibrous cell resources without the additional need of sugar and yeast with simultaneous saccharification.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing ethanol comprising performing a saccharification and fermentation process with Trichoderma asperellum cultivated in a biomass culture medium containing carboxy methycellulose, and collecting the ethanol.
NOVELTY - The wastewater treatment system comprises a membrane bio-reactor connected to a rear end of a sieving mode reaction bath for processing the water except for the microorganism, a separation film for disassembling a biochemical activity microorganism from an effluent flowed out of the sieving mode reaction bath, and a filter element for reducing the sludge density of the processing water. The filtered water is taken out from the sieving mode reaction bath and guided into a separate sieving room. The sieving mode reaction bath sets up the filter element in a gravity gradient portion.    USE - The wastewater treatment system is useful for separating a solid material from the wastewater including food wastewater and livestock wastewater.    ADVANTAGE - The system reduces the concentration of sludge, and improves the water quality in a cost-effective manner.    DETAILED DESCRIPTION - The wastewater treatment system comprises a membrane bio-reactor connected to a rear end of a sieving mode reaction bath for processing the water except for the microorganism, a separation film for disassembling a biochemical activity microorganism from an effluent flowed out of the sieving mode reaction bath, and a filter element for reducing the sludge density of the processing water. The filtered water is taken out from the sieving mode reaction bath and guided into a separate sieving room. The sieving mode reaction bath sets up the filter element in a gravity gradient portion in a sieving-separation film bio-process mode. A circulation pump circulates the processing water within the membrane bio-reactor with the sieving mode reaction bath. An INDEPENDENT CLAIM is included for a sewage disposal method.
NOVELTY - Fresh water microalgae culture comprises (a) producing lipid by culturing freshwater microalgae strains in wastewater, and (b) respectively recovering crystalline substance and amorphous substance in the culture fluid, where the wastewater is simultaneously processed to remove nitrogen, phosphorus, organic carbon and inorganic carbon in the wastewater during the microalgae culture process.    USE - The method is useful for producing biodiesel (claimed).    ADVANTAGE - The method is economical, ensures simultaneous fresh water microalgae culture and wastewater treatment, where the resulting biomass is suitable as biodiesel as renewable energy, soil conditioner and fertilizer.
NOVELTY - Manufacture of fuel cell anode metal support involves providing electrolytic solution containing metal ions on flexible and conductive bed, forming deposited layer by electrodeposition, and peeling off deposited layer from metal foil.    USE - Manufacture of fuel cell anode metal support (claimed).    ADVANTAGE - The method economically enables manufacture of fuel cell anode metal support having excellent strength, impact resistance, and crack resistance.
NOVELTY - Producing water-soluble monoammonium phosphate by using wet-process phosphoric acid comprises neutralizing wet-process phosphoric acid with ammonia gas, subjecting the slurry to solid-liquid separation, removing solid phase slag, collecting the filtrate, concentrating to obtain monoammonium phosphate slurry and drying to obtain water-soluble monoammonium phosphate.    USE - The method is useful for producing water-soluble monoammonium phosphate (claimed).    ADVANTAGE - The method produces solid phase slag, which is used for producing phosphorus-nitrogen fertilizer (claimed); does not require crystallization and filtration, reduces the discharge of tail gas and has good economic benefits; and utilizes high concentration water-soluble monoammonium phosphate production device, which has high production ability, low energy consumption.
NOVELTY - A cultivation material comprises 30-40 wt.% tea seed shell meal, 20-30 wt.% tea root meal, 10 wt.% cottonseed hull, 20 wt.% wheat bran, 6 wt.% corn flour, 2 wt.% tea seed meal, 1 wt.% gypsum powder, and 1 wt.% lime powder.    USE - Cultivation material used for cultivating abalone mushroom (claimed).    ADVANTAGE - The tea seed shells and tea root remove toxic antimicrobial material, allow degradation of macromolecules, and help absorb abalone hyphae. The cultivation material has reasonable ratio, bacteria feed permeability, water retention, high abalone production, biological efficiency of 98.7%-110.2%, and reduces cost of production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of tea seed shell meal comprising drying tea seed shell and crushing to 2-3 mm particle diameter;    (2) preparation of tea root meal comprising taking fresh root, drying, and crushing;    (3) manufacture of culture material comprising pre-wetting tea seed meal, tea root meal, and cottonseed hull in lime water for 2 hours, mixing, maintaining water content to 50-55%; mixing bran, corn powder, tea seed meal, gypsum powder, adding to pre-wet mixed material, slowly adding water, stirring while adding, and uniformly stirring, where water content of culture material in bag is kept at 63-65%; preparing polypropylene plastic bags at 17 cmx 35 cmx 0.005 cm dimension, filling bag with 1100-1200 g culture material, inserting ring on plastic cover, sterilizing at 100 degrees C for 10-12 hours and cooling to 25 degrees C or less; and    (4) cultivation of abalone mushroom comprising inoculating strain in plastic, placing bag in dark room at 22-24 degrees C, where humidity is 30-75%, culturing for 30-32 days, fruiting till plastic bag is covered with mycelium, removing bag, and carrying out fruiting management.
NOVELTY - Production of potassium sulfate and by-product lithium salt includes reacting lithium sulfate and sodium hydroxide, cooling, filtering, separating to obtain lithium hydroxide hydrate and sodium sulfate crystal; reacting sodium sulfate with potassium chloride, carrying out double-decomposition reaction, reacting with sodium chloride to obtain solution containing aphthitalite and sodium chloride, evaporating and concentrating, centrifuging, cooling, separating to obtain aphthitalite and mother liquor I; and reacting potassium chloride and aphthitalite, filtering and separating.    USE - Method for producing potassium sulfate and by-product lithium salt (claimed).    ADVANTAGE - The method avoids environmental pollution, and reduces production cost.    DETAILED DESCRIPTION - Production of potassium sulfate and by-product lithium salt comprises reacting lithium sulfate and sodium hydroxide to obtain mixed solution of sodium sulfate and lithium hydroxide, cooling to - 10-5 degrees C, filtering, separating to obtain lithium hydroxide hydrate and sodium sulfate crystal; reacting sodium sulfate with potassium chloride at room temperature, carrying out double-decomposition reaction, reacting with sodium chloride to obtain solution containing aphthitalite and sodium chloride, evaporating and concentrating, centrifuging, cooling, separating to obtain aphthitalite and mother liquor I; and reacting potassium chloride and aphthitalite at room temperature, filtering and separating to obtain potassium sulfate with mother solution II.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of potassium sulfate and by-product lithium salt production (Drawing includes non-English language text).
NOVELTY - This utility model claims a kind of organic fertilizer deodorization device, wherein it comprises a supporting wall, a ventilation base is set on the oxygen supplying pipe and a base, wherein the supporting wall and a ventilating tube, a supporting wall arranged in the ventilation tube two sides of ventilation and oxygen supply tube are uniformly distributed on the inner side inclined plane and the horizontal plane of the oxygen supply hole, a supporting wall is provided with an angle alpha, the range of angle alpha is 20-40 degrees, the upper surface of the base between the plane and the horizontal plane is provided with an angle (beta), the range of the angle beta is 10-20 degrees. This utility model has advantages of organic fertilizer without peculiar smell, smell, fermentation material can enter into organic fertilizer fermenting stage, the whole structure is simple, it is convenient to popularize and use.
NOVELTY - This utility model claims a method for organic fertilizer turning machine of greenhouse shed, comprising a supporting part, a turn planing, an automatic control cabinet, a supporting part comprises parallel first cross beam and the second cross beam and two supporting plates are respectively fixed on the two ends of the bottom end of the supporting plate are respectively provided with a driving wheel and a driven wheel, turn planing part comprises a supporting frame, a plane, one end of the supporting frame is connected with the first cross beam sliding connection, and the other one end of the movable support frame is connected with the turning plane, supporting frame is provided with a third motor, the third motor is connected with the first winding, the two ends of the first winding are respectively wound with a steel wire rope are respectively fixed on the two supporting plates in the opposite direction. The beneficial effect of the utility model is no need to enter into a room tent for operation, it only needs to carry out the automatic progressive turn planing, each row turn planing, automatically forward turn planing task is the next step, until the terminal to operate, high working efficiency by operating button, the machine of the automatic control cabinet manual part.
NOVELTY - The utility model relates to the technical field of sewage biochemical processing device, especially relates to a kind of sewage biochemical treatment nutrient culture device, comprising a feeding port, a liquid outlet of the fermentation tank, the fermentation tank is fixed is provided with a baffle plate for fermentation tank is divided into a fermentation chamber, a liquid storage cavity, the inclined baffle plate is provided with a fermentation tank, and one end is extended in the fermentation tank, and the other end is in the fermentation tank is connected with a motor output shaft of the stirring shaft, the stirring shaft is vertically set with the clapboard is set with a stirring blade on the upper part of the stirring shaft in the fermentation tank, wherein the stirring face of the stirring blade, the upper and lower stirring plane is provided with a bump, the upper part is provided with a connected with the fermentation chamber, a through hole on the clapboard of the liquor storage cavity. This utility model has simple structure, convenient operation, the raw material is waste, the resource can be recycled, the cost is saved.
NOVELTY - Electrolysis of coal slurry involves polishing titanium/nanotitanium dioxide-zirconium dioxide base material using sandpaper, then washing with distilled water and absolute ethanol, cleaning using hydrofluoric acid, deoiling using acetone and washing using anhydrous ethanol, preparing coal slurry by ball milling coal and adding sulfuric acid and catalyst, providing coal slurry into a diaphragm cell provided with two-electrode system, in which pre-treated base material is used as one electrode, applying current with voltage of 1.2 V and electrolyzing.    USE - Electrolysis of coal slurry used for producing hydrogen.    ADVANTAGE - The method enables production of 6 mL/cm2 hydrogen from the coal slurry.
NOVELTY - A cathode can, an anode can, a separator, an anode, and a cathode arranged in the form of a primary battery, is placed in sun, or under artificial light or illumination. The anode comprises aluminum-gallium nitride, indium phosphide, and gallium nitride. The anode is in electrical contact with carbon dioxide dissolved in the electrolyte. The anode is irradiated with light of wavelength 310-315 nm and carbon dioxide dissolved in the electrolyte solution is reduced on the cathode surface covered with a small amount of nickel metal particles to generate methane.    USE - Preparation of methane by carbon-dioxide reduction (claimed).    DETAILED DESCRIPTION - A cathode can, an anode can, a separator, an anode, and a cathode are arranged in the form of a primary battery, with the separator provided between the cathode and anode cans, and placed in sun, or under artificial light or illumination. The anode comprises 25-45 wt.% aluminum-gallium nitride (AlxGa1-xN, x is 0.1-0.25) and indium phosphide compound semiconductor, and 60-95 wt.% gallium nitride compound semiconductor and indium phosphide compound semiconductor material, in a ratio of 1-1.5:1. The anode is in electrical contact with carbon dioxide dissolved in the electrolyte. The cathode and anode are electrically connected. The anode is irradiated with light of wavelength 310-315 nm and carbon dioxide dissolved in the electrolyte solution is reduced on the cathode surface covered with a small amount of nickel metal particles to generate methane.
NOVELTY - The device has a plasma generating device tube (22) connected with a hydrogen sulfide and carbonyl sulfide supply chamber (10). A plasma flame unit is connected with a horizontal tube of a plasma decomposition chamber (30). A lower end of the plasma generating device tube is connected with the hydrogen sulfide and carbonyl sulfide supply chamber. A vertical tube body (50) is arranged on a lower end of a combining chamber (40). A synthetic gas collecting tank (60) is connected with a sulfur collecting tank (70).    USE - Microwave plasma hydrogen sulfide and carbonyl sulfide removing device.    ADVANTAGE - The device can separate and collect hydrogen and carbon monoxide, simplify gas and sulfur element collecting process and improve microwave plasma production efficiency and economic efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a microwave plasma hydrogen sulfide and carbonyl sulfide removing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a microwave plasma hydrogen sulfide and carbonyl sulfide removing device.'(Drawing includes non-English language text)'    Hydrogen sulfide and carbonyl sulfide supply chamber (10)    Wave guide tube (22)    Plasma decomposition chamber (30)    Combining chamber (40)    Vertical tube body (50)    Synthetic gas collecting tank (60)    Sulfur collecting tank (70)
NOVELTY - Processing potato straw by modern biotechnology device comprises fermenting potato straw for 2-3 weeks to obtain terminal product including beneficial bacteria with 109 colony-forming unit/g.    USE - The method is useful for processing potato straw that is useful in animal feed and organic fertilizer (claimed).    ADVANTAGE - The method is capable of processing potato straw in an eco friendly manner.
NOVELTY - Special composite fertilizer comprises 10-30 %mass granular farm fertilizer, 20-50 %mass crushed plant straw, 5-40 %mass fermented poultry excrement, ferrous sulfate, and 10-30 %mass urea.    USE - As special fertilizer for camphor (claimed).    ADVANTAGE - The special fertilizer is prepared cost-effectively, increases income of farmers, solves low utilization ratio the plant straw, and reduces burning of straw.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned fertilizer, which involves (a) weighing farm manure, putting the manure in granulator and granulating and sieving the mixture until the mixture has grain diameter not greater than 4 mm, (b) weighting poultry excrement, subjecting the excrement to anaerobic fermentation, fermenting the mixture for 10-20 days, adding deodorant agent to the fermented mixture, uniformly stirring the mixture, crushing the mixture using crusher and drying the crushed mixture, (c) crushing plant straw and drying the crushed plant straw, and (d) uniformly mixing the above-mentioned mixtures.
NOVELTY - A balsam pear fertilizer comprises a solid soil fertilizer of chicken manure, pig manure containing liquid of soil, and liquid manure containing potash. The solid soil fertilizer is used for breeding. The liquid manure containing potash is used for transplantation after fertilization and top dressing. The liquid manure containing potash is produced by adding a bitter gourd leaves in the joint digester fermentation.    USE - A balsam pear fertilizer used for improving immunity.    ADVANTAGE - The fertilizer is rich in nutrition, can eliminate plant diseases and insect pests, increases yield and quality of the balsam, and provides beautiful appearance, sweet taste and refreshing taste of balsam.
NOVELTY - Biodiesel pour point depressant comprises methacrylic acid, high carbon alcohol mixture, toluene, p-toluenesulfonic acid and hydroquinone. The methacrylic acid and high carbon alcohol mixture are mixed in the mole ratio of 1:1.    USE - Biodiesel pour point depressant.    ADVANTAGE - The biodiesel pour point depressant has good depressant effect, and can be prepared in a simple manner under mild reaction condition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing biodiesel pour point depressant comprising (1) introducing the high carbon alcohol mixture and 500 ml of water into a three-necked flask, adding toluene, p-toluenesulfonic acid, methacrylic acid and hydroquinone into the flask and then heating to reflux temperature, carrying out esterification reaction, where the high carbon alcohol mixture comprises toluene, p-toluenesulfonic acid, methacrylic acid and hydroquinone, the flask is equipped with equipped with a thermometer, a reflux condenser and a stirrer, (2) distillation of the obtained product under reduced pressure to remove the unreacted methacrylic acid and solvent and then cooling to room temperature to obtain fat acid ester, base, sodium chloride and petroleum ether with the ester and then washing with water, standing to form a layer and then drying to obtain pure carbon methacrylate ester, (3) adding 500 ml of water and pure methyl acrylate into the three-necked flask and then adding mixture of methyl methacrylate, 2-hydroxyethyl acrylate, dodecyl mercaptan, benzoyl peroxide and xylene, passing nitrogen gas into the flask at 120 degrees C for 5 hours, removing xylene by distillation under reduced pressure.
NOVELTY - A biomass fuel comprises waste oil and straw in mass ratio of 10:15. The straw is wheat straw, soybean straw, rice straw or cotton straw. The waste oil is filtered and dehydrated.    USE - Biomass fuel (claimed).    ADVANTAGE - The biomass fuel has excellent combustion property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass fuel.
NOVELTY - Biomass fuel comprises 20-50 wt.% of straw powder, 30-70 wt.% of peanut powder and 10-30 wt.% of wood powder.    USE - The biomass fuel is useful in industrial boilers.    ADVANTAGE - The biomass fuel has high heating value, no slag, ash and smoke content and good energy-saving performance, and is easy to burn and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing biomass fuel comprising crushing straw, peanut shell and wood using a crusher into powder and then drying, mixing and processing by a machinery.
NOVELTY - The method involves entering carbon dioxide gas into a carbon dioxide compressor. The carbon dioxide gas is compressed to remove hydrogen sulfide. Hydrogen sulfide is entered into a gas-liquid separator for extracting hydrogen, nitrogen, carbon monoxide and methane. Separating liquid and carbon dioxide gas are passed to an air-air heat exchanger. Surplus is extracted from carbon dioxide by using a urea production device. Vacuum gas analyzing process is carried out by a pressure swing adsorption device. The air-air heat exchanger is fixed with a lithium bromide water cooler.    USE - Pressure swing adsorption decarburization gas recovery method.    ADVANTAGE - The method ensures valid gas recovering efficiency and enables reducing atmospheric pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a pressure swing adsorption decarburization gas recovery method. '(Drawing includes non-English language text)'
NOVELTY - Co-production of ethanol and biodiesel fuel, involves: (a) distilling an ethanol-containing beer within distillation apparatus (18) of an ethanol plant (12) using corn and producing ethanol and a corn oil product; (b) directing the corn oil product to a biodiesel fuel plant (14) and reacting corn oil product with alcohol to produce biodiesel fuel and by-products including glycerol, ethanol and/or methanol; and (c) transferring the by-products to the ethanol plant for distillation or mixing with a stillage stream of the distillation apparatus undergoing concentration within the ethanol plant.    USE - The integrated process is useful for the co-production of ethanol and biodiesel fuel (claimed).    ADVANTAGE - The integrated process ensures simple and economical co-production of ethanol and biodiesel fuel with increased efficiency and reduced energy consumption and without using any special equipment.    DETAILED DESCRIPTION - Co-production of ethanol and biodiesel fuel, comprises: (a) distilling an ethanol-containing beer within distillation apparatus (18) of an ethanol plant (12) using corn as a feedstock, and producing ethanol and a corn oil product; (b) directing the corn oil product from the ethanol plant to a biodiesel fuel plant (14), and reacting the corn oil product with alcohol to produce a biodiesel fuel and one or more by-products consisting of glycerol, ethanol, and/or methanol; and (c) transferring at least one of the by-products to the ethanol plant for distillation within the distillation apparatus or mixing with a stillage stream of the distillation apparatus undergoing concentration within the ethanol plant.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an integrated ethanol and biodiesel production facility.    Integrated ethanol and biodiesel production facility (10)    Ethanol plant (12)    Biodiesel fuel plant (14)    Beer well (16)    Distillation apparatus. (18)
NOVELTY - The solar energy aerator has a solar panel (1) connected to a charging and discharging controller (2). The charging and discharging controller is connected to a battery (3) and a multi-group of electrolytic electrodes (4). Each group of electrolytic electrodes is connected to an oxygen diffusion plate (5) and a hydrogen leading-out tube (6).    USE - Solar energy aerator for solar energy generating system used in water environment field.    ADVANTAGE - Offers energy-saving and environment-friendly solar energy aerator that provides power of electrolytic water.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a solar energy aerator.    Solar panel (1)    Charging and discharging controller (2)    Battery (3)    Electrolytic electrodes (4)    Oxygen diffusion plate (5)    Hydrogen leading-out tube (6)
NOVELTY - This utility new type relates to a parts, especially parts used for a of intermediate cooling device. Borneol for a of intermediate cooling device, include water, a cooling box body and cover, said cooling box body without bottom, cooling box opening in the middle, and between the opening and the edge is provided with an annular groove, the cover can be embedded to the annular groove sealing the opening, cooling box body is provided with two rows of staggered cooling sheet is composed of one continuous S type of cooling channel, cold-slice one end at the bottom is provided with a water inlet tube, the upper part of the other end is provided with a water outlet tube, upper cooling box is provided with an air inlet tube and the cooling passage of the cooling case body; the cooling case body is placed in the water tank, the water tank and the outer edge higher than the bottom of the cooling box body, upper water tank is provided with a water outlet, the air inlet tube of water outlet is located at one opposite end. The cooling device can be for saponification reaction to generate process of cooling, at the same time a separation of and water, the structure is simple, it saves energy.
NOVELTY - This utility new type relates to one of a methanation reactor, solves the problem that the large amount of methanation reactor catalytic reaction temperature is not uniform, the catalyst has short service life of use. The technical solution include air inlet sealing head, the shell and the air outlet seal head, said upper air inlet end enclosure set with an air inlet, an air outlet upper seal head is set with an air outlet, the shell is set with a catalyst bed layer, a gas inlet sealing head set with connecting with the air inlet of gas distribute tube, said gas distribute wing-shaped tube to lower the diameter is reduced gradually of diameter circular tube structure, upper side surface of said gas distribute uniformity is provided with multi-tube of distribute hole. This utility new type has simple structure, gas distribute uniformity, which avoids dead zone and high temperature reaction area, and can prevent the methane synthesis catalyst poisoning, the service life of the catalyst.
NOVELTY - This utility new type claims a one organic waste treating machine, machine frame include automatic feeding device, the fermentation chamber and allixiary chamber, automatic feeding device and fermentation chamber, the fermentation chamber and the allixiary chamber, the fermentation chamber include crushing and stirring device, an oxygen supply pipeline and heating system, the allixiary chamber is provided with a power system and, through waste automatic feeding device entering into the fermentation chamber, crushing and stirring device operate in a lower driving of power system, an oxygen supply device and oxygen supply pipeline connected to provide needed of oxygen, heating system is high temperature fermentation provide hot energy, accelerating fermentation process. The advantages is that the processor of the kitchen garbage, animal corpse is processed into organic fertilizer, crushing and stirring device to make the material crushing and stirring force uniformity, crushing movable cutter is detachable, time when the tool wear, it can be use, prolong use life of machine rear change blade, knife and allixiary application hammer grinding, obtain the organic of fully grinding, which is good for organic fertilizer of production and application.
NOVELTY - This utility new type claims a one to a paper making sludge as raw material of organic fertilizer machinery device, the rear device belonging to the papermaking sludge treatment field, include the sludge dehydrating machine, a sludge dryer, a crusher, a fermenting tank, a mixing machine, wherein the upper sludge dewatering machine set with paper-making sludge inlet, the sewage outlet, a sludge dewatering machine and sludge drying machine set with first conveyor, a sludge dryer and crusher set with second conveyor upper machine set with composite amino acid chelating microelement inlet, composite the humic acid chelating microelement inlet, and set with the third fermentation tank, fermenting tank set with upper water inlet, organic fertilizer fermenting agent inlet, a sterilizing deodorant inlet, a fermenting tank and mixing machine set with the fourth conveyor, crusher and mixing machine set with fifth conveyor, upper mixing machine set with a finished product outlet.
NOVELTY - This utility new type claims a one a vertical wire apple special base fertilizer of machinery device, the device belongs to the field of organic fertilizer field, include: crusher, fermenting tank, a neutralizing tank, a concentrating tank, a crusher, a mixing machine, wherein the upper machine set with drying of excrement inlet, and no pollution of pond mud inlet, peanut and rapeseed straw inlet of cattle and sheep and horse manure inlet, grain inlet, a cake inlet, and set with first fermentation tank, fermenting tank set with upper organic fertilizer fermenting agent inlet, a water inlet, a fermenting tank and the mixing machine set with the second conveyor upper neutralizing tank set with amino acid waste liquid inlet, waste alkali liquor inlet, a neutralizing tank and concentrating tank set with first slurry pump and pipeline, concentrate tank and mixing machine set with the third conveyor, set with upper inlet of potassium sulphate, diammonium phosphate inlet, furan pill inlet, calcium chloride inlet, inlet humic acid, and mixing machine set with fourth conveyer, mixing up machine set with a finished product outlet.
NOVELTY - Movable biomass rubbish gasification furnace include furnace body, and the furnace body of the furnace frame, a furnace body upper end inlet connecting with a feeding mechanism, upper end of said furnace body is provided with a drying room, a drying room lower end is provided with a guide hot property of having downward opening and closing of seal door drying, drying under a seal door is provided with a reducing room, lower end of said reducing room is provided with a reducing seal door, the lower part of said reducing seal door is provided with a combustion room, a lower end is provided with a combustion chamber isolation belt, a lower isolation belt is provided with a coke combustion. This utility new type has reasonable structure, low manufacturing cost, good energy-saving effect, carbonizing temperature high, and the harmful substance is high removal rate, carbonizing; through three seal door feeding, no discharge, and the environment protection effect is good.
NOVELTY - Hot wood coal trash and biomass high temperature environment-friendly production system, include, connecting to the gasification furnace of the carbonization furnace, a carbonizing furnace include furnace body, said furnace body from upper to lower in turn include drying room, reducing room, burning room and carbonizing chamber, a drying room of lower end is provided with a drying seal door, lower end of said reducing room is provided with a reducing seal door, lower end of said burning room is provided with a combustion isolation belt, a furnace body on side wall of said carbonizing room is provided with a through hole, said through hole is connected with a connecting tube, a furnace body through the connecting tube and a gasification furnace are connected. This utility new type has simple structure, through biomass generating cold coal efficiency high, combustion temperature high, hot coal has good purification effect, air transparent, blackness, good environment protection effect.
NOVELTY - This utility new type one a biomass destructive distillation pyrolysis and gasification device, include inclined roller, a roller set with feeding tube, a material cavity, the cavity is equipped with an air outlet tube, a slag tube, and an outer wall is provided with the roller gear, the lower part with the transmission motor, a gearbox connecting of transmission shaft, the transmission shaft is provided with a transmission shaft gear, two end of the roller is provided with a clamping groove, the clamping groove is provided with multiple rolling shaft, the outer shaft is covered with shaft regulating pressure ring, roller two end a is connected with the material chamber, a feeding tube through bolt connecting with an inner flange ring and the outer flange, the inner flange is provided with an oil regulating bolt, oil regulating bolt pressing roller regulating pressing ring, wherein the combined of the outer flange and the roller is provided with a packing strip, roller is provided with spiral groove plate, and an outer roller is provided with a transverse rod, a transverse rod with a connecting rod, connecting with several electric heating coil, an electric heating coil covered on the outer wall of the roller, the electric heating coil is further covered with an insulating layer. This utility new type energy-saving and consumption-reducing, which greatly reduces the enterprise production cost.
NOVELTY - This utility new type claims a rice hull recovery by using one device, include adding a, rice processing device, a gas device and used for detecting gas component of a gas component analysis detecting a, rice hull processing device include discharging control device, a pre-heating furnace, reaction furnace and the reaction furnace through a connected pre-heating furnace, pre-heating furnace and the reaction furnace through a feeding valve of material passing hole tube connected, a gas connecting device on the top end of furnace and reaction of reaction furnace connected with the inner cavity, the bottom of reaction furnace set with a discharging port, a discharging device is installed on the discharging port, a pre-heating furnace include pre-heating temperature detecting device, the heating chamber and the heating chamber used for provide heat of heating device, pre-heating temperature detecting device mounted include reaction temperature detection device, an inner container and a shell of the heating cabin, reaction furnace, the inner shell is sleeved outside the container, reaction temperature detecting device is installed on the inner container. This utility new type can improve the use ratio of the rice at the same time improves the production efficiency, reduces the pollution of the environment.
NOVELTY - coal trash and biomass high temperature environment-friendly production system, include, connecting to the gasification furnace of the carbonization furnace, a carbonizing furnace include furnace body, said furnace body from upper to lower in turn include drying room, reducing room, burning room and carbonizing chamber, a drying room of lower end is provided with a drying seal door, lower end of said reducing room is provided with a reducing seal door, lower end of said burning room is provided with a combustion isolation belt, a furnace body on side wall of said carbonizing room is provided with a through hole, said through hole is connected with a connecting tube, a furnace body through the connecting tube and said gasification furnace is connected, said gasification furnace in turn include several de-coke oven, and connect to a de-coke furnace rear end of filter. This utility new type has simple structure, through biomass generating cold coal efficiency high, combustion temperature high, cold coal purifying effect is good, the production process has no pollution in the discharge.
NOVELTY - This utility new type claims a biomass granule one production line device, composed of connecting with material inlet of slicing, drying, conveying belt of crushing mechanism, mechanism, a cooling mechanism and a sieving mechanism, a drying mechanism is provided with a rotary feeding cylinder, a discharge end of said cylinder is set with rotary feeding mechanism is connected with the crushing of belt conveyors, crushing mechanism through a conveyor and the granulating mechanism is connected with packaging machine connecting the sieving of the discharging end. This utility new type has a good continuity of the biomass raw material suitable for wide range of advantages, but also suitable for high water straw material, the water content of biomass granule fuel control 15% following the front treatment to the forming process, low energy consumption, easy forming, high efficiency of production, and forming a rear of density, small volume, convenient for transportation and storage.
NOVELTY - Smoke agent comprises 3-25 %mass copper nitrate, 3-28 %mass aerosol density regulator, 3-18 %mass ammonium chloride, 4-19 %mass sulfur, 21-54 %mass surfactant, 0.2-1.4 %mass flame retardant, 5.5-24.5 %mass urea and 1.2-14.5 %mass talc powder.    USE - The smoke agent is used with pesticides.    ADVANTAGE - The smoke agent is nonflammable as the agent is added with the flame retardant, and hence riks of fire hazards at time of use of the agent is eliminated, has compatibility with pesticides and high utilization rate, and does not pollute environment. The agent enables safe and uniform usage of the pesticides.
NOVELTY - Method for producing edible mushroom involves (a) mixing 60 pts. wt. corn cob, 20 pts. wt. cottonseed hulls, 10 pts. wt. wheat bran, 1.5 pts. wt. lime, 1 pts. wt. calcium superphosphate, and 1 pts. wt. gypsum powder, (b) packaging the mixture in bag, sealing using cotton, and sterilizing at 200 kPa and 130 degrees C for 10 minutes, and (c) inoculating 8 plus minus 2% bacterial culture, maintaining 20-28 degrees C temperature and 65-80% humidity, cleaning contamination, ventilating, measuring temperature inside the bag to prevent high heat, increasing indoor humidity to 80-90%, and picking the mushroom.    USE - The method is useful for producing edible mushroom (claimed).    ADVANTAGE - The method is simple, environmentally-friendly and suitable for industrial production and produces edible mushroom having high nutrient content at less period.
NOVELTY - A fungicidal composition comprises pyraclostrobin and dichloroisocyanuric acid as active components at mass ratio of 35:1-5:50. Composition includes 1-80 wt.% active components, additive and complement components.    USE - Fungicidal composition in the form of wettable powder, suspension, emulsifiable concentrate, aqueous emulsion or water dispersible granule (claimed).    ADVANTAGE - The quick-acting, persistent and environment-friendly fungicidal composition increases crop production, and reduces application frequency, dosage and cost.
NOVELTY - This utility new type provide a high-efficient organic fertilizer, one set with two link the fermentation unit, wherein the first fermentation unit fermentation groove, stirring unit, heating unit, hot air unit and driving unit, second fermentation unit comprises rolling mixing unit, the hot air unit and driving unit, a driving unit driving the stirring unit and a rolling unit mixing a mixture of raw materials in the fermentation and fermentation, and to heating unit and the hot air unit to maintain the fermentation groove space specific temperature and provide needed air (oxygen), accelerated to a raw material of organic fertilizer, organic fertilizer greatly shortens the manufacturing time, provide high yield and the organic fertilizer of high mass, and the valid fermentation process pollution and cost.
NOVELTY - This utility new type relates to one used for automatic production system of a biomass dense forming, which in turn include of connecting material preprocessing part, material forming part, a finished product sieving mechanism and finished product cooling conveyor, a material preprocessing part through inclined feeding forming part connecting with the material, the material preprocessing include in connecting part of original material belt machine, boiling chamber, an exhaust fan, a sieving machine and water-material belt machine, further connecting ebullition chamber humidifying device and hot-blast stove, a water purifying material belt machine and the inclined feeding machine, material forming part include connecting of distributor in turn, a modulator, a extrusion forming machine, a discharging belt machine and discharging machine, and the inclined feeding machine with the product sieving mechanism connecting finished product discharging machine and the finished product cooling conveyor, the utility model is new type feeding and discharging, not need aritificial operation to realize the continuous production and improves the production efficiency and yield, saves the labour of, so as to reduce the production cost and improve the profit of the enterprise.
NOVELTY - This utility new type provide a one hot-efficient tea chamber, include one main body and multiple detachable tea chamber compost, said compost is set around the said main body of the outer wall upper tea chamber, each of said compact box of upper part set with one organic waste entering into port, lower part set with one organic waste outlet, said hot tea chamber effect of the bottom set with one hot energy conveying tube, a tea chamber of main body is set with one hot energy dispersing plate, a hot energy dispersing plate and a hot energy conveying connecting tube. This utility new type through the green organic waste of ferment compost process and a combined form by using the local circulation of system, reduces the transportation cost of municipal organic waste, but also can solve the problem that consumption of heating season landscape tea chamber cold.
NOVELTY - This new type utility claims one engine system of a hydrogen-oxygen generating device, include: an internal combustion machine, a water tank, with a liquid inlet and the air outlet, the water tank is filled with water, a car battery, electrolytic groove, internal of said electrolytic groove is provided with a multi-electrode plate of are arranged in parallel, each two adjacent of the electrode plate in, wherein one electric connect to the anode of vehicle battery, and the other one electrically connecting the cathode of vehicle battery, each two adjacent electrode plate between the forming of one electrolysis space, said electrolytic space through one water inlet tube and a water tank connected so that a space for accommodating water, electrolyzing said electrolytic space through one air outlet tube and a connected water tank, the air outlet of said water tank is connected to the cylinder of said internal combustion engine. This utility new type provided by the device can save fuel, reduces the tail gas emission and lifting power, at the same time, it can remove carbon for internal combustion engine of vehicle and prolong engine life.
NOVELTY - The system has a system body provided with a catalytic oxidation (CO) reactor. A rear discharge unit of the CO reactor is fixed with a SCR reactor. A rear hot exchanger unit of the SCR reactor is filled with air and tail gas. The CO reactor is connected with a gas discharging chimney by an external processing unit. A multi-boiler is formed with as a waste hot boiler that is connected with the SCR reactor via a regulating inlet. The waste hot boiler is provided with a boiler water-feeding device, a discharging device and an over-hot steam tube valve. A heater is formed as an electric heater.    USE - Tail gas catalytic combustion treatment system.    ADVANTAGE - The system is simple in structure and environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a tail gas catalytic combustion treatment system.'(Drawing includes non-English language text)'
NOVELTY - Production of activated carbon/calcium-zinc oxide solid base catalyst involves mixing high specific surface area activated carbon powder with calcium nitrate tetrahydrate and zinc nitrate hexahydrate mixture, adding sodium carbonate and sodium hydroxide solution slowly, adjusting pH of the mixture to 9, stirring at 60 degrees C, aging for 24 hours, separating precipitate filtration, washing using deionized water, drying at 130 degrees C, calcining at 850 degrees C in muffle furnace for 8 hours, cooling to room temperature, sieving and obtaining particles having size of 90-200 mu m.    USE - Activated carbon/calcium-zinc oxide solid base catalyst is used for preparing biodiesel.    ADVANTAGE - The catalyst has conversion rate of 98.2%, strength and stability.
NOVELTY - Method of processing domestic waste involves (a) crushing and fermenting domestic waste at normal temperature; (b) separating obtained waste into three different types chosen from (i) waste paper, scrap metal and glass, (ii) kitchen waste and other organic matter, and (iii) sand, soil inorganic material and other minerals; (c) recycling waste chosen from (i) and (ii) to obtain organic fertilizer and waste chosen from (iii) to obtain building material or brick; and (d) disposing the harmful substances having no recycling value.    USE - The method is useful for processing domestic waste (claimed).    ADVANTAGE - The method is cost-effective and environmentally-friendly.
NOVELTY - A biological treatment is performed by preprocessing raw biogas slurry in aeration tank, filtering using filter, feeding to 1st stage of biological reactor, inoculating microalgae, breeding for 5-8 days, degrading pollutants, feeding slurry to 2nd stage of biological reactor, reacting for 4-7 days to obtain 80% degradation rate of nitrogen and phosphorus, feeding in storage tank, filtering and separating microalgae, refining to obtain biological diesel oil and level B water which can be used in agricultural irrigation.    USE - A biological treatment for purifying biogas slurry (claimed).    ADVANTAGE - The method is highly efficient, simple, low cost, and purified product has high value.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of biological treatment for purifying biogas slurry. (Drawing includes non-English language text).
NOVELTY - An organic fertilizer treatment device comprises reaction tank (1), L type inlet (2), reverse L type sealing cover (3), and outlet (4).    USE - Harmless treatment device used for organic fertilizer, particularly manure or urine with straw (claimed).    ADVANTAGE - The device protects nutrient loss, avoids water washing, is simple, and has low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of harmless treatment device.    Reaction tank (1)    L type inlet (2)    Reverse L type sealing cover (3)    Outlet (4)
NOVELTY - Petrochemical sludge dehydrating agent, obtained by 1 mmol/l isopropyl beta -D-1-thiogalactopyranoside (IPTG) induction of human lysozyme engineered bacteria XD3-hLyz, is claimed.    USE - The petrochemical sludge dehydrating agent is useful in petrochemical sludge dehydrating process (claimed).    ADVANTAGE - The dehydrating agent used lysozyme engineering bacteria as sludge conditioning agent, and thus can destroy zoogloea structure; reduces the surface adsorbed water and internal bonding water, to improve the dehydration rate by 32.41%; reduces pathogens, inhibits septic potential, reduces sewage treatment cost and improves the treatment of sewage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the petrochemical sludge dehydrating agent, comprising (i) adding high efficient flocculant and human lysozyme engineered bacteria XD3-hLyz into petrochemical sludge mixed with the air, and treating for 10 days to obtain preliminary treatment sludge; (ii) inducing the preliminary treatment sludge by adding IPTG, subjecting reaction equilibrium, diffusion and mass transfer balance for 36-72 hours, to obtain advanced treatment sludge; and (iii) allowing the advanced treatment sludge to stand so as to precipitate, obtaining upper supernatant water and lower precipitate, filtering and discharging the supernatant water, and the lower precipitate is lower petrochemical sludge dehydrating agent.
NOVELTY - The organic waste composting reactor has discharging groove (34) which is located at ends of cylindrical container (11). The container is arranged on feeding groove (21) and discharging groove so as to rotate the roller (12,13). A rubber seal portion (33) is provided between round ring and adjacent tubular portion of circular plate. The ring barrel is installed on upper portion of circular plate (15,16) so as to rotate the circular plate. A long tube shaft (46) is provided along the axial direction of container so as to compost the reactor automatically.    USE - Organic waste composting reactor.    ADVANTAGE - The organic waste composting reactor can be processed continuously. The high efficiency of the organic waste composting reactor can be ensured. The high degree of automation organic waste composting reactor can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic waste composting reactor.    Cylindrical container (11)    Roller (12,13)    Circular plate (15,16)    Feeding groove (21)    Rubber seal portion (33)    Discharging groove (34)    Long tube shaft (46)
NOVELTY - Biofertilizer is prepared by using agricultural waste including 60-70 wt.% waste vegetable leaves, 9-15 wt.% crop straw, 0.5-1 wt.% complex fermenting agent, 5-10 wt.% humic acid, 5-10 wt.% rice hull and 4-20 wt.% Acetobacter xylinum.    USE - As biofertilizer.    ADVANTAGE - The biofertilizer is environmentally-friendly, and enables to increase income of farmer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the biofertilizer using agricultural waste which involves crushing the waste vegetable leaves, and crop straw at 2-3 degrees C, where the water content of the mixture is 60-65%, adding complex fermenting agent to the mixture, performing stacked fermentation for 15-30 days, uniformly mixing the fermented mixture with humic acid, rice hull ash, and A.xylinum, and sieving the obtained product using 3 mm meshes sieve.
NOVELTY - Organic fertilizer formulation comprises 5 pts. fresh pumpkin, 5 pts. fresh peanut straw, 5 pts. fresh cabbage leaf (stem), 5 pts. oil cake (vegetable oil), 0.2 pts. brown sugar, 0.1 pts. fermentative strain, 4 pts. minerals and 0.004 pts. trace elements.    USE - The organic fertilizer formulation is useful for melons (claimed).    ADVANTAGE - The organic fertilizer formulation improves fruit (melon) quality, and causes no pollution, and leaves no residues.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned organic fertilizer formulation, which involves fermenting the above-mentioned raw materials except trace elements at room temperature for 168 hours, filtering the fermented product, and adding the above-mentioned trace elements to the obtained filtrate.
NOVELTY - Method for preparing composite microbial fertilizer, involves (a) inoculating Pseudomonas fluorescens P13 strain to liquid culture medium at 28 degrees C under stirring speed of 200 revolutions/minute (rpm) for 16-20 hours, centrifuging the culture medium, collecting supernatant, and adding preservative to the supernatant to obtain suspension bacteria liquid, (b) adding the suspension bacteria liquid to substrate, and (c) mixing mixture with earthworm at a mass ratio of 1:1.    USE - The method is useful for preparing composite microbial fertilizer which is used for promoting growth of crops, and preventing and controlling plant pathogenic bacteria (claimed).    ADVANTAGE - The method prepares fertilizer in cost-effective, easy and environmentally-friendly manner, and improves soil quality.
NOVELTY - Method for preparing organic fertilizer, involves crushing biomass material to 0.1-5 cm, boiling the crushed product using water (natural) for 1-5 minutes, and burying the obtained product in soil (depth of at least 10 cm).    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The method is simple to perform (easy to control and master). The organic fertilizer prepared by the method reduces pathogenic bacteria in soil and diseases of crops, and improves soil environment, and is suitable for long term usage (fertilizer can be retained for a long period in soil).
NOVELTY - Organic nitrogenous fertilizer comprises components in complex form.    USE - The organic nitrogenous fertilizer is useful for promoting plant growth.    ADVANTAGE - The fertilizer enables mass production and high yield of crops.    DETAILED DESCRIPTION - Organic nitrogenous fertilizer comprises components in complex form which is represented by formula: NH4COOCH2-FeMo-co-NH4HCO3. An INDEPENDENT CLAIM is included for method for preparing the organic nitrogenous fertilizer, which involves (a) drying chicken manure until water content becomes 60-65% at 110 degrees C, mixing brown sugar and dried manure in a ratio of 1:1, and adding mixture to fermentation kettle maintained at 45 degrees C for 3 days, (b) processing spirulina at 110 degrees C, and fermenting processed spirulina at 32 degrees C for 7 days, and (c) crushing fermented product, mixing product of step (a) with respect to crushed product, fermenting mixture with straw in reaction kettle at 45 degrees C for 7 days, and stirring fermenting materials for 30 minutes to obtain fertilizer.
NOVELTY - Method for producing composting agent, involves mixing filter mud, cassava residue, and bagasse ash in a weight ratio of 3-4:3-4:1-2, adding microbial cell, mixing the mixture uniformly, and fermenting the mixture for 20-30 days, crushing the fermented product and drying at low temperature to obtain the product. The microbial cells are Bacillus. The amount of Bacillus is added to the filter mud, cassava residue and bagasse ash is 2-8 wt.%.    USE - The method is useful for producing composting agent (claimed).    ADVANTAGE - The method is cost-effective. The prepared composting agent has high viable cells.
NOVELTY - The automatic fertilizer machine has a bracket (1) which is pivotally mounted on upper portion of compost box (2). The compost box is located at the opening (21) on the cover (22). The opening of the cover is sealed. A transmission connecting device is connected to compost box. The transmission connecting device is connected and powered to power device (3) so as to rotate the compost box.    USE - Automatic fertilizer machine.    ADVANTAGE - The working efficiency of the automatic fertilizer machine can be improved. The labor intensity required for operating the automatic fertilizer machine can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the automatic fertilizer machine.    Bracket (1)    Compost box (2)    Power device (3)    Opening (21)    Cover (22)
NOVELTY - The automatic fertilizer machine has a bracket (1) that is pivotally connected with a compost tank (2). The rotary power device (3) and transmission device are connected between compost tanks. An opening (21) is formed on an upper surface of the tank. A cover (22) is movably connected with opening. The transmission units are driven by a driving unit. The transmission unit is connected with the drive unit when the compost tank is in rotating state, and is disconnected from the drive unit when the compost tank is in stationary state.    USE - Automatic fertilizer machine.    ADVANTAGE - The compost working status can be easily switched, and high balance property can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the automatic fertilizer machine.    Bracket (1)    Compost tank (2)    Rotary power device (3)    Opening (21)    Cover (22)
NOVELTY - The fermentation tank has heat preservation solid-liquid separating tank (2) that is installed in workshop factory building (1), and is connected with a heat-preservation ferment pool (3) through conveying device. The anti-seepage cement layer, radiating layer, high temperature heating cable layer, barrier layer and building base layer are orderly arranged from inside to outside on bottom and side walls of solid-liquid separating tank, ferment pool and factory building. The solar panel with insulating plate is provided on roof of factory to form double-layer structure.    USE - Warming and heat-preserving-type organic waste aerobic fermentation tank used in livestock and poultry cultivation industry.    ADVANTAGE - By using the high-temperature heating cables, full use of clean energy can be enabled, and the need for generating heat by coal can be avoided, such that the air pollution and haze generation can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an organic waste aerobic fermentation tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic waste aerobic fermentation tank.    Workshop factory building (1)    Solid-liquid separating tank (2)    Ferment pool (3)
NOVELTY - The device has low temperature outlet (3) and discharge port (7) that are provided on side wall and bottom of fermentation tank (1). An air storage tank (26) is coupled between air pump (27) and air heater (24) which is equipped with gas flow meter (17) through electromagnetic valve (23). The gas flow meter is connected with air supply room (13). The output ends of stack and environment temperature sensors (18,19) are connected with programmable logic controller (PLC) module (21) through temperature module (20). The PLC module is connected with display electromagnetic valve (23).    USE - Full-automatic aerobic compost test device used in livestock cultivation field.    ADVANTAGE - The stack vent uniformity is ensured, exogenous air pressure is reduced, electric energy consumption is minimized, longer automatic flow control ventilation is optimized, the temperature data is automatically recorded, heat preservation effect is improved, cost is reduced, operation is simplified and high automatic degree is realized.    DETAILED DESCRIPTION - A gas collecting tank (12) is connected with tank cover (8) through a tail gas outlet (11). An air column (14) is installed on gas distribution disc (15), and a distributing bracket (16) is connected between gas distribution disc and slope bottom surface (4), so as to form air supply room.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the aerobic compost test device.    Fermentation tank (1)    Low temperature outlet (3)    Slope bottom surface (4)    Discharge port (7)    Tank cover (8)    Tail gas outlet (11)    Gas collecting tank (12)    Air supply room (13)    Air column (14)    Gas distribution disc (15)    Distributing bracket (16)    Gas flow meter (17)    Stack and environment temperature sensors (18,19)    Temperature module (20)    PLC module (21)    Electromagnetic valve (23)    Air heater (24)    Air storage tank (26)    Air pump (27)
NOVELTY - The system has a fermentation tower main portion (3) that is provided with material inlet (1) and tail gas outlet (2). A discharging device (7) is installed on the fermentation tower main portion. The bottom of the fermentation tower main portion is equipped with a level sensor. The fermenting tower main portion is provided with temperature-oxygen sensor (13) and sampling port (6). The discharging device is provided with discharging driving bridge motor (5).    USE - Tower-type self-coupling and high temperature aerobic fermentation system.    ADVANTAGE - The cost of the aerobic fermentation system can be reduced effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the tower-type self-coupling and high temperature aerobic fermentation system.    Material inlet (1)    Tail gas outlet (2)    Fermentation tower main portion (3)    Discharging driving bridge motor (5)    Sampling port (6)    Discharging device (7)    Temperature-oxygen sensor (13)
NOVELTY - Method of preparing potassium-phosphorus organic compound fertilizer, involves harvesting corn stalk and waste of wheat straw hood, crushing the materials into granule, placing the mixture in a tank, pressing, sealing and naturally fermenting for 20 days to obtain the natural organic fertilizer, where the organic compound fertilizer comprises potassium fertilizer and urea fertilizer in a ratio of 6:4.    USE - The method is useful for preparing potassium-phosphorus organic compound fertilizer used for banana and persimmon.    ADVANTAGE - The fertilizer is easily absorbed by the crops, is convenient to use and store for long period of time, environmentally-friendly and cost-effective, can be prepared simply, and improves crop quality and yield of agricultural product.
NOVELTY - Method of preparing nitrogen-potassium organic compound fertilizer, involves harvesting corn stalk and waste of wheat straw hood, crushing the materials into granule, placing the mixture in a tank, pressing, sealing and naturally fermenting for 16 days to obtain the natural organic fertilizer, where the organic compound fertilizer comprises potassium fertilizer and urea fertilizer in a ratio of 8:1.    USE - The method is useful for preparing nitrogen-potassium organic compound fertilizer (claimed).    ADVANTAGE - The fertilizer is easily absorbed by the crops, is convenient to use and store for long period of time, environmentally-friendly and cost-effective, can be prepared simply, and improves crop quality and yield of agricultural product.
NOVELTY - Method of preparing organic compound fertilizer, involves harvesting corn stalk and waste of wheat straw hood, crushing the materials into granule, placing the mixture in tank, sealing and naturally fermenting for 16 days to obtain natural organic fertilizer, where the organic fertilizer comprises nitrogenous fertilizer and phosphate fertilizer.    USE - The method is useful for preparing organic compound fertilizer (claimed).    ADVANTAGE - The fertilizer is easily absorbed by the crops, is convenient to use and store for long period of time, environmentally-friendly and cost-effective, can be prepared simply, and improves crop quality and yield of agricultural product.
NOVELTY - Preparation of substrate for growing eggplant involves selecting chicken manure, stacking the manure into pile and naturally fermenting for 3 months, stacking horse manure, adding 100 g actinomycetes, mixing uniformly, covering with cloth, and fermenting for 5-7 days, selecting peat soil, mixing the soil with the fermented chicken and horse manure, adding 100-150 g nitrogen fertilizer, 200-250 g phosphate fertilizer, 100-150 g potassium fertilizer, 80-150 g radix scutellariae powder and 100-200 g fructus cnidii, and stirring uniformly.    USE - Preparation of substrate for growing eggplant (claimed).    ADVANTAGE - The method is simple and enables preparation of substrate that promotes rapid propagation of eggplant. The method effectively shortens time of planting to harvest, and thus reduces harvest date by 10-13 days.    DETAILED DESCRIPTION - Preparation of substrate for growing eggplant involves selecting chicken manure, stacking the manure into pile with length of 3-5 m, height of 1-1.2 m and width of 1.5-2 and naturally fermenting for 3 months, stacking horse manure, adding 100 g actinomycetes to each cubic meter stack, mixing uniformly, covering with cloth, and fermenting for 5-7 days, selecting 15 cm deep peat soil, mixing the soil with the fermented chicken and horse manure, adding 100-150 g nitrogen fertilizer, 200-250 g phosphate fertilizer, 100-150 g potassium fertilizer, 80-150 g radix scutellariae powder and 100-200 g fructus cnidii, and stirring uniformly.
NOVELTY - Microbial organic fertilizer comprises 40-60 pts. wt. salts, 40-60 pts. wt. beans, 40-60 pts. wt. mushroom residues, 40-60 pts. wt. molasses, 20-30 pts. wt. vitamin, and 1-10 pts. wt. composite agent. The vitamin comprises 1-2 pts. wt. vitamin B1, 1-2 pts. wt. vitamin B2, 1-2 pts. wt. vitamin B6, 1-2 pts. wt. vitamin B12, 1-2 pts. wt. vitamin C.    USE - As microbial organic fertilizer.    ADVANTAGE - The microbial organic fertilizer is valuable and saves natural resource, has high beneficial substance by using large amount of waste, protect environment, and provides enough crop growth of organic molybdenum and vitamins.    DETAILED DESCRIPTION - Microbial organic fertilizer comprises 40-60 pts. wt. salts, 40-60 pts. wt. beans, 40-60 pts. wt. mushroom residues, 40-60 pts. wt. molasses, 20-30 pts. wt. vitamin, and 1-10 pts. wt. composite agent. The vitamin comprises 1-2 pts. wt. vitamin B1, 1-2 pts. wt. vitamin B2, 1-2 pts. wt. vitamin B6, 1-2 pts. wt. vitamin B12, and 1-2 pts. wt. vitamin C. The composite agent comprises 1-2 pts. wt. photosynthetic bacteria, 1-2 pts. wt. nitrifying bacteria, 1-2 pts. wt. lactic acid bacteria, 1-2 pts. wt. yeast, 1-2 pts. wt. nitrogen-fixing bacteria, 1-2 pts. wt. actinomycetes, 1-2 pts. wt. phosphate solubilizing bacteria, 1-2 pts. wt. Bacillus subtilis, and 1-2 pts. wt. plant growth promoting bacteria. An INDEPENDENT CLAIM is included for preparation of the fertilizer, which involves crushing above-mentioned raw materials to 20-80 mesh sizes, mixing mixture uniformly, fermenting the mixture at 65 degrees C for 12-36 hours, and concentrating the mixture to obtain product.
NOVELTY - Method for preparing organic fertilizer, involves (a) crushing straw, coal gangue and rice hull powder, and steam sterilizing mixture at high temperature to obtain mixture, (b) adding mixture comprising urea, calcium superphosphate and propanetriol to the obtained mixture, uniformly stirring mixture and adding the mixture to fermentation tank, (c) adding the mixed strain powder to fermentation tank, (d) adding auxiliary materials to the fermented mixture, and uniformly stirring the mixture and (e) adding the mixture to disc pelletizer, and drying product.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The method is easy to operate, suitable for large scale production, and cost-effective.    DETAILED DESCRIPTION - Method for preparing organic fertilizer, involves (a) crushing straw, coal gangue and rice hull powder into 80 meshes sieve, and steam sterilizing mixture at high temperature to obtain mixture, (b) adding mixture comprising urea, calcium superphosphate and propanetriol to the obtained mixture, uniformly stirring mixture and adding the mixture to fermentation tank, (c) adding the mixed strain powder into fermentation tank, (d) adding auxiliary materials to the fermented mixture, and uniformly stirring the mixture and (e) adding the obtained mixture into disc pelletizer, and drying to obtain organic fertilizer.
NOVELTY - Biological organic fertilizer comprises raw materials comprising 15-25 wt.% straw, 5-10 wt.% wood vinegar, 40-60 wt.% chicken manure, 1-5 wt.% ore powder and 14-20 wt.% soybean meal.    USE - As biological organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic fertilizer, which involves mixing the above-mentioned raw materials and pelleting the mixture.
NOVELTY - Preparing bio-organic fertilizer by weighing 20-25% Epimedium extract residues, 23-28% Rhodiola extract residues, 25-30% pig manure, 20-28% sheep manure, 3-6% calcium phosphate, and 0.3-0.5% effective microorganism, adding cellulase having 3.5-4.5 million U activity to the weighed material in ratio of 1:2000, mixing uniformly, stacking the mixture, hydrolyzing, crushing the mixture, fermenting the mixture at 50-60 degrees C for 12-16 days in summer and 18-25 days in winter, adjusting nitrogen content, drying at low temperature, and adding into disc granulator.    USE - The method is useful for preparing bio-organic fertilizer (claimed).    ADVANTAGE - The prepared bio-organic fertilizer has more than 50% organic matter content, is stable, and environmentally-friendly and improves cellulose decomposition level.    DETAILED DESCRIPTION - Method for preparing bio-organic fertilizer involves (a) weighing 20-25% Epimedium extract residues, 23-28% Rhodiola extract residues, 25-30% pig manure, 20-28% sheep manure, 3-6% calcium phosphate, and 0.3-0.5% effective microorganism, (b) adding cellulase having 3.5-4.5 million U activity to the weighed material in ratio of 1:2000, mixing uniformly, stacking the mixture, hydrolyzing, and crushing the mixture, (c) fermenting the mixture at 50-60 degrees C for 12-16 days in summer and 18-25 days in winter, and (d) adjusting nitrogen content, drying at low temperature, and adding into disc granulator.
NOVELTY - Bio-organic fertilizer comprises 0.001-0.003 pts. wt. Bacillus thuringiensis powder, 15-20 pts. wt. rice bran, 3-9 pts. wt. rape, 1-2 pts. wt. dipotassium hydrogen phosphate, 3-9 pts. wt. sodium dihydrogen phosphate, 11-16 pts. wt. disodium hydrogen phosphate, 12-15 pts. wt. rice hull powder, 2-6 pts. wt. ammonium nitrate, 1-2 pts. wt. calcium nitrate, 10-15 pts. wt. rapeseed cake, 15-30 pts. wt. soybean meal, and 1-2 pts. wt. Bacillus subtilis.    USE - The bio-organic fertilizer is useful for tea (claimed).    ADVANTAGE - The bio-organic fertilizer is rich in organic and inorganic nutrients, and multi-nutrients, and nontoxic, and causes no side effects, and does not leave any residues. The fertilizer causes no pollution, and has no drug resistance, and provides necessary nutrients to tea, and improves quality of tea and soil conditions.
NOVELTY - Biologically controlled-release fertilizer comprises raw materials containing 15-20 pts. wt. tea leaves powder, 10-12 pts. wt. stone powder, 20-25 pts. wt. carbon powder, 30-40 pts. wt. chicken manure, 15-20 pts. wt. rice bran, 15-20 pts. wt. wheat bran, 10-20 pts. wt. rice straw powder, 10-15 pts. wt. corn straw powder, 0.001-0.002 pts. wt. silicate bacterial powder, 0.002 pts. wt. Bacillus cereus powder, 0.001-0.002 pts. wt. Verticillium powder, 25-30 pts. wt. chicken manure, 15-20 pts. wt. rice bran, 10-12 pts. wt. kieselguhr, and 6-20 pts. wt. peat.    USE - The biologically controlled-release fertilizer is useful for mountain tea tree (claimed).    ADVANTAGE - The biologically controlled-release fertilizer contains organic and inorganic nutrients, and trace elements, and improves soil conditions and quality of tea, and provides balanced nutrients to tea tree, and is cost-effective.    DETAILED DESCRIPTION - Biologically controlled-release fertilizer comprises raw materials containing 15-20 pts. wt. tea leaves powder, 10-12 pts. wt. stone powder, 20-25 pts. wt. carbon powder, 30-40 pts. wt. chicken manure, 15-20 pts. wt. rice bran, 15-20 pts. wt. wheat bran, 10-20 pts. wt. rice straw powder, 10-15 pts. wt. corn straw powder, 0.001-0.002 pts. wt. silicate bacterial powder, 0.002 pts. wt. Bacillus cereus powder, 0.001-0.002 pts. wt. Verticillium powder, 25-30 pts. wt. chicken manure, 15-20 pts. wt. rice bran, 10-12 pts. wt. kieselguhr, and 6-20 pts. wt. peat.
NOVELTY - The method involves heating powdered catalyst and biomass raw material, and passing carrier gas to a fluidized bed reactor through a rear screw conveyor. The powdered catalyst and the biomass raw material are sprayed on the fluidized bed reactor. The biomass raw material is injected into a bed cracking reactor and added with the powdered catalyst to obtain solid hot coke by-product and gas product. The gas product is entered into a spraying bed reactor by an injection cyclone channel. Purified gas product is conveyed to a spray cooling tower by a small hole channel.    USE - Biological oil and non-condensable gas pyrolysis method for a catalyst spraying bed.    ADVANTAGE - The method enables improving quality of biological oil and oil producing rate and reducing production cost.    DETAILED DESCRIPTION - The catalyst is nickel, platinum, palladium, cobalt and metal catalyst. The biomass raw material is wood fiber. The spray cooling tower is filled with cooling liquid that is bio-oil and complementary mixing of organic solvent. The organic solvent is alcohol or ketone, soluble oil of low organic solvent, isopropyl alcohol, n-butyl alcohol and isobutyl alcohol. The ketone is acetone and methyl isobutyl ketone.
NOVELTY - The system has a fluidized bed-type biomass gasification furnace provided with a reaction section and a tail ash section that are fixed with a fire grate. The reaction section is equipped with a vertical tube. A feeding port is located at a middle part of the reaction section. The tail ash section is equipped with a cone-shaped structure. A tail ash outlet is fixed at a bottom part of the tail ash section, where a side part of the tail ash section is equipped with an air inlet that is connected with an air inlet pipeline. A dust removing device is provided with a gas outlet and a slag outlet.    USE - Boiling-type biomass gasification system.    ADVANTAGE - The system increases gas flow speed and solid substance of the fluidized bed-type biomass gasification furnace so as to reduce ash content. The system shortens pyrolysis time of a gasification furnace fuel, reduces tar content so as to prevent tar. The air inlet is located at the side of the tail ash section, which ensures smooth deslagging process.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic circuit diagram of a boiling-type biomass gasification system.
NOVELTY - The system has a furnace body arranged at bottom of a conical hopper-shaped section. A tail ash section is arranged with a cylindrical gas generating section. A side part of a gas section is provided with a gas outlet that is connected with a gas dividing pipeline. Bottom and side parts of the ash section are provided with a slag outlet and an air inlet, respectively. A fuel inlet is fixed at a top end of the gas section. A side part of a blanking pipeline is fixed with a feeding port. A fire grate is provided with a rotating pole. A feeding device is a multi-stage feed device.    USE - Biomass fuel gasification system.    ADVANTAGE - The system has compact structure, biomass raw material adaptability, high water content and high gasification efficiency, and meets requirement of water and realizes gas property for multi-section gas production process.    DETAILED DESCRIPTION - The fire grate is a water cooling fire grate.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a biomass fuel gasification system.
NOVELTY - The system has a furnace body connected with a bottom part of a conical hopper-shaped section. A tail ash section is provided with a slag outlet and fixed with an air inlet and an upper part of a surface body is arranged with a reaction section. A multi-feeding device is provided with a first feeding device and a second feeding device. A feeding port is formed on a discharging opening. A middle feeding device is connected with a middle box. A material outlet is arranged with a feed port of a biomass gasification furnace.    USE - Self-drying type biomass gasification system.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a self-drying type biomass gasification system.
NOVELTY - The method involves providing gasification furnace with a reaction section and a tail ash section that is provided with a fire grate. A feeding port is fixed with the gasification furnace, which is provided with biomass raw material. The feeding port is located on the reaction section. The gasification furnace tail ash section is entered into a gasification medium section. The biomass raw material in the gasification furnace is formed with a combustion layer, which is provided with the fire grate. Fuel gas is generated by the gasification reaction section.    USE - Boiling type biomass gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a boiling type biomass gasification method.
NOVELTY - The method involves obtaining qualified grain size by biomass fuel crushing and sieving process. Biomass particles are generated to a pyrolysis furnace by using a crushing feeding system. Hot solution rear residual ash and residual coke material are obtained by using internal and external synchronous heating process. Carbon-containing substance is converted into high temperature synthesis gas. Clean synthesis gas is generated by a purifying device, where the pyrolysis furnace synthesis gas outlet temperature is 1100 to 1300 degrees Celsius.    USE - Pressurizing coupling type biomass pyrolysis method.    ADVANTAGE - The method enables avoiding hot inertia effect and environmental pollution, providing high temperature plasma reaction, high efficiency, high carbon conversion rate, high synthesis gas quality, single processing ability and simple subsequent purification process, effectively increases air volume content up to 90 percentage, performing subsequent process without using additional compressors, saving lot of compression work, reducing system power consumption and generating synthesis gas without tar.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a pressurizing coupling type biomass pyrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a pressurizing coupling type biomass pyrolysis system.
NOVELTY - A biofuel composition comprises 78-90 wt.% methanol, 8-20 wt.% water, 0.058-0.178 wt.% silver powder, 0.058-0.178 wt.% red phosphorus powder, 0.058-0.178 wt.% ethyl acetate, 0.024-0.144 wt.% strontium carbonate, 0.058-0.178 wt.% acetone, 0.179-0.479 wt.% industrial glycerol, 0.058-0.178 wt.% ferrocene, 0.058-0.178 wt.% nitromethane and 0.179-0.479 wt.% absolute ethanol.    USE - Biofuel composition.    ADVANTAGE - The biofuel composition is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biofuel composition comprising mixing silver powder, red phosphorus powder and ethyl acetate for 5-10 minutes, adding strontium carbonate, acetone, industrial glycerol and ferrocene, stirring for 5-10 minutes, heating, adding absolute ethanol and water, adding nitromethane, stirring for 5-20 minutes, adding methanol, heating for 2-3 hours, adding water, mixing, adding methanol and water, and stirring.
NOVELTY - An alcohol composition comprises 20-50 wt.% ethanol, 30-60 wt.% biodiesel, 10-20 wt.% cosolvent, 1-2 wt.% additives, and 0.1-0.2 wt.% flash point improving agent.    USE - Alcohol composition used as fuel.    ADVANTAGE - The alcohol composition has high flash point.
NOVELTY - An alcohol composition comprises 40-70 wt.% ethanol, 30-40 wt.% biodiesel, 10-20 wt.% cosolvent, 1-2 wt.% additives and 2-6 wt.% calorific value reinforcing agent mixture.    USE - Alcohol composition used as fuel.    ADVANTAGE - The alcohol composition with high calorific value has a simple preparation.
NOVELTY - An alcohol-based fuel comprises 70 wt.% alcohol compound, 25 wt.% hydrocarbon compound and 5 wt.% additive.    USE - Alcohol-based fuel.
NOVELTY - A methanol fuel composition is prepared by mixing 3-5 pts. wt. benzene, 2-4 pts. wt. alkyl naphthalene, 1-3 pts. wt. amyl nitrate, 1-3 pts. wt. sodium dihydrogen phosphate, 4-6 pts. wt. ethylene-vinyl acetate copolymer, 15-20 pts. wt. light diesel oil, 1-3 pts. wt. tert-butyl peroxyacetate, 5-10 pts. wt. gasoline, 2-3 pts. wt. dispersing agent and 1-3 pts. wt. metal deactivators, stirring at 30-40 degrees C for 4-6 hours, adding 60-80 pts. wt. methanol, cooling to 20-25 degrees C, stirring for 2-3 hours, and standing for 10-12 hours.    USE - Method for preparing methanol fuel composition (claimed).
NOVELTY - A blended biodiesel is prepared by adding surface active agent in oil groove, stirring in stirring tank, and filtering; adding base oil, kerosene, diesel, and solvent oil No. 200, stirring, adding cetane improved agent and stabilizing agent, and maintaining for 15-30 minutes; stirring, and adding decoloring agent; stirring for 20-40 minutes, filtering, conveying to stirring tank, and heating at 40-55 degrees C for 1.5-3 hours; and taking into finished product oil tank.    USE - Method for preparation of blended biodiesel (claimed) for vehicle.    ADVANTAGE - The method has simple process flow, inexpensive and easy to obtain raw materials, high yield, and no pollution to environment.
NOVELTY - A methanol diesel comprises 15-40 pts. wt. methanol, 10-25 pts. wt. 6-12C alcohol, 15-40 pts. wt. diesel additive, and 10-44 pts. wt. national standard diesel. The national standard diesel is 50# or 10# national standard diesel. The diesel additive is polyformaldehyde dimethyl ether, n-amyl ether, and/or glycol ether.    USE - Methanol diesel.    ADVANTAGE - The diesel has simple production technique, is convenient for large-scale industrial production, has high cetane number and low sulfur content, and has exhaust gas discharge that meets the requirement of environment protection.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the diesel.
NOVELTY - A biomass clean gasoline is prepared by mixing propyl alcohol and ethanol, combustion-supporting smoke agent, dicyclopentadienyl iron, stabilizing agent, oleic acid, anti-oxygen-proof glue agent, N,N-butyl p-phenylenediamine, methyl cyclopentadienyl manganese tricarbonyl antiknock agent, catalyst, and potassium permanganate at normal temperature and normal pressure; filtering; and adding crude gasoline in the mixed solution, and fully stirring.    USE - Method for preparing biomass clean gasoline (claimed).    ADVANTAGE - The method has simple operation, abundant raw material source, and high yield.
NOVELTY - A high proportion methanol gasoline clean fuel comprises 0-10 vol.% gasoline, 5-10 vol.% light naphtha, 2-5 vol.% hydrocarbon, 0-6 vol.% solvent oil No. 120, 0-6 vol.% solvent oil No. 200, and 70-85 vol.% methanol.    USE - High proportion methanol gasoline clean fuel for car (claimed).
NOVELTY - A composite additive comprises 60-70 pts. wt. ethanol, 5-15 pts. wt. methyl acetate, and 20-30 pts. wt. acetonitrile.    USE - Composite additive used in biological oil.    ADVANTAGE - The additive reduces viscosity of biological oil, and increases biological oil storage period.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the additive.
NOVELTY - Purification of marsh gas by removing carbon dioxide (CO2) includes alternately passing pressurized marsh gas and air through absorbing container containing normal pressure water.    USE - Purification of marsh gas by removing CO2 (claimed), useful for small- and medium-sized biogas engineering.    ADVANTAGE - The method has low running energy consumption and small device investment.
NOVELTY - A biomass fuel comprises 90 wt.% wood powder and 10 wt.% combustion-promoting binder.    USE - Biomass fuel.    ADVANTAGE - The biomass fuel is environment-friendly and has good moldability. It has porous fiber structure that can absorb biomass fuel heating system flue gas tar so as to avoid tar adhesion to a granulator and eliminate cleaning difficulty problem.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the biomass fuel, comprising crushing wood powder to grain size of less than or equal to 1.8 mm, drying wood powder to water content of 12-17%, adding wood powder and combustion-promoting binder and uniformly stirring for 3-5 minutes, subjecting mixed material to mold extrusion forming process to obtain granular solid fuel, and cooling the granular solid fuel.
NOVELTY - A biomass fuel granule comprises 25-40 wt.% straw, 30-50 wt.% tree stem, 20-45 wt.% bamboo shavings, and 0.5-2 wt.% dechlorinating agent.    USE - Biomass fuel granule.    ADVANTAGE - The biomass fuel granule has low cost, high combustion value, long burning time with no harmful combustion gases, and high lignin content. It contains dechlorinating agent to reduce generation of chlorine-containing substances, and does not cause corrosion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass fuel granule, comprising crushing straw and tree stem, filtering and drying to obtain powder material, adding powder material with bamboo shavings and dechlorinating agent and uniformly mixing, then granulating the mixture, and cooling to obtain biomass fuel granule.
NOVELTY - An anti-sintering biomass fuel granule comprises 25-45 wt.% tree bark, 30-50 wt.% nut shell, 20-45 wt.% bamboo chips, and 1-3 wt.% acidic oxide.    USE - Anti-sintering biomass fuel granule.    ADVANTAGE - The anti-sintering biomass fuel granule has low cost, low content of alkaline-earth metal, high lignin content and combustion value, and long combustion time. The addition of acidic oxide can regulate biomass fuel property so that the fuel is not easy to slag and there is no discharge of harmful gases.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of anti-sintering biomass fuel granule, comprising crushing tree bark, nut shell and bamboo chips, filtering and drying to obtain powder material; uniformly mixing powder material with acidic oxide; granulating the mixed material; and cooling to obtain anti-sintering biomass fuel granule.
NOVELTY - High combustion value biomass fuel comprises 20-40% branches, 30-50% bamboo shavings and 20-40% leaves.    USE - High combustion value biomass fuel.    ADVANTAGE - The biomass fuel has long combustion time, and no harmful gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of high combustion value biomass fuel comprising crushing branch, bamboo and leaf, filtering, drying, granulating mixture, and cooling.
NOVELTY - Composite biomass fuel granule comprises 5-15% straw, 20-35% bamboo, 25-40% anthracite and 20-40% oxidant.    USE - Biomass fuel granule.    ADVANTAGE - The granule reduces ignition temperature, and is safe.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite biomass fuel granule comprising crushing raw materials, filtering, drying, removing and crushing large volume, granulating mixture, and cooling to obtain composite biomass fuel granule.
NOVELTY - Low chlorine value biomass fuel particle comprises 20-40% branches, 30-50% bamboo shavings, and 20-40% sugar cane bagasse.    USE - Low chlorine value biomass fuel particles.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of low chlorine value biomass fuel particles comprising crushing raw materials, filtering, drying, granulating, and cooling.
NOVELTY - Preparation of refuse-derived fuel comprises sorting domestic garbage, removing metal, glass and ceramic and crushing to 25-35 mm; crushing inorganic non-combustible and domestic garbage to 15-25 mm; adding 0.5-1% domestic garbage, oil-containing solid waste, 3-5% calcium oxide and 2-3% catalyst, heating at 300-400 degrees C for 0.5-2 hours, pressing under 20 MPa, and drying to obtain product.    USE - Method of preparation of refuse-derived fuel (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the preparation of refuse-derived fuel (Drawing includes non-English language text).
NOVELTY - An Orychophragmus violaceus oil (A) is prepared by physically pressing O. violaceus seed to extract O. violaceus oil.    USE - Method for preparing O. violaceus oil (A) used in preparing biodiesel (B) which can be utilized as component for diesel fuel (C) employed in e.g. aviation or internal combustion engine (claimed).    ADVANTAGE - The method is simple and economical, and can provide O. violaceus oil (A) which can be efficiently processed into high-quality biodiesel through chemical conversion.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) preparation of biodiesel (B), comprising converting O. violaceus oil (A) into fatty acid methyl ester via transesterification reaction with alcohol at 50 degrees C for 50 minutes in the presence of 1 wt.% catalyst based on 6:1 alcohol/oil (A) mole ratio to obtain biodiesel (B); and (2) a diesel fuel (C) comprising biodiesel (B).
NOVELTY - A biodiesel (I) comprises oil (A), catalyst, and organic solvent.    USE - Biodiesel (I) used as biological energy source.    ADVANTAGE - The biodiesel (I) can be prepared conveniently through base catalysis in flotation machine. The preparation process is simple, can be performed under low reaction temperature, and can provide biodiesel product with a yield that is improved by 10-30 %.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biodiesel (I), comprising:    (1) adding organic solvent and oil (A) into flotation groove of flotation machine, stirring;    (2) adding with catalyst, stirring under high speed for 5-10 minutes, introducing air at a rate of 0.45-0.75 m3/hour through flotation machine air inlet valve to generate air bubbles;    (3) reacting at 35-55 degrees C for 7-24 hours, closing the air inlet valve and stopping the stirring process; standing for 7-15 hours to separate the reaction mixture into lower layer comprising glycerol and upper layer comprising crude biological diesel; discharging the lower layer via discharge port; and    (4) continuously adding the upper layer with water to wash under stirring condition; standing for 7-8 hours to separate the mixture into lower layer comprising water and upper layer comprising biodiesel; discharging the lower layer via discharge port; and collecting the upper layer to obtain biodiesel (I).
NOVELTY - Method for production of biogas from food waste, involves (a) adding water to recovered food waste and hydraulic crushing the recovered food waste, (b) regulating the pH of the aqueous waste to be 9-10, and heating at 70-100 degrees C with stirring for 1-2 hours, (c) feeding into heat exchanger and cooling to 30-50 degrees C, (d) aerobically fermenting the mixture using aerobic bacteria for 36-48 hours, (e) then anaerobically fermenting the mixture and collecting biogas, and (f) filtering to remove plastic, metal and other solids, and collecting microbial culture.    USE - The method is useful for production of biogas from food waste. The food waste includes wastes of fruits, vegetables, meat and eggs (all claimed).    ADVANTAGE - The method overcomes the problem of too long food waste fermentation period by shortening the fermentation time, thus produces large amount of biogas.
NOVELTY - Biological organic fertilizer comprises 40-45 wt.% erythromycin bacterial residue, 20-25 wt.% tylosin bacterial residue, 10-15 wt.% rice straw, 5-10 wt.% dry yeast residue and 5-25 wt.% human waste.    USE - Biological organic fertilizer.    ADVANTAGE - The fertilizer is eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of biological organic fertilizer comprising mixing erythromycin bacterial residue, tylosin bacterial residue and human waste, processing under aerobic conditions, adding 1-2 wt.% 5% microbial solution, heating at 70-80 degrees C and oxygen concentration of 2-4 mg/mL for 5 days, cooling at 35-40 degrees C, fermenting for 10-12 days, crushing and sieving.
NOVELTY - Removal of oxalic acid during fermentation process involves fermenting corn, obtaining fermented mash, heating at 60-70 degrees C, filtering, obtaining filtrate, adding calcium carbonate and water in weight ratio of 30-50:100, stirring, adjusting pH to 3.5-4.5, reacting, obtaining reaction solution, adding perlite and water in weight ratio of 1-4:100, obtaining perlite slurry, uniformly coating the obtained perlite slurry on an upper filter cloth of plate-and-frame filter press, filtering, obtaining filtrate and removing oxalic acid.    USE - Removal of oxalic acid during fermentation process (claimed).    ADVANTAGE - The method economically enables the removal of oxalic acid during fermentation process, with high removal rate of oxalic acid, by a simple process with reduced energy consumption.
NOVELTY - The system (100) has a heat exchanger (122) having a fuel cell with an electrolyte. A steam turbine generator (112) in which water from the water source is directed adjacent the heat exchanger, and the water is converted into steam in response to heat generated by the fuel cell and the steam is directed to the steam turbine generator to produce alternating current electricity. An external power source operating the electrolysis unit receives supplemental power in response to routing a portion of the direct current electricity produced by the fuel cell to the electrolysis unit.    USE - Steam-driven electricity generating system used in applications such as power plant, to subsidize commercial and residential electricity demands, land vehicle power demands and marine craft power demands, employed in remote location such as used for hospitals, military facilities, or in moving vehicle such as submarine.    ADVANTAGE - The non-precious metals can be used as catalysts at the anode and cathode of molten carbonate fuel cell, thus the costs is reduced. Since the waste heat is captured and used, the overall fuel efficiencies can be as high as in molten carbonate fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electric generating system.    Steam-driven electricity generating system (100)    Turbine generator (112)    Water storage tank (118)    Molten carbonate fuel cell (120)    Heat exchanger (122)
NOVELTY - The reactor (20) has a first reactor (210) which gasifies injected biomass by making sand or tar pyrolysis catalyst to move along with the flow of external heat source so as to gasify biomass and to produce bio-char. A distribution plate (221) such as nickel plate is arranged between first reactor and second reactor (220), so as to prevent movement of bio-char and sand or tar pyrolysis catalyst in first reactor towards second reactor and to prevent leakage of carbon adsorbent in second reactor towards first reactor.    USE - Biomass gasification reactor used in biomass gasifier (claimed) used for electric power production applications.    ADVANTAGE - The gas production from the biomass can be economically and effectively obtained with minimized amounts of tar and ammonia. The gas having higher calorific power and low tar and ammonia content can be steadily used in the electric power production.    DETAILED DESCRIPTION - The second reactor connected to first reactor, is filled with carbon adsorbent so as to decrease the content of the tar in the gas produced in the first reactor and to increase hydrogen production for the supply of the gas to a subsequent process. An INDEPENDENT CLAIM is included for biomass gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gasifier including the biomass gasification reactor.    Biomass gasification reactor (20)    Reactors (210,220)    Pipe (211)    Accommodating chamber (212)    Distribution plate (221)
NOVELTY - A device (1) for transforming organic matters, comprises transformation chamber (2) provided with inlet (3), for introducing into the chamber organic matters to be decomposed, and outlet (4) for decomposed organic substances, obtained by transformation of the organic matters introduced in the chamber; circuit (5) for supplying superheated steam, which leads to the chamber, for the conveyance and subsequent transfer of heat, carried by the superheated steam, to the organic matters, and for their consequent decomposition into organic substances with short molecular chains.    USE - As device for transforming organic matters (claimed).    ADVANTAGE - The device is capable of decomposing organic matters constituted by carbon chains, such as cellulose, paper or wood; is capable of decomposing organic matters constituted by carbon chains effectively and practically; without releasing, during the process, polluting and/or explosive products; that ensures high reliability in operation; can be obtained easily starting from commonly commercially available elements and materials; and has low costs and is safe in application. The choice to resort to superheated steam allows utilization of a fluid that has high specific heat and does not cause oxidation. The chamber is thus completely saturated and filled by the superheated steam and instead air is entirely absent, thus avoiding the danger of forming oxidizing elements (potentially explosive, toxic, dangerous and polluting). The use of a circuit for feeding superheated steam leads to the chamber assigned to the transformation of organic matters constituted by carbon chains, allows adding heat to them, causing their decomposition into organic substances having short molecular chains.    DESCRIPTION OF DRAWING(S) - The figure shows perspective view of transforming device.    Transforming device (1)    Transformation chamber (2)    Inlet (3)    Outlet (4)    Circuit (5)    Nozzle (6)
NOVELTY - Producing a synthesis gas, comprises: (a) adsorbing water by reacting a solid acid mixture comprising a carbon compound and a solid acid with water or steam; (b) producing hydrogen by introducing the water-adsorbed solid acid mixture into a reactor and splitting the water adsorbed on the solid acid mixture; (c) producing a synthesis gas by reacting the produced hydrogen with the carbon compound in the reactor; and (d) discharging the produced synthesis gas out of the reactor.    USE - The method is useful for producing a synthesis gas (claimed), preferably methane.    ADVANTAGE - The method provides the synthesis gas in an environmentally friendly manner.    DETAILED DESCRIPTION - Producing a synthesis gas, comprises: either (a) adsorbing water by reacting a solid acid mixture comprising a carbon compound and a solid acid with water or steam, (b) producing hydrogen by introducing the water-adsorbed solid acid mixture into a reactor and splitting the water adsorbed on the solid acid mixture, (c) producing a synthesis gas by reacting the produced hydrogen with the carbon compound in the reactor, and (d) discharging the produced synthesis gas out of the reactor; or (e) preparing a water mixture comprising water and a carbon compound and a water mixture comprising water, a carbon compound and a solid acid, (f) producing hydrogen by introducing the water mixture into a rock formation located at the bottom of an underground bedrock reactor having a bedrock covering structure and reacting the water mixture with a solid acid included in the rock formation or with the solid acid included in the water mixture, (g) producing a synthesis gas by reacting the produced hydrogen with a carbon compound included in the rock formation or with the carbon compound included in the water mixture, and (h) discharging the produced synthesis gas out of the reactor.
NOVELTY - A gas-producing reactor (1) consists of a housing (11) with a combustion portion accommodating a fluidized bed (7) in operation, a riser (2) extending along a longitudinal direction of the reactor, a downcomer (3) positioned coaxially around the riser and extending into the fluidized bed, and feed channel(s) (8) for providing fuel to the riser. The riser is attached to the housing at the bottom. A portion of the riser above the feed channel(s) is moveable with respect to the downcomer in the longitudinal direction of the reactor.    USE - Reactor is used for producing product gas from fuel, e.g. biomass gasification (claimed) used for producing fuel for boilers, gas engines, and gas turbines.    ADVANTAGE - The reactor is reliable and endurable, even after several starts and stops. Since a portion of the riser is moveable with respect to the downcomer in the longitudinal direction of the reactor, the riser can thermally expand with respect to the downcomer channel, as a result of which no thermal fatigue of the reactor component occurs. The arrangement of feed channels allows for efficient operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the reactor.    Reactor (1)    Riser (2)    Downcomer (3)    Fluidized bed (7)    Feed channels (8)    Housing (11)
NOVELTY - Sustainable purification of water by application of a number of intermediate steps which include (membrane)filtration, water softening and aeration, involves: (i) degassing water; (ii) incinerating the gases obtained in step (i); and (iii) further treating the degassed water obtained in step (i) in one or more intermediate steps, where the released incineration products in step (ii), in particular carbon dioxide (CO2) and water, energy, heat are at least in part usefully re-used in one or more of the intermediate steps.    USE - The process is useful for sustainable purification of water by application of a number of intermediate steps which include (membrane)filtration, water softening and aeration(claimed).    ADVANTAGE - The gases present in the water to be purified are reused in a useful way. The release into the atmosphere of gases present in the water to be treated is limited to a minimum. The gases present in the water to be treated are recovered and the gases are converted into products or energy streams which can be further used in the treatment of the water to be purified.
NOVELTY - Preparation of ester involves reacting reaction mixture containing organic acid with dialkyl carbonate in the presence of alcohol-containing solvent, without an extrinsic catalyst.    USE - Preparation of ester used for esterification method used for formation of ester compound (all claimed).    ADVANTAGE - The method enables the preparation of ester having high yield with effective separation process, and is simple, economical, and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for esterification method, which involves reacting reaction mixture containing organic acid and dialkyl carbonate with alcohol-mediating agent, without an extrinsic acid or a base catalyst.
NOVELTY - A recombinant polypeptide comprising an amino acid sequence that is at least 75% identical to the amino acid sequence of fully defined approximately 900 amino acids (SEQ ID NO: 2) or fully defined approximately 900 amino acids (SEQ ID NO: 3), given in the specification, where the polypeptide has beta-glucosidase activity, is new.    USE - The recombinant polypeptide, composition and methods are useful for producing a beta-glucosidase; and for hydrolyzing a lignocellulosic biomass substrate (all claimed); and for degrading or hydrolyzing lignocellulosic biomass.    ADVANTAGE - The recombinant polypeptide has improved efficacy or capability to hydrolyze cellulosic feedstock.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a composition comprising the recombinant polypeptide, further comprising one or more other cellulases;    (2) a nucleic acid encoding the recombinant polypeptide;    (3) an expression vector comprising the nucleic acid in operable combination with a regulatory sequence;    (4) a host cell comprising the expression vector;    (5) a method of producing a beta-glucosidase, comprising: culturing the host cell in a culture medium, under suitable conditions to produce the beta-glucosidase; and    (6) a method for hydrolyzing a lignocellulosic biomass substrate, comprising: contacting the lignocellulosic biomass substrate with the polypeptide, or the composition, to yield a glucose or other sugars.
NOVELTY - The system (10) has electrolysis continuation unit (82) which continues electrolytic treatment by high pressure water electrolyzer until the water level in gas-liquid separation apparatus (14) reaches upper limit water level threshold value at time of system breakdown. A depressurization process unit (86) depressurizes cathode, when water level in gas-liquid separation apparatus attains upper limit water level threshold. The water level in gas liquid separation apparatus is drained to minimum water level threshold, while supplying hydrogen to gas-liquid separation apparatus.    USE - High-pressure water electrolysis system.    ADVANTAGE - The amount of hydrogen discarded can be reduced favorably and the gas-liquid separation apparatus is maintained by filled-up state, when high-pressure water electrolysis system stops, so that system efficiency can be improved. The high capacitance storage tank is not used as hydrogen storage apparatus, so that manufacturing cost can be reduced. The durability of pressure-reduction valve can be improved effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operating method of the high-pressure water electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the explanatory high-pressure water electrolysis system. (Drawing includes non-English language text)    High-pressure water electrolysis system (10)    Gas-liquid separation apparatus (14)    Hydrolyzing cell (30)    Electrolysis continuation unit (82)    Depressurization process unit (86)
NOVELTY - Producing (P1) a diesel boiling range hydrocarbon comprises: contacting at least one fossil-based oil and at least one renewable based oil with hydrogen in the presence of a catalyst; and performing a separation to obtain the diesel boiling range hydrocarbon.    USE - The process is useful for producing a diesel boiling range hydrocarbon (claimed) used for fuel purposes, diesel oil, diesel fuel or co-processed diesel fuel.    ADVANTAGE - The process: provides diesel boiling range fraction including high content of at least one paraffinic product comprising pentadecane, n-hexadecane, n-heptadecane or n-octadecane, and having enhanced cetane number compared to conventional diesel fuel that is 57-75 and increased heating value compared to conventional diesel fuel, and conversion ratio of the fossil-based fuel source and renewable-based fuel source to an intermediate hydrocarbon product which is 85% including 65% diesel boiling range hydrocarbon (all claimed); and does not require investment or equipment modification.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) producing (P2) diesel boiling range hydrocarbon comprising: contacting a set of input fuel source streams including renewable based oil with hydrogen in the presence of a nickel molybdenum-based catalyst; and performing a separation procedure to obtain the diesel boiling range hydrocarbon; and    (2) the diesel boiling range hydrocarbon produced by the process (P1).
NOVELTY - Method for preparing biocrude from wet biomass involves (a) providing the wet biomass, heating the wet biomass for a first period of time from ambient temperature to a first temperature of 100-600 degrees C to form a reaction mixture comprising the biocrude, and optionally heating the reaction mixture at the first temperature for a second period of time, where the first period of time and the second period of time are collectively less than 180 seconds.    USE - The method is useful for preparing biocrude from wet biomass (claimed).    ADVANTAGE - The method enables to prepare biocrude with fewer impurities, rapidly with improved yield as compared with existing method, and cost-effectively.    DETAILED DESCRIPTION - Method for preparing biocrude from wet biomass involves (a) providing the wet biomass, heating the wet biomass for a first period of time from ambient temperature to a first temperature of 100-600 degrees C to form a reaction mixture comprising the biocrude, and optionally heating the reaction mixture at the first temperature for a second period of time, where the first period of time and the second period of time are collectively less than 180 seconds or (b) providing the wet biomass, selecting a set point temperature of at least 300 degrees C, and heating the wet biomass at the set point temperature such that the wet biomass is heated from ambient temperature at the set point temperature for a period of time of less than 180 seconds, thus forming reaction mixture comprising the biocrude.
NOVELTY - An organic acid fermentation liquid is passed through an ultrafiltration membrane having molecular weight cutoff of 3500 or less, to obtain a membrane-permeable liquid. The membrane-permeable liquid is crystallized, to produce organic acid or its salt. The organic acid fermentation liquid contains glucose which is derived from raw material of cellulose-containing biomass.    USE - Manufacture of organic acid or its salt used as monomer of plastics.    ADVANTAGE - The method is easy, and enables manufacture of high pure organic acid or its salt, with high yield. The organic acid contributes to break away dependence on fossil resources. Fouling of reverse osmosis membrane during filtration process is suppressed, even when using concentrated liquid. Energy consumption is reduced during purification of organic acid.
NOVELTY - Fluid-catalytic cracking of pyrolysis oil derived from biomass-containing material involves preparing partially-deoxygenated pyrolysis oil by subjecting a feed comprising pyrolysis oil to hydro-deoxygenation process, forming a preheated hydrocarbon feed by heating the hydrocarbon feed at 50-200 degrees C, obtaining feed mixture by mixing partially-deoxygenated pyrolysis oil and preheated hydrocarbon feed, contacting the feed mixture with a catalytic cracking catalyst in catalytic cracking reactor at 400 degrees C or more, and preparing product stream containing one or more cracked products.    USE - Fluid-catalytic cracking of pyrolysis oil derived from biomass-containing material e.g. cellulosic or lignocellulosic material used for recovery of biofuel and biochemical components (all claimed).    ADVANTAGE - The method enables the cracking of pyrolysis oil with catalytic cracking catalyst having high catalytic activity, by simple and economical process, and suppresses the coking of feed pipelines and atomizing nozzles.
NOVELTY - Liquefied propellant composition comprises 5-8 wt.% of nitrous oxide and/or carbon dioxide dissolved in a mixture of two or more hydrocarbons consisting of cyclopentane, isohexane, 2,3-dimethyl-butane, 3-methyl-pentane and 2,2-dimethyl-butane.    USE - The liquefied propellant composition is useful for producing aerosol spray (claimed) for an engine.    ADVANTAGE - The liquefied propellant composition produces the aerosol with improved stability, reduced inflammability, and good distribution of dimensions of particle and percentage of sedimentation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing the liquefied propellant composition, comprising (a) introducing 92-95 wt.% of a mixture of two or more hydrocarbons comprising cyclopentane, isohexane, 2,3-dimethyl-butane, 3-methyl pentane and 2,2-dimethyl-butane into a reactor equipped with thermostatic valves, and (b) bubbling 5-8 wt.% of nitrous oxide and/or carbon dioxide;    (2) an aerosol composition comprising the liquefied propellant composition; and    (3) conditioning the aerosol composition, comprising introducing 5-20 wt.% of an active ingredient or mixture of active ingredients into an aerosol package, adjusting a valve on the aerosol package so that it is hermetically closed, and introducing 80-95 wt.% of the propellant composition into the aerosol package.
NOVELTY - Process (P1) for converting a solid biomass material, comprises: (a) providing a pneumatic fluid; (b) dispersing the solid biomass material into the pneumatic fluid to prepare a pneumatic dispersion and transporting the pneumatic dispersion to a reactor; and (c) contacting the pneumatic dispersion with a catalyst in the reactor to produce a product stream comprising at least one conversion product.    USE - The process is useful for converting a solid biomass material (claimed), which is useful for producing a biofuel and/or biochemical.    ADVANTAGE - The process utilizes solid biomass material that have undergone drying, demineralization, torrefaction, steam explosion, particle size reduction, densification and/or pelletization before being dispersed into the pneumatic fluid, thus allowing for improved process operability and economics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fluid catalytic cracking process (P2) for converting a solid biomass material, comprising: step (a) as above per se; dispersing the solid biomass material into the pneumatic fluid to prepare a pneumatic dispersion; and contacting the pneumatic dispersion with a fluid catalytic cracking catalyst in a fluid catalytic cracking reactor to produce the product stream.
NOVELTY - A bioethanol manufacturing apparatus (1) comprises fermentation unit (2) to obtain fermentation solution which ferments saccharified solution of biomass and contains bioethanol, transfer unit (3) to transfer fermentation solution, extraction unit (4) where solvent extraction of bioethanol from fermentation solution transferred by transfer unit is carried out, and protein removal unit (6) to separate and remove protein contained in fermentation solution in the middle of transfer unit.    USE - A bioethanol manufacturing apparatus (claimed).    ADVANTAGE - The bioethanol manufacturing apparatus can efficiently extract bioethanol from fermentation solution and can suppress deterioration of extracting solvent.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the bioethanol manufacturing apparatus. (Drawing includes non-English language text).    Bioethanol manufacturing apparatus (1)    Fermentation unit (2)    Transfer unit (3)    Extraction unit (4)    Protein removal unit (6)
NOVELTY - Preparation of acrylate ethylene urea involves adding acrylic acid (II), N-hydroxyethyl ethylene urea (III) and polymerization inhibitor in the presence of catalyst, heating and condensing, preparing ethyl acrylate and ethylene urea with azeotropic aqueous medium, refluxing with water, performing water stratification, continuously separating water from the reaction system.    USE - Preparation of acrylate ethylene urea used in organic synthesis field.    ADVANTAGE - The acrylate ethylene urea is efficiently prepared with high yield without polluting the environment.    DETAILED DESCRIPTION - Preparation of acrylate ethylene urea involves adding acrylic acid of formula: H2C=C(-H)-COOH (II), N-hydroxyethyl ethylene urea of formula (III) and polymerization inhibitor in the presence of catalyst, heating and condensing, preparing ethyl acrylate and ethylene urea with azeotropic aqueous medium, refluxing with water, performing water stratification, continuously separating water from the reaction system. The acrylate ethylene urea is of formula (I).
NOVELTY - An unsteady in situ surface chemical reaction representation method involves using coal oxygen surface reaction, crushing and sieving coal. The sieved coal is transferred to surface reaction device, followed by passing carrier gas and adsorbed gas according to a certain flow rate, raising the temperature to experimental preset temperature, contacting coal sample with reaction gas adsorbed in the surface during the experiment, and transferring gas produced in the surface reaction device to gas purifier and separating device to separate hydrogen, carbon dioxide, carbon monoxide, and methane gas.    USE - Method for representation of unsteady in situ surface chemical reaction.    ADVANTAGE - The method enables representation of unsteady in situ surface chemical reaction with better accuracy.    DETAILED DESCRIPTION - An unsteady in situ surface chemical reaction representation method involves using coal oxygen surface reaction, crushing and sieving coal to required grain diameter. The sieved coal is transferred to surface reaction device, followed by passing carrier gas and adsorbed gas according to a certain flow rate, raising the temperature to experimental preset temperature, contacting coal sample fully with reaction gas adsorbed in the surface during the experiment, transferring gas produced in the surface reaction device to gas purifier and separating device to separate hydrogen, carbon dioxide, carbon monoxide, and methane gas. The separated gas is transferred to detection and control system for quantitative analysis of gases. The separated gas is transferred to another detection system for synchronous online qualitative review analysis. An INDEPENDENT CLAIM is also included for a unsteady in situ surface chemical reaction representation device.
NOVELTY - Substrates conversion involves using a catalytic system formed by one or multiple enzymes supported by using ionic liquid, where the enzyme is selected from lipases.    USE - Modification method for converting substrates based on enzymatic catalysis reactions.    ADVANTAGE - Modification processes of biodiesel or other substrates of fatty acids and their derivatives by epoxidation reactions supported by enzymatic catalysis in ionic liquids and their applications.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composition, which comprises lipases and ionic substrates for modification via enzymatic catalysis in heterogeneous or homogeneous reaction medium.
NOVELTY - Fertilizer preparation involves collecting waste including tobacco, then grinding the material, and then performing high-temperature and high-pressure sterilizing and separating process. Tobacco wastes, nutrients and auxiliary material in mass ratio of 70-75:10-20:10-20 and water content is adjusted to 50-60%. All the materials are kept in fermentation tank maintained 75 degrees C for 7-10 days with stirring 2 times daily. After this fermentation is carried out at 45-55 degrees C for 5-10 days. After the end of fermentation, the fermented material is dried and then packaged to obtain finished product.    USE - Method for preparing fertilizer (claimed) used for preventing growth of pathogenic bacteria and weed.    ADVANTAGE - The fertilizer promotes soil granule structure and fertility, improves soil microbial activity and tobacco quality, and prevents soil-borne disease.
NOVELTY - Producing hydrogen using solar energy and cyanobacteria, is claimed. The method utilizes hydrogen-producing cyanobacteria and produces hydrogen under the action of solar energy.    USE - The hydrogen is useful in fuel cell (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use method of the hydrogen in fuel cell, comprising (i) culturing Anabaena cylindrica under conditions of constant temperature, continuous illumination and liquid ventilation culture and storing the seed culture in solid agar BGII(+N) culture medium flat plate; (ii) growing in a culture medium for specific concentration, packing into an anaerobic inducing container, adding dichlorophenyl dimethylurea, maintaining anaerobic environment and sealing the test tube; and (iii) collecting hydrogen produced in the step (ii), coupling hydrogen production cyanobacteria and the fuel cell, connecting photosynthetic hydrogen production cyanobacteria container with the fuel cell anode via a silicon glue soft pipe, at the same time, using air pump providing air and oxygen to cathode material of lithium ion battery, and producing electric energy from the fuel cell.
NOVELTY - A Fischer-Tropsch synthesis method involves utilizing synthesis gas of hydrogen/carbon monoxide as a raw material and cobalt-based Fischer-Tropsch synthetic catalyst at a reaction temperature of 18-250 degrees C and reaction pressure of 1-4 MPa, where molar ratio of the synthesis gas is 1-3, the gas hourly space velocity is 600-2500 h-1 and catalyst is perovskite structure of composite metal oxide.    USE - Fischer-Tropsch synthesis method.    ADVANTAGE - The method enables realizing long-term operation stability and low methane selectivity.    DETAILED DESCRIPTION - A Fischer-Tropsch synthesis method involves utilizing synthesis gas of hydrogen/carbon monoxide as a raw material and cobalt-based Fischer-Tropsch synthetic catalyst at a reaction temperature of 18-250 degrees C and reaction pressure of 1-4 MPa, where molar ratio of the synthesis gas is 1-3, the gas hourly space velocity is 600-2500 h-1, catalyst is perovskite structure of composite metal oxide (ABO3-y), A is a rare earth metal and/or alkaline earth metal, B is mole of transition metal, y is number of moles of oxygen present in the composite oxide.
NOVELTY - Wastewater treatment involves: performing breeding and acclimatization of activated sludge; supplying wastewater to an aeration basin and a bioreactor equipped with a membrane, preferably submerged membrane bioreactor (SMBR); conditioning the activated sludge with a predetermined concentration of biomass; running synthetic waste feed with a predetermined concentration of chemical oxygen demand (COD) into SMBR; conducting observations and calculations of flux of SMBR; performing cleaning using an acid and an alkaline; and restoring the performance of the membrane.    USE - The method is useful for treating industrial and domestic wastewater.    ADVANTAGE - The method is capable of easily treating industrial and domestic wastewater without using high technology, and can reduce the load of COD up to 99%.    DETAILED DESCRIPTION - Wastewater treatment involves: performing breeding and acclimatization of activated sludge; using wastewater with a certain flow rate supplied to the aeration basin and bioreactor equipped with a membrane, preferably submerged membrane bioreactor (SMBR); conditioning the activated sludge with a predetermined concentration of biomass; running synthetic waste feed with a predetermined concentration of chemical oxygen demand (COD) into SMBR containing activated sludge with a predetermined concentration; conducting observations and calculations of flux of SMBR; performing cleaning using an acid and an alkaline, preferably hydrochloric acid and 2% sodium hydroxide, when the membrane is no longer efficient based on the calculation of flux; and restoring the performance of the membrane by backflushing and backwash.
NOVELTY - A high purity tea polyphenol is prepared by removing processing, microwave extracting, film concentrating and extracting, absorbing, and analyzing.    USE - Method for industrial production of high purity tea polyphenol (claimed).    ADVANTAGE - The method has high extracting rate, low cost, reduced pollution, low energy consumption, and high yield, making it suitable for industrial production.
NOVELTY - Method for isolating and identifying marine phytoplankton, involves (a) taking samples of marine phytoplankton cultures comprising bacteria and other microorganisms e.g. Protozoa, (b) transferring the marine phytoplankton in a new culture medium, (c) selecting the marine phytoplankton to plant cells on jelly-like medium comprising a Arschat medium, (d) observing growth of phytoplankton under the microscope, (e) taking phytoplankton that are not associated with bacterial cells, (f) growing the cell, and (g) mass culturing the cells in Arschat medium.    USE - The method is useful for isolating and identifying marine Phytoplankton which is useful for preparing biofuel, preferably bioethanol (all claimed).    ADVANTAGE - The method is environmentally-friendly, and has maximum carbohydrate content.    DETAILED DESCRIPTION - Method for isolating and identifying marine phytoplankton, involves (a) taking samples of marine phytoplankton cultures comprising bacteria and other microorganisms e.g. Protozoa, (b) transferring the marine phytoplankton in a new culture medium, (c) selecting the marine phytoplankton to plant cells on jelly-like medium comprising a Arschat medium, (d) observing growth of phytoplankton under the microscope for every 3-5 days, (e) taking phytoplankton that are not associated with 2-5 bacterial cells to be grown in a new Arschat medium, (f) growing the cell for 8-15 days at an specific interval, and (g) mass culturing the cells in Arschat medium. An INDEPENDENT CLAIM is included for method for purifying biofuel, preferably bioethanol products from fermented biomass of the marine phytoplankton, which involves (a) distilling the biomass for at least three times and repeating the distillation to obtain 96% bioethanol, and (b) dehydrating bioethanol, adding calcium chloride and acidic zeolite and obtaining 99.75% bioethanol.
NOVELTY - An enzyme solution for removing ortho-nitrobenzaldehyde comprises water solution or buffer solution containing 0.03-0/1 mg/ml ortho-benzeneformaldehyde degrading enzyme, and 0.1-0.3 mM magnesium chloride (MgCl2), where pH value of buffer solution is 6.5-8. The enzyme has specific amino acid sequence. The buffer solution contains sodium phosphate buffer.    USE - As an enzyme solution for removing ortho-nitrobenzaldehyde (claimed).    ADVANTAGE - The process has low cost, which is good for large scale popularization; has simple and safe operation; has mild reaction condition; and does not form secondary pollution.    DETAILED DESCRIPTION - An enzyme solution for removing ortho-nitrobenzaldehyde comprises water solution or buffer solution containing 0.03-0/1 mg/ml ortho-benzeneformaldehyde degrading enzyme, and 0.1-0.3 mM magnesium chloride (MgCl2), where pH value of buffer solution is 6.5-8. The enzyme has amino acid sequence containing 482 amino acids (SEQ ID NO: 1), as given in the specification. The buffer solution contains sodium phosphate buffer. An INDEPENDENT CLAIM is included for preparation of enzyme solution sample involving selecting recombinant plasmid's strain containing nbaA gene fragment by Luria Bertani (LB) culture medium, culturing at 37 degrees C, adding isopropyl beta -D-1-thiogalactopyranoside (IPTG) until the final concentration becomes 1 mM, then at 20 degrees C overnight expression, centrifuging and collecting the cell, controlling the pH to 7.5 using phosphate buffer solution in the ice water bath, ultrasonic crushing the cell for 15 seconds, centrifuging for 10000 g for 30 minutes at 4 degrees C to remove cell debris, and extracting the supernatant to obtain crude enzyme extracted solution, extracting the solution using station type histidine tag protein purification reagent and purifying to obtain the purified enzyme solution sample.
NOVELTY - Culturing freshwater microalgae comprises producing fresh water microalgae containing a lipid by culturing microalgae strains in a culture medium. The culture medium includes 3-5 wt.% of closed mine drainage, and has iron ore concentration of 7-12 mg/l.    USE - The method is useful for culturing a freshwater microalgae for producing biodiesel using a wastewater such as livestock wastewater, agricultural wastewater, industrial wastewater, sewage sludge, sewage treatment plant inflow water and an effluent of sewage treatment plants (all claimed).    ADVANTAGE - The method efficiently and economically cultures the freshwater microalgae with high growth thus producing high quality biodiesel.
NOVELTY - Method for culturing fresh water microalgae for biodiesel production, involves culturing fresh water microalgae containing lipid in culture medium under salinity controlled condition, where the salinity of the culture medium is controlled using 2-12% 25-200 mM sodium chloride.    USE - The method is useful for culturing fresh water microalgae for biodiesel production, where the fresh water microalgae strain includes Chlamydomonas mexicana, Botryococcus braunii, Chlorella sp. and Scenedesmus sp. (all claimed).    ADVANTAGE - The method enables massive culture of microalgae with high quality of fatty acid production, improves growth rate of the microalgae, is environmentally-friendly and cost-effective, and reuses resource.
NOVELTY - A livestock and poultry manure fermentation initiator comprises glucose, cellulase, humic acid, urea, and mineral stone.    USE - Fermentation initiator used for livestock and poultry manure (claimed).    ADVANTAGE - The fermentation initiator induces and promotes inherent microbial activity, accelerates degradation of cellulose, achieves rapid fermentation of manure and other agricultural wastes, and does not cause excessive loss of nitrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fermentation of livestock and poultry manure by uniformly mixing chicken manure, pig manure, cattle manure and fungus chaff at volume ratio of 15:15:20:50 in fermentation tank; adding 2 wt.% fermentation initiator and adjusting water content to 65%; and fermenting while aerating at 2-4 L/minute/m3 every 11 o'clock in the morning for 1.5-2 hours.
NOVELTY - Preparation of bioorganic fertilizer comprises hydrolyzing microbial cell waste liquid at 108-130 degrees C for 0.5-4 hours; centrifuging or filtering; nanofiltering and ion-exchanging, or electrodialyzing; reacting with papain and lysozyme at 30-50 degrees C for 4-10 hours; and adding potassium fulvate, potassium humate, phosphorite powder and/or bone material powder to adjust nitrogen, phosphorus and potassium contents.    USE - Method for preparing bioorganic fertilizer (claimed).    ADVANTAGE - The method is environment-friendly and achieves waste recycling treatment.    DETAILED DESCRIPTION - Preparation of bioorganic fertilizer comprises adjusting water content of microbial cell waste liquid to 80-90% by adding water, adding calcined lime or concentrated sulfuric acid and uniformly stirring, and hydrolyzing at 108-130 degrees C for 0.5-4 hours; centrifuging or filtering for solid-liquid separation; nanofiltering to remove monovalent salt ions and ion-exchanging to remove divalent salt ions, or electrodialyzing to remove all salt ions; reacting with papain and lysozyme at 30-50 degrees C for 4-10 hours; and adjusting composition of water-soluble organic fertilizer in accordance with the national standard requirements by adding potassium fulvate, potassium humate, phosphorite powder and/or bone material powder to adjust nitrogen, phosphorus and potassium contents. The microbial cell waste liquid is penicillin or cephalosporin fermentation waste liquid, eutrophic lake blue-green algae, and/or city sewage treatment plant sludge.
NOVELTY - Preparation of quinolone compound comprises carrying out reduction of piperazine, adding inorganic base, decompressing and recovering.    USE - Method for preparing quinolone (claimed).    ADVANTAGE - The method is environment-friendly, high recovery rate and reduced production cost.
NOVELTY - The utility model relates to a kind of synthesis reactor and a method for synthesizing hydrazine, the synthesis reactor is provided with multiple branch pipes and connected with elbow is equipped with a high-efficient filler in step a, a high porosity is 0~80%, the two ends of the sleeve is provided with a flange, a medium flow spaces with the inner pipe of the jacket tube and the outer tube of the package flange, is provided with a medium inlet pipe and a medium outlet pipe at the two ends of the outer pipe, and the chloride amine for synthesizing hydrazine... a preparation unit, sodium hydroxide preparation unit, sodium hypochlorite preparation unit, hydrazine... The beneficial effects of the utility model are as: ammonia for producing hydrazine process has high yield and selectivity, low energy consumption and little three-waste, realizing the continuous production in a large scale, the production cost is 2/3 the chlorine amine method cost.
NOVELTY - Method of preparing fertilizer using radix paeoniae rubra and xylitol residue involves (a) adding and crushing radix paeoniae rubra residue and edible fungi; (b) weighing radix paeoniae rubra residue, xylitol residue, wheat bran, cottonseed hull, corn powder, calcium carbonate, mixed gypsum and adjusting pH; (c) cooling the substrate obtained in step (b) and fermenting by inoculating biological species; (d) preparing secondary substrate by performing above-mentioned steps (b) and (c); and (e) mixing the substrates and processing to obtain organic fertilizer.    USE - The method is useful for preparing fertilizer using radix paeoniae rubra and xylitol residue (claimed).    ADVANTAGE - The method is environmentally-friendly and reasonable and has high biological conversion rate.    DETAILED DESCRIPTION - Method of preparing fertilizer using radix paeoniae rubra and xylitol residue involves (a) adding radix paeoniae rubra residue and edible fungi and crushing to obtain particles of 0.5-3 mm size; (b) weighing 45-75 wt.% radix paeoniae rubra residue, 10-30 wt.% xylitol residue, 5-20 wt.% wheat bran, 0-20 wt.% cottonseed hull, 1-10 wt.% corn powder, 0.2-1 wt.% calcium carbonate, 0.5 wt.% mixed gypsum and adjusting pH to 7-10 using lime and water and controlling moisture content to 55-70% to obtain substrate; (c) cooling the substrate obtained in step (b) and fermenting by inoculating biological species; (d) preparing secondary substrate by performing above-mentioned steps (b) and (c) and adjusting pH to 8-10; and (e) mixing the substrates obtained in step (b) and (d) and processing to obtain organic fertilizer.
NOVELTY - Producing metalaxyl suspending agent comprises weighing and mixing the pesticide original medicine, wetting agent, dispersing agent, antifoaming agent and water in the mixing and stirring kettle uniformity, crushing, cutting, homogenizing, emulsifying, and sand mill grinding, material rear grinding of the rotary pump into the mixing kettle, adding thickening agent, preservative, anti-freezing agent, defoaming agent and water, homogenizing, mixing and defoaming under the condition of stirring, filling, high speed cutting, grinding, defoaming and transferring to the tank.    USE - Method for producing metalaxyl suspending agent (claimed).    ADVANTAGE - The method is energy-saving and environment-friendly, and has low investment cost and short period of production.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the method for producing metalaxyl suspending agent (Drawing includes non-English language text).
NOVELTY - This utility new type relates to a method for manufacturing biomass energy using device, especially the one for manufacturing biomass energy using a roasting furnace, comprising a shell, a smoke outlet and the furnace door, wherein a shell of the inner wall to the inner direction of the shell is orderly provided with a hot insulating layer and fire-resisting brick layer, the bottom of said shell fixed with a furnace core mounting platform is provided with at least one of the upper furnace core is installed on the furnace core, the furnace core and the gas collecting tube outlet end connected, the air inlet end of the gas collecting tube through a three-way valve with an air inlet and fuel gas inlet tube connected the air inlet end of the fan of a connected air inlet pipe, the inlet end of said gas inlet tube and the gas supply, said air inlet pipe and upper gas inlet tube are provided with an inner regulating tube and pressure of the flow rate adjusting valve, a regulating valve by operation with PLC control chip of control. This utility new type because of said structure has the advantages of: it reduces energy consumption, shortens the production time, reduces the labour intensity and improves the environmental protection.
NOVELTY - This utility new type relates to a method for manufacturing biomass energy using device, especially one up manufacturing biomass energy using a lifting goods basket, wherein the basket shell, in the basket of the bottom of the shell cavity fixing with a screen, the screen and the basket between the inner cavity of the shell form containing biomass of space part, and an outer wall of said basket body is provided with a hook. This utility new type because of said structure has the advantages of: it reduces the energy consumption and improves the production efficiency, reduces the labour intensity and shortens the production time.
NOVELTY - This utility new type relates to a method for manufacturing biomass energy using device, especially one for manufacturing a biomass dry distillation kettle, comprising a kettle body, a kettle cover of the kettle body is installed on the top part, the air outlet tube of the upper kettle cover, the inner cavity of the air tube and the kettle body connected, wherein the bottom plate center of said kettle body upwards, the convex part in the inner cavity of the kettle body form the hot conducting tube, time is used in conducting the hot biomass is heated in the kettle inner cavity of uniformity. This utility new type because of said structure has the advantages of: it reduces energy consumption, shortens the production time, improves the production and producing carbon efficiency.
NOVELTY - This utility new type relates to a method for manufacturing biomass energy using device, especially a straw gas one wood tar spiral separating tower, wherein it comprises two separated tower through connecting tube of connecting, a separating tower and in the inner cavity of the tower body of the tower body comprises a closed set of air inlet tube and air outlet tube on the upper tower body between the air inlet tube and the air outlet tube is provided with a separating disk tube of air inlet end to air outlet end of a separating disk tube along the tower body centre line form spiral winding is set with an overflow hole on the upper tube wall of separating disk tube the bottom of the inner cavity of the air inlet end of said connecting tube and the first stage separating tower of the air outlet tube, the air outlet end of the connecting tube and the second separation tower of air inlet tube; a first stage separating tower of the tower body is installed on the top spray head, the spray head is connected with the water source. This utility new type because of said structure has the advantages of improving the cleanness of fuel gas of straw to the user.
NOVELTY - Microorganism culture frame, between adjacent of the culture room and storeroom, culturing room and storage room set with clapboard, bottom end of baffle plate set with seal strip, left and right of plate two side card in the slot, the top part of storage room set with a liquid inlet, the bottom of culture room set with discharge port and port, only a partition in the culture room set with PH indicator and thermometer, culture room and storage room in the neck set with U-shaped seal groove, card in the U-shaped seal groove, the clapboard can be up and down in the U-shaped seal groove. This utility new type, the structure is simple and compact, it can continuously culture of microorganism in the continuous function of system, to input a biochemical pool, improve the efficiency of sewage treatment, reduces sludge discharging amount.
NOVELTY - This new type utility claims one a hydrogen engine, a hydrogen combustion engine comprising: provide programmable adjustable constant current power supply device of electric current, hydrogen-oxygen generating device, a check device and gas spray gun, a constant-current power supply device and hydrogen-oxygen generating device through the connecting circuit, the device and the inverted device through the connecting pipeline, a gas gun through pipeline with a check device connect. This utility new type by the constant-current power supply device, generating device, a check device and a separated from the gas spray gun to modularization of mode, the utility model is new type for individual and of each module are very convenient, and can be targeted to maintain each module component, the actual operation is convenient and practical, and the modularized structure device of produce in the working of the temperature easily, not the electrolytic solution the device would produce high temperature occurs, the electrolysis of hydrogen purity, hydrogen mass obtain, combustion-supporting effect of hydrogen is greatly improved, which can reach the needed of the boiler combustion heat.
NOVELTY - A quinatic acid derivative (I) is new.    USE - Quinatic acid derivative used for preventing and treating type II diabetes.    ADVANTAGE - The environment-friendly preparation is easy to operate. The compound is stable and easy to store.    DETAILED DESCRIPTION - A quinatic acid derivative of formula (I), its salt or ester is new. An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - The system comprises a reaction tank, a feed tube, and an electrodialysis cell. The electrodialysis cell comprises an anode, a cathode, a cationic membrane, and an anionic membrane. The tube has outlets. The electrodialysis cell is attached to a reaction tank.    USE - The system is useful for producing praziquantel (claimed).    ADVANTAGE - The system produces praziquantel with reduced environmental pollution.
NOVELTY - Method of preparing new fertilizer using kitchen waste resource involves (a) recycling kitchen waste and heating obtained mixture to obtain soft material; (b) carrying out hydraulic crushing of obtained soft material; (c) screening crushed waste and mixing with water to obtain mixture; (d) heating and sieving obtained mixture; (e) filtering mixture and removing plastic, metal and other solid materials; (f) fermenting the filtrate by inoculating optional biological strain; and (g) performing spray granulation of fermented mixture to obtain product.    USE - The method is useful for preparing new fertilizer using kitchen waste resource (claimed).    ADVANTAGE - The method is cost-effective and ensures to prepare high quality product.    DETAILED DESCRIPTION - Method of preparing new fertilizer using kitchen waste resource involves (a) recycling kitchen waste with a weak base and heating obtained mixture in a water bath at 20-60 degrees C for 1-2 hours to obtain soft material; (b) carrying out hydraulic crushing of soft material obtained in step (a); (c) screening the crushed waste and mixing with water to obtain a mixture; (d) heating the mixture obtained in step (c) at 60-100 degrees C for 0.4-2 hours and sieving obtained mixture; (e) filtering the mixture obtained in step (d) and removing plastic, metal and other solid materials, where the mixture comprises small molecules of carbohydrates and other substance; (f) filtering obtained filtrate and fermenting the filtrate by inoculating 20% optional biological strain at 30-50 degrees C for 7-15 days; and (g) performing spray granulation of fermented mixture and concentrating to obtain product.
NOVELTY - Agent comprises 20-30 %mass Bacillus subtilis, 20-30 %mass Aspergillus niger, 10-15 %mass Candida utilis, 15-20 %mass green Trichoderma, 10-15 %mass A.oryzae and 1-2 %mass cellulose.    USE - The agent is useful for decomposing crop straw (claimed).    ADVANTAGE - The agent has synergistic effect, and rapidly decomposes crop straw.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage method of the agent, which involves harvesting crop, placing crushed straw, scattering crop in farmyard manure, adding 150-200 pts. wt. urine or marsh gas-liquid, adding straw rotten agent, adding 3-5 times inoculant fine soil, uniformly scattering, turning cover, and controlling straw and soil when water content is 60%.
NOVELTY - Bioorganic fertilizer comprises 12.5-26 %mass castor, 18.5-25.5 %mass feather, 18-25 %mass meat and bone meal, 14-21.8 %mass waste wooden meal, 15-23.4 %mass coffee residue and 0.1-0.2 %mass composite microorganisms.    USE - As bioorganic fertilizer for tobacco.    ADVANTAGE - The fertilizer has high organic matter content, improves soil quality and improves growth of tobacco.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the bioorganic fertilizer, which involves selecting the above-mentioned raw materials except composite microorganism and placing in workshop, preparing composite microorganism using the 20-27 %mass fungal composition, 10-16 %mass bacteria, 18-27 %mass Actinobacteria, 3-6 %mass salt, 7-18 %mass rice vinegar, 10-15 %mass millet, and 7-16 %mass sugar, fermenting the feather at normal temperature by adding 40-50% composite microorganism, mixing the remaining composite microorganism into the remaining raw materials, mixing and stirring, stacking the concentrate, where each time turning every 1-3 days at 30-50 degrees C for 20-40 days, crushing the waste wooden meal, coffee residue, and castor by crusher, fermenting at normal temperature for 8-10 days, mixing and granulating the concentrate, mixing and stirring uniformly and obtaining product.
NOVELTY - Bioorganic fertilizer comprises 18.4-34 %mass tobacco stem, 17.5-26.5 %mass feather, 10.5-18 %mass meat and bone meal, 12.5-20 %mass waste wooden meal, 16.3-26 %mass mushroom and 0.1-0.2 %mass composite microorganisms.    USE - As bioorganic fertilizer for tea.    ADVANTAGE - The fertilizer has high organic matter content, improves soil quality and improves growth of tea.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the bioorganic fertilizer, which involves selecting the above-mentioned raw materials except composite microorganism and placing in workshop, preparing composite microorganism using the 18-28 %mass fungal composition, 10-18 %mass bacteria, 28-39 %mass Actinobacteria, 2-6 %mass salt, 3-9 %mass rice vinegar, 4-12 %mass millet, and 9-14 %mass sugar, fermenting the feather at normal temperature by adding 40-50% composite microorganism, mixing the remaining composite microorganism into the remaining raw materials, mixing and stirring, stacking the concentrate, where each time turning every 1-3 days at 28-40 degrees C for 28-32 days, crushing the waste wooden meal, waste mushroom, and tobacco stem by crusher, fermenting at normal temperature for 8-10 days, mixing and granulating the concentrate, mixing and stirring uniformly and obtaining product.
NOVELTY - Bioorganic fertilizer comprises 12.5-26 %mass tobacco stem, 18.5-25.5 %mass feather, 18-25 %mass meat and bone meal, 14-21.8 %mass waste wooden meal, 15-23.4 %mass rice straw and 0.1-0.2 %mass composite microorganisms.    USE - As bioorganic fertilizer for flower.    ADVANTAGE - The fertilizer has high organic matter content, improves soil quality and improves growth of flowers.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the bioorganic fertilizer, which involves selecting the above-mentioned raw materials except composite microorganism and placing in workshop, preparing composite microorganism using the 19-27 %mass fungal composition, 10-16 %mass bacteria, 30-39 %mass Actinobacteria, 2-6 %mass salt, 3-7 %mass rice vinegar, 5-10 %mass millet, and 12-14 %mass sugar, fermenting the feather at normal temperature by adding 40-50% composite microorganism, mixing the remaining composite microorganism into the remaining raw materials, mixing and stirring, stacking the concentrate, where each time turning every 1-3 days at 28-32 degrees C for 28-40 days, crushing the waste wooden meal, rice straw, and tobacco stem by crusher, fermenting at normal temperature for 8-10 days, mixing and granulating the concentrate, mixing and stirring uniformly and obtaining product.
NOVELTY - Bioorganic fertilizer comprises 22.3-32.4 %mass waste mushroom, 18.5-25.5 %mass feather, 15-21 %mass meat and bone meal, 14-18 %mass waste wooden meal, 14-19 %mass rice straw and 0.1-0.2 %mass composite microorganisms.    USE - As bioorganic fertilizer for fruit and vegetable.    ADVANTAGE - The fertilizer has high organic matter content, improves soil quality and improves growth of fruit and vegetable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the bioorganic fertilizer, which involves selecting the above-mentioned raw materials except composite microorganism and placing in workshop, preparing composite microorganism using the 20-27 %mass fungal composition, 10-16 %mass bacteria, 30-39 %mass Actinobacteria, 3-6 %mass salt, 3-7 %mass rice vinegar, 5-10 %mass millet, and 8-16 %mass sugar, fermenting the feather at normal temperature by adding 40-50% composite microorganism, mixing the remaining composite microorganism into the remaining raw materials, mixing and stirring, stacking the concentrate, where each time turning every 1-3 days at 28-40 degrees C for 28-32 days, crushing the waste wooden meal, waste mushroom, and rice straw by crusher, fermenting at normal temperature for 8-10 days, mixing and granulating the concentrate, mixing and stirring uniformly and obtaining product.
NOVELTY - Cavity type negative pressure fermentation method involves uniformly mixing to-be fermented culture material, setting ground layer plane cavity and ensuring gas exchange of bottom layer culture material, adding the culture material into the plane cavity upper portion which is provided with exhaust pipeline provided with exhaust device, sealing plastic greenhouse on the surface of culture material, performing heat preservation, and regulating greenhouse air status.    USE - The method is useful for cavity type negative pressure fermentation process (claimed).    ADVANTAGE - The method enables to perform fermentation process with less energy consumption, and cost-effectively, and conveniently.    DETAILED DESCRIPTION - Cavity type negative pressure fermentation method involves uniformly mixing to-be fermented culture material according to required proportion, setting ground layer plane cavity and ensuring gas exchange of bottom layer culture material, adding the culture material into the plane cavity upper portion which is provided with exhaust pipeline provided with exhaust device, where the exhaust device is provided to supply oxygen during fermentation process, and negative pressure within the abdominal cavity, uniformly entering fresh air into microorganism of solid state fermentation material which is pile movable through gap of the culture material, sealing plastic greenhouse on the surface of culture material, performing heat preservation, and regulating greenhouse air status.
NOVELTY - Garden greening, highly nutrient and environmentally-friendly compound fertilizer comprises organic waste, fermented Bacillus, nitrogenous fertilizer, and calcium superphosphate. The compound fertilizer is prepared by mixing, stirring, and stacking the above-mentioned raw materials, and performing fermentation at 30-55 degrees C for 120-240 hours, where the carbon, nitrogen, phosphorus and potassium ratio of the fermented organic matter is 30-80%:1-3%:0.1-0.3%-1-7%.    USE - As garden greening compound fertilizer.    ADVANTAGE - The compound fertilizer is rich in nutrition, environmentally-friendly, and free of chemical additive, can be prepared simply and conveniently, inhibits plant disease and insect pest, improves soil environment and pH, product quality, and landscape plant root, promotes growth of plants, and does not cause harm to health of human body.
NOVELTY - The roller has main reaction tank (1) whose outer side wall is set with water inlet valve and return valve (14). An inner portion of reaction tank is set with three temperature sensors (19). A portion of gas distribution chamber is set with rotating shaft (9). An air supply device is set with air compressor (3) connected with gas distribution cavity (2) via connecting pipeline. A drive device of reaction tank is set with gas distribution chamber. A cross section of stirring tooth is L shape, and upper surface of stirring tooth (18) is set with several vent holes.    USE - Hydro-thermal roller for high temperature compost reactor.    ADVANTAGE - Since the controllability of the hydro-thermal roller is high, and the oxygen supply to the high temperature compost reactor is controlled easily, the efficiency of the sludge compost is improved, and the pollution risk is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the of the hydro-thermal roller.    Main reaction tank (1)    Gas distribution cavity (2)    Air compressor (3)    Rotating shaft (9)    Return valve (14)    Stirring tooth (18)    Temperature sensor (19)
NOVELTY - Method for preparing fertilizer, involves taking animal excrement, removing impurity, adding deodorant and effective microbial liquid, mixing, placing in container and sealing to ferment at 25-35 degrees C for 7-14 days, adding pine needle powder, saw milling ash and grass powder, mixing uniformly, drying and crushing the fern root, dry tea, soybean cake and rape seed cake, adding and fermenting at high temperature, sterilizing, mixing and drying to obtain product.    USE - The method is useful for preparing fertilizer which is used for cultivating blueberry (claimed).    ADVANTAGE - The method optimizes the fertilizer formulation, and prepares fertilizer which can control the acidity of soil for cultivating blueberry and improve yield of blueberry.    DETAILED DESCRIPTION - Method for preparing fertilizer, involves weighing 3-5 pts. wt. animal excrement, 1-2 pts. wt. pine needle powder, 1-2 pts. wt. saw milling ash, 2-3 pts. wt. grass powder, 2-3 pts. wt. fern root, 1-2 pts. wt. dry tea, 1-2 pts. wt. soybean cake, and 1-2 pts. wt. rape seed cake, taking animal excrement, removing impurity, adding deodorant and effective microbial liquid, mixing and stirring uniformly, placing in container and sealing to ferment at 25-35 degrees C for 7-14 days, adding pine needle powder, saw milling ash and grass powder, mixing uniformly, drying and crushing the remaining raw materials, adding and fermenting at high temperature, sterilizing, mixing and drying to obtain product.
NOVELTY - Method for preparing blueberry special base fertilizer involves removing impurities of animal excrement and mixing with deodorant and effective microorganism bacterial liquid, fermenting the mixture at 25-35 degrees C for 7-14 days in sealed space, mixing the fermented mixture with pine needle powder, saw milled ash, carbon powder, fern root, and edible fungi waste package, and crushing and drying the obtained product.    USE - As blueberry special base fertilizer.    ADVANTAGE - The blueberry special base fertilizer enables to control acidity of soil and improve yield of blueberry during blueberry cultivation.    DETAILED DESCRIPTION - Method for preparing blueberry special base fertilizer involves using 3-5 pts. wt. animal excrement, 1-2 pts. wt. pine needle powder, 1-2 pts. wt. saw milled ash, 2-3 pts. wt. carbon powder, 1-2 pts. wt. fern root, and 4-6 pts. wt. edible fungus waste package, removing impurities of animal excrement and mixing with deodorant and effective microorganism bacterial liquid, fermenting the mixture at 25-35 degrees C for 7-14 days in sealed space, mixing the fermented mixture with pine needle powder, saw milled ash, carbon powder, fern root, and edible fungi waste package, and crushing and drying the obtained product.
NOVELTY - This utility new type provide a one electrochemical plating catalytic magnesium-hydrogen production system, comprising a function cabin, a controller, a hydrogen pressure sensor, a condenser, a hydrogen fuel battery and accessory, wherein only one set of a reaction chamber, storage water tank, a tail storage function of function bin chamber is integral recovery changeable function, a function cabin pre-separated from each other of magnesium powder, water and additive, the chamber wall through the connecting function of chamber sunk bottom of magnesium powder, through the control circuit connecting the anode catalytic electrode, function chamber with the external circuit using contact type connecting, a function cabin is set with function chamber hydrogen outlet, and a function chamber hydrogen outlet using fast inserting connecting, said controller circuit connecting hydrogen pressure sensor, hydrogen fuel battery and catalyzing electrode, said function chamber hydrogen outlet through the hydrogen pipeline connecting the condenser and hydrogen pressure sensor, a hydrogen pressure sensor set with hydrogen outlet and the hydrogen pipeline connecting hydrogen fuel battery. Chamber of the system function is set as the whole recycling replaceable module, high efficiency and environment-friendly.
NOVELTY - This utility new type claims a one anaerobic sludge bed reactor, comprising a top part of one three-phase separator in the tank-type reactor, the three-phase separator comprises a gas-liquid separating sloping plate module and solid-liquid separating sloping plate module, the top part of module the solid-liquid separating sloping plate set with the weir, two groups of oblique-plate separating module in the middle set with one chunk separating baffle, waste water feeding pump in the reactor with a tube, and then entering into reactor through water distributor, water upwards flow rear through the sludge bed layer with the biological anaerobic bacteria produce large amount of marsh gas, mixed solution time rises to the gas-liquid interface with a marsh gas from the mixed solution of a large amount in separation, dropping mixed solution of most marsh gas from the gas-liquid separating sloping plate module top entering into gas-liquid separating sloping plate module of solid and liquid and gas-liquid separating part, marsh gas upwards flow collecting to reactor top, and finally sent to the marsh gas processing unit treatment through biogas; futher separating the mixed liquid of gas and then entering into solid-liquid separating sloping plate module to realize solid-liquid separation. This utility new type three-phase separator in simple process, small module, low price with the current compared with the reactor is of advantage.
NOVELTY - This utility new type relates to positive and reverse spiral stirring mechanism, comprising a motor, a gear box, two spiral shaft, two spiral blade, wherein the motor is connected with the gear box, the gear box of two inner output gear is one of a spiral shaft, and the spiral direction of two opposite screw, each screw shaft are installed one spiral blade. The according to turning operation of the utility model is new type trolley is installed on the lengthways movement of upper upender composed by motor through the gear box rear power transmitting two opposite the rotation of the spiral shaft by operation of the spiral blade, the bottom of the raw material continuously upwards. This utility model is new type of bridge track self-walking type organic waste aerobic fermentation upender, year treatment abiligy (organic fertilizer production exceeds 1 million tons.
NOVELTY - This utility new type belongs to the biological diesel oil production using device technology field, especially relates to a one for methanol recovery of biodiesel production process in the device, comprising a first-stage condenser, cooling buffer tank and the outlet of the condenser connected of one level, the top part set with steam outlet, the bottom is set with leakage fluid dram; second level condenser, the top part set with connected with the steam outlet of the secondary condenser outlet, the bottom is set with second level condenser, time used, first-stage condenser for methanol steam primary condensation process, most condensing out and collected in the tank in rear entering into the buffer tank, cooling is not condensation of methanol steam entering into the second level condenser to condense to water content is very low of liquid methanol, second level condenser outlet returns to the production section of bio-diesel, which solves the production or in other biological diesel oil methyl esterification of chemical production process to produce methanol steam of not directly recycled of the problem, and it can effectively reduce the energy consumption and production cost.
NOVELTY - This utility new type claims a garbage processing field, especially relates to household gas device, comprising: a remote anti-explosion main control, garbage sorting, methane, marsh gas, marsh gas separating island, natural island, CO2, carbon , a garbage sorting island and methane island, island connect marsh gas, marsh gas and marsh gas separating island connect island, methane, methane separated islands and natural island connecting, methane, methane separated island and CO2 island connecting; CO2 island and carbon connecting of carbon black, island and methane island connecting. This utility new type of beneficial effects of this utility new type is suitable for large-scale processing domestic garbage, it can finish the daily processing amount 3000-30000 ton domestic garbage of target, can reduce the device occupied area at the same time of connecting device to form a circulation system, safety, air pressure, temperature and so on capable of remote monitoring and operation device of index, which greatly improves the safety.
NOVELTY - This utility new type claims a one supercritical biodiesel processing device, comprising the ester exchange reaction device, biological diesel oil distilling device, auxiliary rectifying device, further comprising extraction, supercritical reaction pipeline group, high temperature, low temperature heat-conducting oil tank pump, a heat exchanger, a hot upper extractor set with liquid outlet and a light liquid outlet, a liquid outlet through a conveying pipeline and the biodiesel distillation device connect, a light liquid outlet through a conveying pipeline and super-critical reaction pipeline group connect, up a supercritical reaction pipeline group is further set with waste heat pipeline, hot tube. Processing device with the existing phase compare, this utility new type substituted acid alkali catalytic device of front-acid catalysis of esterification device, which avoids the defect of difficult esterification section of acid catalysis, super-critical device processing the small amount of defect, at the same time, the device for pipeline of supercritical reaction, the reaction of high temperature high pressure, but also meets the of heat exchange under the condition, the large amount of hot grading can be fully recycled.
NOVELTY - This utility new type claims a one in the hot garage solid anaerobic fermentation device. The technical solution comprises a garage type fermentation device main body (1), door (2), a spraying pipe (3), collecting tube (11), storing and hardening and tempering device (12), a heat exchanger (15), an aeration tube (18), the aeration tube (18) and exhaust tube (5) stage of aerobic fermentation, which greatly reduces the fermentation process can be hot, using percolate collecting tube (11) and the percolate storage and tempering device (12) the rear and of the percolate collecting backflow solid material to the process, the mass transfer hot, solving the problem that the traditional valid high solid content material anaerobic fermentation process acid-suppressible, the whole system has no biogas liquid discharge by the heating coil pipe (14) and heat exchanger (15) to provide in fermentation anaphase of the heat, anaerobic fermentation system to ensure continuous and stable operation, and it has wide application prospect.
NOVELTY - Soil conditioner comprises: 0.5-0.9 wt.% of silicon containing more than 25% of petrochemical powder, 5.6-9.6 wt.% of amino acid powder, 11.8-13.6 wt.% of dihydrogen phosphate, 22.8-31.7 wt.% of potassium salt, 15.4-22.3 wt.% of ammonium sulfate, 12.8-16.6 wt.% of peat, 4.8-7.5 wt.% of calcium carbonate powder, and 8.7-15.4 wt.% of serpentine powder.    USE - The rhizome high-fat green microbial soil conditioner is useful in paddy fields (claimed).    ADVANTAGE - The conditioner improves pH value of the soil to above 4.5 for 100 kg per acre, and improves the quality of agricultural products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing soil conditioner comprising: mixing 0.5-0.9% of silicon powder with 5.6-9.6% of amino acid powder; fermenting for three days; mixing the fermented product with 11.8-13.6% of phosphoric acid; mixing 22.8-31.7 wt.% of potassium salt; again fermenting at 10 degrees C for 15 days; adding 12.8-16.6% of peat after fermentation; adding 4.8-7.5 wt.% of calcium carbonate powder, and 8.7-15.4 wt.% of serpentine powder; mixing and stirring.
NOVELTY - This new type utility claims one a hydrogen and oxygen generator for electrolysis of groove of seal device, comprising a seal ring, further comprising a fixing ring of said seal ring is embedded in the said of fixed ring. This utility new type has the advantages of the seal ring periphery and fixed ring, fixed ring using hard material, the effect is the shape of fixed seal ring to reach the effect of the seal ring is not caused by the short service life, so as to prolong the service life of high temperature resistant seal ring, saves the maintenance and change cost of hydrogen and oxygen generator, so that the operation is more stable and reliable due to thermal deformation.
NOVELTY - This utility new type claims a one for hydrogen and oxygen generator of radiating device, comprising an electrolytic groove, further comprising a first cooling unit and second cooling unit, cooling unit a first and second cooling unit of a set on the two end of said electrolytic groove of. This utility new type has the advantages of: using the multi-cooling system are mounted on the two sides of the fan electrolytic groove process of cooling, the wind direction, the electrolytic groove and faster and the other electrolytic groove out of gas and liquid through the circulation water cooling system of the back gas-liquid separation process of when close to the gas-liquid separating device of fan can be gas-liquid separating device to process cooling, increases effect of gas-liquid separation, the liquid phase gas-liquid separating device out of the cooling effect is better, and the electrolytic groove of, the temperature, so as to enhance the cooling effect of the electrolytic groove.
NOVELTY - The method involves filling copper catalyst in carbon monoxide isothermal conversion furnace (1). The water bath for shell side boiler feed water of constant temperature is located at the top of the carbon monoxide conversion furnace steam drum (2). The methane gas from the carbon monoxide isothermal conversion furnace is passed under the action of catalyst for generating carbon monoxide conversion reaction. The conversion reaction hot tube is connected to the shell side through the tube wall. A heating boiler water supply is provided for supplying side product low pressure steam.    USE - Carbon monoxide isothermal conversion method used in chemical industry for coal production.    ADVANTAGE - The temperature of the carbon monoxide conversion furnace in the carbon monoxide conversion process can be maintained constant, so as to ensure the normal conversion process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the carbon monoxide isothermal conversion furnace. (Drawing includes non-English language text)    Carbon monoxide isothermal conversion furnace (1)    Carbon monoxide conversion furnace steam drum (2)
NOVELTY - Carbon biomass is prepared by heating plant branch in steam cracking furnace under nitrogen atmosphere, cooling, pulverizing and sieving through 80-100 mesh sieve to obtain biomass carbon.    USE - Carbon biomass used for preparing composting material.
NOVELTY - The resource utilization device comprises a biogas unit comprising digesters, a cover located on the digester and a transparent plastic film, a gas storage unit, a septic unit comprising septic tanks and a liquid discharge, and a separation tank. The separation tank is provided with an outlet. The gas storage unit includes an exhaust port with a valve. A first septic tank and a third digester are positioned adjacent to each other. The second septic tank is provided with a sewage pump and a hole provided on its upper wall.    USE - The resource utilization device is useful for treating livestock manure (claimed) that is useful for producing biogas.    ADVANTAGE - The resource utilization device has simple structure, and is easy and economical to use in the rural areas.    DETAILED DESCRIPTION - The resource utilization device comprises a biogas unit comprising digesters, a cover located on the digester and a transparent plastic film, a gas storage unit, a septic unit comprising septic tanks and a liquid discharge, and a separation tank. The separation tank is provided with an outlet. The gas storage unit includes an exhaust port with a valve. A first septic tank and a third digester are positioned adjacent to each other. The second septic tank is provided with a sewage pump and a hole provided on its upper wall. The plastic thin film is inclined at an angle of 30-45 degrees with respect to a vertical plane and a horizontal plane. The cover is made of soft material.
NOVELTY - Preparation of bioorganic fertilizer comprises adding 0.08-0.12 pt. wt. microorganism fermenting agent to waste material, performing primary and secondary fermentation to 100 pts. wt. organic material, adding 3-4 earthworms to cultivation mixture, drying and maintaining 15-20% humidity to obtain bioorganic fertilizer.    USE - Method for preparing bioorganic fertilizer used for treating garbage, sludge or waste material (claimed).    ADVANTAGE - The bioorganic fertilizer is efficient and environmental-friendly.
NOVELTY - Eco-friendly organic fertilizer comprises 7-11 wt.% potassium ore, 9-18 wt.% ground phosphate rock, 10-16 wt.% calcium chloride, 12-15 wt.% potassium and magnesium sulfate, 11-17 wt.% plant residue, 15-19 wt.% animal waste and 11-15 wt.% black soybean.    USE - Eco-friendly organic fertilizer.
NOVELTY - Preparation of organic potash fertilizer comprises crushing corn stalk, wheat straw, rice straw, soybean pole, bean pole, pea pole and weeds, adding human and animal urine, mixing, pressing, sealing, fermenting for 15 days and storing.    USE - Method for preparing organic potash fertilizer (claimed) used for fruit crops, particularly grapefruit, persimmon, orange, peach, pumpkin and watermelon.    ADVANTAGE - The simple and convenient method reduces pollution and production costs, and improves quality and yield of products.
NOVELTY - Preparation of organic waste fertilizer comprises sterilizing animal waste with ozone, adding 6-15 kg nitrogen-fixing bacteria to 1000 kg sterilized waste, stirring at 1-40 degrees C and relative humidity of 40-95%, fermenting for 10-45 days, and packaging.    USE - Method for preparing organic waste fertilizer (claimed).    ADVANTAGE - The method is eco-friendly.
NOVELTY - Aerobic fermentation aeration device comprises box body bottom plate (1) with aeration holes and aeration cap (2).    USE - Aerobic fermentation aeration device used for fermenting organic waste.    ADVANTAGE - The simple and convenient device ensures long service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of aerobic fermentation aeration device.    Bottom plate (1)    Aeration cap (2)
NOVELTY - Vegetable fertilizer comprises 10-30 pts. wt. corn cob, 5-20 pts. wt. straw, 5-10 pts. wt. wood chips, 5-15 pts. wt. peanut, 10-15 pts. wt. peanut stem leaf, 5-15 pts. wt. slag, 2-3 pts. wt. diammonium phosphate and 5-50 pts. wt. earthworm waste.    USE - Vegetable fertilizer used for suppressing plant diseases and pathogen growth.    ADVANTAGE - The fertilizer is eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of vegetable fertilizer comprising crushing corn cob, straw, wood chips, peanut, peanut stem leaf, slag, diammonium phosphate, sieving, piling for not less than 40 days, and adding earthworm waste and chicken waste.
NOVELTY - Preparation of nitrogen-potassium organic fertilizer comprises collecting corn stalk, wheat straw, rice straw, soybean pole, broad bean pole and/or pea pole, crushing, adding human or animal urine, mixing, placing in tank, sealing, fermenting for 15 days, adding urea fertilizer, mixing, sealing and fermenting for 7 days.    USE - Method for preparing nitrogen-potassium organic fertilizer (claimed).    ADVANTAGE - The method is simple and environment-friendly.
NOVELTY - Preparation of nitrogen-phosphorus-potassium organic fertilizer comprises collecting corn stalk, wheat straw, rice straw, soybean pole, broad bean pole and/or pea pole, crushing, adding human or animal urine, mixing, placing in tank, sealing, fermenting for 15 days, adding nitrogenous fertilizer and phosphate fertilizer, mixing, sealing and fermenting for 12 days.    USE - Method for preparing nitrogen-phosphorus-potassium organic fertilizer (claimed).    ADVANTAGE - The method is simple and environment-friendly.
NOVELTY - Comprehensive treatment of waste sulfuric acid sulfonation products comprises adding water and caustic calcined magnesia to waste sulfuric acid sulfonation products, heating to 80-90 degrees C, adding magnesite powder, reacting until pH value is 4-5, adding caustic calcined magnesia, reacting until pH value is 6.8-7, adding formaldehyde, stirring, adding urea and activated carbon, stirring, filtering, crystallizing filtrate, centrifuging, drying to form dried magnesium sulfate heptahydrate, and calcining at 600-1000 degrees C.    USE - Comprehensive treatment of waste sulfuric acid sulfonation products used for producing silicon, calcium and magnesium fertilizer (claimed), and solving pollution problems.    ADVANTAGE - The method is simple, inexpensive and suitable for industrial application.
NOVELTY - An enzyme-containing organic foliar fertilizer (Ca3(Po4)2-MgSiO3-CH3-CH3-COOCu-CH3COONa-K2PO4) is new.    USE - Enzyme-containing organic foliar fertilizer used for promoting full grain cereal crops and suppressing pests.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of enzyme-containing organic foliar fertilizer.
NOVELTY - Preparation of organic phosphorus and potassium fertilizer comprises crushing harvested crops comprising corn stalks, wheat straw, rice straw, soybean rod, pole beans, pole peas and weeds, placing into pressure tank, sealing, fermenting for 16 days to obtain natural organic potash fertilizer, mixing organic potash and phosphate at mass ratio of 7:3, placing into fermentation vessel, sealing, and fermenting mixed fertilizer for 18 days to penetrate in organic potash.    USE - Method for preparing organic phosphorus and potassium fertilizer used for cultivating flowers and fruits on yellow soil comprising bananas, persimmons, citrus, peanuts, watermelons and melons (claimed).    ADVANTAGE - The simple and convenient method reduces environmental pollution, reduces cost, and improves quality and yield of agricultural products.
NOVELTY - A sheep manure fertilizer comprises 50-55 pts. wt. fresh sheep manure, 10-15 pts. wt. soy flour, 10-15 pts. wt. corn starch, 5-10 pts. wt. wheat bran, 3-5 pts. wt. brown sugar, 1-1.5 pts. wt. seaweed, 1-2 pts. wt. effective microorganism agent, 9-12 pts. wt. soil improver and water.    USE - Sheep manure fertilizer used for improving physical and chemical property of soil, and promoting water and nutrient absorption.    ADVANTAGE - The method is simple and inexpensive. The fertilizer increases crop yield and disease resistance.    DETAILED DESCRIPTION - A sheep manure fertilizer comprises 50-55 pts. wt. fresh sheep manure, 10-15 pts. wt. soy flour, 10-15 pts. wt. corn starch, 5-10 pts. wt. wheat bran, 3-5 pts. wt. brown sugar, 1-1.5 pts. wt. seaweed, 1-2 pts. wt. effective microorganism agent, 9-12 pts. wt. soil improver and water. The soil improver comprises 100-120 pts. wt. diatomite, 1-2 pts. wt. nanocarbon powder, 4-5 pts. wt. soapstock, 4-5 pts. wt. metasilicate, 1-2 pts. wt. KH550 (RTM: silane coupling agent), 3-4 pts. wt. selenite, 2-3 pts. wt. chitosan, 1-2 pts. wt. Eucalyptus oil, 1-2 pts. wt. Texanol (RTM: 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate), 2-3 pts. wt. nanojade powder, 4-5 pts. wt. Alangium root, 3-4 pts. wt. garlic and water. The soil improver is prepared by crushing Alangium root and garlic, adding diatomite and water, heating to 80-90 degrees C, adding nanocarbon powder and nanojade powder, grinding for 30-45 minutes, adding sodium silicate and chitosan, stirring for 10-15 minutes to form paste, adding rest of materials, stirring, granulating and drying.
NOVELTY - A gardening substrate is prepared by crushing straw, immersing slurry in slurry bed material, aerating for 10-20 minutes, adding hygroscopic material to absorb moisture from air, filtering slurry, adding 5-10 wt.% material acidifiers and 0.5-1.5 wt.% composting agent, mixing, aerating for 0.5-1 hour, aerobically fermenting, controlling temperature at greater than or equal to 50 degrees C for 7-10 days, anaerobically fermenting for 5-7 days, sieving, and drying.    USE - Method for preparing gardening substrate (claimed).
NOVELTY - A Calendula officinalis fertilizer comprises 5-10 wt.% potassium chloride, 25-40 wt.% calcium bicarbonate, 5-8 wt.% ash, 23-45 wt.% bentonite, 14-23 wt.% pulverized coal ash, 12-15 wt.% calcium superphosphate and 0.01-0.03 wt.% brown Azotobacter powder.    USE - Calendula officinalis fertilizer.
NOVELTY - A grape foliar fertilizer is prepared by mixing soybeans and malt, crushing to obtain fermentation substrate, mixing sodium bisulfite, manganese sulfate, zinc sulfate, sugar and urea, adding to fermentation substrate, stirring, adding water, fermenting, adding manure, mixing, extracting to obtain liquid fertilizer, compacting solid phase, crushing, adding leaching solution, mixing, adding abscisic acid, 5-aminolevulinic acid, and potassium dihydrogen phosphate, calcium nitrate or sodium borate, mixing, and neutralizing.    USE - Method for preparing grape foliar fertilizer (claimed).    DETAILED DESCRIPTION - A grape foliar fertilizer is prepared by mixing 100 kg soybeans and 10 kg malt, crushing to obtain fermentation substrate, mixing 10-15 kg sodium bisulfite, 3-5 kg manganese sulfate, 3-5 kg zinc sulfate, 15-25 kg sugar and 3-5 kg urea, adding to fermentation substrate, stirring, adding 200 g water, fermenting at 25-35 degrees C for 10-30 days, adding manure, mixing, extracting at 35-55 degrees C to obtain liquid fertilizer, compacting solid phase, crushing, adding leaching solution, mixing, adding 0.02 kg abscisic acid, 0.025 kg 5-aminolevulinic acid, and 2-3 kg potassium dihydrogen phosphate, 1.5-3 kg calcium nitrate or 1-1.5 kg sodium borate per 100 kg liquid fertilizer, mixing, and neutralizing.
NOVELTY - A fertilizer composition is prepared by mixing chicken manure powder, crushed rice straw and bentonite material, crushing, adding binder, mixing, adding with water, extruding, granulating, cooling, drying to kill undesirable bacteria, cooling to obtain carrier, activating Bacillus megatherium, Bacillus mucilaginosus and Streptomyces rimosus, granulating, adding water, mixing carrier and activated bacteria, fermenting, adding carrier, and mixing.    USE - Method for preparing fertilizer composition used for preventing Verticillium wilt (claimed).    DETAILED DESCRIPTION - A fertilizer composition is prepared by mixing 20-50 wt.% chicken manure powder, 15 wt.% crushed rice straw and 15 wt.% bentonite material, crushing, adding binder, mixing, adding with water to moisture content is less than or equal to 25%, extruding, granulating, cooling, drying at 80 degrees C for 15 minutes to kill undesirable bacteria, cooling to obtain carrier, activating Bacillus megatherium, Bacillus mucilaginosus and Streptomyces rimosus, granulating, adding 1000 mL water, mixing carrier and activated bacteria at mass ratio of 1:2, fermenting at 18-25 degrees C for 3-5 days, adding carrier at mass ratio of 1:10, and mixing.
NOVELTY - Foliar fertilizer comprises furnace ash and minerals, and further comprises 20-25 pts. wt. methylenesuccinic acid, 1.5-3 pts. wt. yeast, 5-10 pts. wt. ferric sulfate, and 15-26 pts. wt. sweet potato powder.    USE - Foliar fertilizer.    ADVANTAGE - The foliar fertilizer has better crop growth promoting effect compared with existing product.
NOVELTY - Fertilizer composition comprises (in pts.wt.): sodium alginate liquid (10-20), fermented chicken manure (20-30) and inorganic fertilizer (15-30).    USE - Fertilizer composition.    ADVANTAGE - The fertilizer composition promotes yield of plants, and safety of crops, and improves soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer composition, which involves:    (A) drying (in pts.wt.): seaweed (30-50), sea mud (5-15) and soybean meal (10-15) to obtain dried raw materials having water content less than or equal to 12%;    (B) crushing the dried raw materials to obtain powder, which is sieved through 60 mesh sized sieve to obtain fine powder;    (C) mixing the obtained powder with fresh water (100 parts), corn flour (30 parts), Saccharomyces cerevisiae, Bacillus subtilis, lactic acid bacteria, Rhizobium, phosphorus bacteria and potassium bacteria (0.3 parts) under stirring condition to obtain uniform mixture;    (D) fermenting the uniform mixture for 2 hours to obtain a fermented mixture; and    (E) fermenting the obtained fermented mixture by adding 1-1.5% of primer and clean water (80 pts.wt.) at 35-45 degrees C for 12-24 hours, and stirring the fermentation liquid from bottom of the fermentation tank to obtain another fermentation liquid.
NOVELTY - Sludge plant growth medium comprises main material and auxiliary material. The main material comprises straw fiber and decomposed sludge compost. The auxiliary material comprises chemical fiber, water retention agent, adhesive, microbial fertilizer, soil modifier, trace element fertilizer, pesticide and insecticide. The straw fiber of the main material, decomposed sludge compost and auxiliary material are present in a ratio of 7-17:80-90:2-5.    USE - Sludge plant growth medium used for slope greening for ecological restoration, repairing soil of slope by preventing soil erosion and loss of nutrients from the soil, and increasing organic matter in soil.    ADVANTAGE - The sludge plant growth medium improves mechanical strength of the soil, and converts the waste product into vegetation and plantation, reduces soil erosion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for slope greening, which involves:    (A) mixing the sludge plant growth medium with garden soil in a ratio of 1-1:1-3 to obtain uniform soil mixture;    (B) filling the uniform soil mixture in ecological bag;    (C) placing the ecological bags containing uniform soil mixture on the slope; and    (D) growing plants on the slope.
NOVELTY - Fertilizer composition comprises (in pts.wt.): chicken manure (30-40), rice flour (15-19), tobacco stalk (13-18), shell powder (12-16), basalt powder (20-26), zinc sulfate (4-5), ferric sulfate (5-6), copper sulfate (3-5), manganese sulfate (2-3), effective microorganisms inoculants (1-2) and soil modifying agent (10-13).    USE - Fertilizer composition.    ADVANTAGE - The fertilizer composition is safe, cost-effective, eco-friendly and high nutritional value, and promotes plant growth.    DETAILED DESCRIPTION - Fertilizer composition comprises (in pts.wt.): chicken manure (30-40), rice flour (15-19), tobacco stalk (13-18), shell powder (12-16), basalt powder (20-26), zinc sulfate (4-5), ferric sulfate (5-6), copper sulfate (3-5), manganese sulfate (2-3), effective microorganisms inoculants (1-2) and soil modifying agent (10-13). The soil modifying agent comprises (in pts.wt.): diatomite (100-120), nanocarbon powder (1-2), residue (4-5), sodium metasilicate (4-5), ascorbic acid (1-2), silane coupling agent KH550 (1-2), sodium selenite (3-4), zinc sulfate (3-4), manganese sulfate (1-2), borax (2-3), ferrous sulfate (3-4), ammonium citrate (1-2), chitosan (2-3), wintergreen oil (1-2), tributyl citrate (1-2), nano jade powder (2-3) and radix sophorae flavescentis (4-5). Soil modifying agent is prepared by mixing and grinding diatomite, sodium selenite, zinc sulfate, manganese sulfate, borax, ferrous sulfate and ammonium sulfate to obtain 200-400 mesh powder. The obtained powder is mixed and ground nanocarbon powder and silane coupling agent KH550. The obtained powder is mixed with remaining components at 1200-1500 revolutions per minute for 30-45 minutes and then ground to obtain desired product.
NOVELTY - Phenol and p-aminobenzoic acid are acylated under reflux to produce paracetamol. Dilute acetic acid is introduced into reaction vessel containing butanol and esterified to produce butyl acetate.    USE - Manufacture of paracetamol and butyl acetate (claimed).    ADVANTAGE - Since the dilute acetic acid is recycled to the esterification reaction, the energy consumption for the reaction is reduced and discharge of waste is reduced. The entire reaction forms a closed loop effect.
NOVELTY - Chloroacetonitrile and hydrogen cyanide are reacted in the presence of a catalyst and a solvent at 15-25 degrees C for 8-15 hours to obtain malononitrile.    USE - Manufacture of malononitrile used as pesticide intermediate.    ADVANTAGE - The method produces malononitrile with high yield and high purity, economically, with low energy consumption and reduced environmental pollution.
NOVELTY - Preparation of 3-dimethylamino-1-(3-pyridyl)-2-propen-1-one comprises reacting N,N-dimethyl formamide and 3-acetylpyridine using zeolite socony mobil-5 (ZSM-5) as catalyst, hot filtering, recrystallizing by cooling, and filtering to obtain solid product.    USE - Method for preparing 3-dimethylamino-1-(3-pyridyl)-2-propen-1-one (claimed).    ADVANTAGE - The simple and inexpensive method has great economical efficiency and environmental benefits.
NOVELTY - Fermentation of tylosin comprises heating and stirring tylosin fermentation broth at 50-60 degrees C, adding industrial grade oxalic acid, sodium oxalate or glutamic acid, adjusting pH, stirring, filtering using stainless steel mesh, filtering via membrane filtration, cooling, diluting, reducing chemical potency to 20-30%, filtering via nano filtration, stirring and cooling to 5-10 degrees C, adjusting pH, precipitating, standing, performing solid-liquid separation, washing, adding acid solution, stirring, adjusting pH, filtering via ultrafiltration and spray drying.    USE - Method for fermenting tylosin used for producing sterile drug tylosin salt (claimed).    ADVANTAGE - The simple and easy method reduces production time, increases extraction efficiency, saves energy, reduces pollution and reduces cost.    DETAILED DESCRIPTION - Fermentation of tylosin comprises heating and stirring tylosin fermentation broth at 50-60 degrees C, adding 0.1-0.5% industrial grade oxalic acid, sodium oxalate or glutamic acid, adjusting pH to 3-5, stirring for 20-30 minutes, filtering using stainless steel mesh to obtain tylosin filtrate, filtering via tubular porous ceramic membrane filtration at 1-1.2 bar and 50-60 degrees C, cooling to 20-30 degrees C, diluting with purified water, reducing chemical potency to 20-30%, filtering via nano filtration, stirring and cooling to 5-10 degrees C, adjusting pH to 10-11 by adding weak acid or weak alkali comprising 10% sodium hydroxide or ammonia, precipitating crystals, standing for 1 hour, performing solid-liquid separation, washing solid with purified water, adding 10-30% acid solution, stirring, adjusting pH to 5-6, filtering via ultrafiltration and spray drying to obtain tylosin salt.
NOVELTY - The method involves pre-processing biomass. Liquid acid catalyst and solvent are mixed and put into an ultrasonic-microwave synergistic extractor. Ultrasonic microwave catalyzing and biomass liquefying process is performed to obtain a liquefied product. The liquefied product is separated from the biomass. The liquefied product is dried at temperature of 105 degrees Celsius. Weight of the biomass is calculated. Solid suspended substance filter operation process is performed. Oil phase or solid residue is collected to obtain biomass liquefied oil.    USE - Ultrasonic-microwave biomass liquefaction method.    ADVANTAGE - The method enables realizing enforcing hot transfer process and mass transfer process, improving biomass liquefied liquid-solid ratio and working efficiency, reducing energy consumption and reaction time consumption and transforming biomass to chemical energy.    DETAILED DESCRIPTION - The biomass is formed of fir, pine, poplar, corn core raw material. The liquid acid catalyst is sulfuric acid, hydrochloric acid and phosphoric acid. The solvent is ethanol, polyethylene glycol, glycerine and octanol.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating an ultrasonic-microwave biomass liquefaction method. '(Drawing includes non-English language text)'
NOVELTY - An ether ester methanol fuel contains 60-90 wt.% methanol, 0-30 wt.% ethanol, and 10 wt.% mixed additive in which mixed additive contains 20 wt.% mercaptobenzothiazole, 20 wt.% 2,6-di-tert.-butyl-4-methylphenol (T501), 20 wt.% liquid benzotriazole derivative (T551), 20 wt.% diethyl ether, and 20 wt.% ethylhexyl nitrate.    USE - Ether ester methanol fuel for vehicle.    ADVANTAGE - Ether ester methanol fuel is cheap and has convenient production process.
NOVELTY - An ether gasoline is prepared by mixing dimethyl ether, ethanol, biological straw, distilled water, catalyst, and additive.    USE - Preparation of ether gasoline for biomass residue production (claimed).    ADVANTAGE - Preparation process is simple and has low cost. Product has high olefin content and high octane value.
NOVELTY - A biocomposite diesel contains 30-50 pts. wt. soybean oil, 5-10 pts. wt. ethylene glycol, 5-10 pts. wt. sodium hydroxide, 5-10 pts. wt. hydrochloric acid solution, and 20-35 pts. wt. water.    USE - A biocomposite diesel (claimed).    ADVANTAGE - Biocomposite diesel is energy-saving and environment-friendly and has low cost, good performance, and good stability. Preparation process is simple and easy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biocomposite diesel which involves performing decolorization of soybean oil, removing impurities, purifying soybean oil, mixing ethanol:sodium hydroxide with weight ratio of 2:1, heating at 80 degrees C for 3 hours under reflux to obtain sodium alkoxide solution, heating purified soybean oil at constant temperature of 70-90 degrees C, adding sodium alkoxide solution, stirring at 80 rpm for 1-3 hours, adding 5-10 pts. wt. hydrochloric acid solution, standing, layering at 90 degrees C for 18-24 hours to obtain solution, distilling upper layer of solution under reduced pressure of 1.5 kPa to recover ethylene glycol, removing filter by suction, repeatedly washing with water for 4-7 times, and drying for 15-20 hours to obtain clear and transparent pale yellow product.
NOVELTY - An alcohol gasoline additive contains 50-80 pts. wt. methanol, 15-30 pts. wt. ethanol, 5-10 pts. wt. isopropanol, 4-10 pts. wt. methyl tert.-butyl ether, 1-3 pts. wt. diethyl ether, 3-5 pts. wt. polyisobutylene imide, 1-2 pts. wt. methylcyclopentadienyl manganese tricarbonyl, 2-5 pts. wt. acetone, 2-4 pts. wt. methyl isobutyrate, and 2-4 pts. wt. maleic anhydride.    USE - An alcohol gasoline additive (claimed).    ADVANTAGE - Alcohol gasoline additive has corrosion resistance and is simple to use. Preparation process is simple and has low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of alcohol gasoline additive which involves adding methanol, ethanol, and isopropanol in mixing tank, stirring at room temperature to disperse and obtain mixture, adding with methyl tert.-butyl ether, diethyl ether, polyisobutylene imide, methylcyclopentadienyl manganese tricarbonyl, acetone, methyl isobutyrate, and maleic anhydride, stirring at room temperature and pressure for 20-30 minutes to obtain mixed solution, and standing mixed solution for 2 hours.
NOVELTY - An environment-friendly methanol gasoline is prepared by preparing nano-fuel additive, preparing cosolvent, and preparing denatured alcohol.    USE - Preparation of environment-friendly methanol gasoline (claimed).    ADVANTAGE - Preparation process increases thermal gasoline efficiency and reduces fuel waste and emissions.
NOVELTY - A methanol diesel contains 40-70 pts. wt. diesel, 10-30 pts. wt. methanol, and 10-30 pts. wt. additive.    USE - A methanol diesel (claimed).    ADVANTAGE - Methanol diesel is environment-friendly. Preparation process is simple and has low cost and mild reaction conditions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of methanol diesel which involves mixing methanol and cyclopentyl ferrocene, denaturing, fully dissolve to obtain denatured methanol, mixing denatured methanol with vegetable oil acid to obtain mixture 1, mixing diesel, isooctyl nitrate, and zinc peroxide to obtain mixture 2, mixing mixture 1, mixture 2, and aviation kerosene, adding cosolvent, and stirring.
NOVELTY - A composite additive is prepared by adding dodecyl methacrylate, stearyl acrylate, isooctyl nitrate, and diethyl phthalate in mixing tank, stirring, adding maleic anhydride and isooctanol, stirring, adding tert.-butylamine and dicetyl(dimethyl)ammonium chloride, stirring for 30-35 minutes to obtain solution, adding polyoxyethylene cetyl alkylphenol ether and phenyl propargyl ether, heating at 45-50 degrees C, stirring at 0.5-1 MPa for 20-30 minutes, standing for 24 hours, filtering, and removing precipitate.    USE - Preparation of composite additive for biodiesel (claimed).    ADVANTAGE - Composite additive has good cold filler plugging point effect and stable dispersion ability and is oil-soluble.
NOVELTY - An emulsified biodiesel contains 40-50 mass% biodiesel, 2-3 mass% emulsifier, 45-50 mass% weighting agent, and 3-7 mass% water.    USE - Emulsified biodiesel (claimed).    ADVANTAGE - Emulsified biodiesel has uniform dispersion and good stability, does not contain any nitrogen-containing compound, reduces emission of nitrogen oxide and smoke, and is clear, transparent, non-toxic, and conducive to store and transport. Preparation process is simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of emulsified biodiesel which involves mixing biodiesel, emulsifier, weighting agent, and water at 35-50 degrees C for 0.5-1.5 hours with speed of 2000 rpm to form transparent emulsion.
NOVELTY - A clean biodiesel oil contains 20-30 pts. wt. bio-oil, 5-20 pts. wt. short-chain alcohol, 30-40 pts. wt. diesel oil, 5-8 pts. wt. additive, and 2-40 pts. wt. water.    USE - A clean biodiesel oil (claimed).    ADVANTAGE - Preparation process is simple and low cost, and product is environment-friendly, clean, easy to transport and store, and safe and has better index, excellent overall performance, and high combustion efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of clean biodiesel oil which involves adding bio-oil, short-chain alcohol, diesel oil, additive, and water in reaction vessel, stirring for 20-30 minutes, fully mixing, and filtering.
NOVELTY - A microalgae biodiesel is prepared by inoculating microalgae which is cultured to logarithmic growing period in fresh culture medium with 0.2-0.4 inoculum density at 20-30 degrees C, collecting microalgae cell, centrifuging and concentrating, freeze-drying, grinding, adding obtained algae powder in chloroform-methanol-water mixed solution, performing chloroform extraction, mixing, collecting supernatant, adding chloroform, collecting lower chloroform layer, removing chloroform, adding methanol and lipase to obtained microalgae grease, and performing enzyme catalytic reaction.    USE - Preparation of microalgae biodiesel (claimed).    ADVANTAGE - The preparation improves biodiesel yield and biodiesel trans-esterification efficiency, has mild reaction condition and simple alcohol and glycerol byproduct separation, reduces process and cost, and meets diesel fuel standard.    DETAILED DESCRIPTION - A microalgae biodiesel is prepared by inoculating microalgae which is cultured to logarithmic growing period in fresh culture medium with 0.2-0.4 inoculum density at 20-30 degrees C under 3000-40001x illumination condition, collecting microalgae cell, centrifuging and concentrating, freeze-drying, fully grinding to obtain algae powder, adding obtained algae powder in chloroform-methanol-water mixed solution, performing chloroform extraction in which volume ratio chloroform:methanol:water is 1:2:0.8-3 and mass-to-volume (g:ml) algae powder:chloroform-methanol-water is 1:100, uniformly mixing for 3-5 hours, collecting supernatant, adding chloroform to obtain chloroform-methanol-water ratio at 1:1:0.9, collecting lower chloroform layer, removing chloroform at 60 degrees C to obtain microalgae grease, adding methanol and lipase to obtained microalgae grease in which lipase is 20-30 wt.% of microalgae grease weight, and performing enzyme catalytic reaction at 30-40 degrees C for 48-60 hours.
NOVELTY - Achromobacter marplatensis (TNSC2011) comprising preservation number CGMCC NO. 8192, is new.    USE - Achromobacter marplatensis is useful in sugar beet cultivation (claimed), and promoting the growth of crops and photosynthesis.    ADVANTAGE - Achromobacter marplatensis: ensures insoluble phosphate conversion to increase its bioavailability; is suitable for deep research of stability to promote the growth of crops; and is a good endophyte.
NOVELTY - Burkholderia comprising a preservation number CGMCC NO.7980, is new.    USE - Burkholderia useful in preparing microbial fertilizer for preventing and controlling Fusarium oxysporum and promoting the growth of Vanilla (claimed).    ADVANTAGE - Burkholderia can be stably colonized in humus soil; The microbial fertilizer improves soil microorganism environment; and eliminates continuous biological barriers.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) a microbial fertilizer, comprising Burkholderia obtained by solid-state fermentation of livestock and poultry manure; (2) preparation of the microbial fertilizer, comprising (a) inoculating Burkholderia into nutrient agar (NA) liquid culture medium of pH 6-8, culturing in a shaker incubator, centrifuging the bacterial suspension, re-suspending the pellet with sterile water, centrifuging, adding equal volume of sterile water to obtain aqueous bacterial suspension, and (b) inoculating the bacterial suspension into livestock poultry manure, carrying out solid-state fermentation until Burkholderia reaches to more than 108 colony forming units (cfu)/g, and maintaining the solid fermentation temperature to be not greater than 50 degrees C to obtain microbial fertilizer.
NOVELTY - This utility new type claims a one cooling machine, comprising a tube, one said end of tube connecting with a feeding box, and the other end connecting with a discharging box, middle part of said tube connecting with a transmission device by a bolt, a feeding box with the transmission device through the tube is equipped with a front roller, a discharging box and the transmission device through tube is equipped with rear wheel. This utility new type one a cooling machine of a, it has simple structure, convenient operation, continuous operation time of stable and reliable, the transmission device and the driving component, the energy-saving effect is obvious, the daily maintenance is convenient.
NOVELTY - The device has a natural gas producing device body provided with a heavy hydrocarbon separation tank and a condenser. A de-nitrification rectification tower is connected with an upper part of a rectifying section. The rectifying section is connected with a tower plate. A heat exchanger is formed with a heat exchanger hot section. A compressor is connected with a feeding tube. The rectification tower is connected with a discharging tube. The heavy hydrocarbon separation tank is connected with the feeding tube that is connected with a nitrogen rectification tower section.    USE - Liquefied natural gas and high purity nitrogen producing device.    ADVANTAGE - The device has high operating efficiency and better economic benefits, and realizes liquefied natural gas and high-purity nitrogen mass production operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a liquefied natural gas and high purity nitrogen producing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a liquefied natural gas and high purity nitrogen producing device.'(Drawing includes non-English language text)'
NOVELTY - Slow-release compound microbial fertilizer comprises 100-150 pts. wt. fertilizer core and 2-3 pts. wt. coating materials, where the fertilizer core comprises 15-25 pts. wt. polyacrylamide, 5-10 pts. wt. epsilon -polylysine, 3-5 pts. wt.ascorbic acid, 3-5 pts. wt. EDTA and 50-150 microbial composite inoculum and remainder organic fillers, and coating materials comprises 2-5 pts. wt. gelatin, 1-5 pts. wt. polyvinyl alcohol, 20-40 pts. wt. urea, 5-25 pts. wt. ferrous sulfate, 5-25 pts. wt. zinc sulfate, 2-5 pts. wt. ammonium citrate, 0.5-1 pts. wt. formaldehyde and 30-55 pts. wt. water.    USE - As slow-release compound microbial fertilizer (claimed).    ADVANTAGE - The slow-release compound microbial fertilizer is stable and environmentally-friendly and easily absorbed by crops.    DETAILED DESCRIPTION - Slow-release compound microbial fertilizer comprises 100-150 pts. wt. fertilizer core and 2-3 pts. wt. coating materials, where the fertilizer core comprises 15-25 pts. wt. polyacrylamide, 5-10 pts. wt. epsilon -polylysine, 3-5 pts. wt.ascorbic acid, 3-5 pts. wt. EDTA and 50-150 microbial composite inoculum and remainder organic fillers, and coating materials comprises 2-5 pts. wt. gelatin, 1-5 pts. wt. polyvinyl alcohol, 20-40 pts. wt. urea, 5-25 pts. wt. ferrous sulfate, 5-25 pts. wt. zinc sulfate, 2-5 pts. wt. ammonium citrate, 0.5-1 pts. wt. formaldehyde and 30-55 pts. wt. water. An INDEPENDENT CLAIM is included for slow-release compound microbial fertilizer, which involves preparing fertilizer core and coating materials and coating.
NOVELTY - Organic fertilizer comprises 72-85 %mass lees, 8.5-15 %mass rice bran, 6-10 %mass ash and 0.5-3 %mass microbial fermentation agent.    USE - As organic fertilizer.    ADVANTAGE - The fertilizer is cost-effective and stable in nature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, which involves (a) mixing the above-mentioned raw materials to obtain mixture, (b) stacking the mixture and fermenting for 2-3 days to obtain mixed mixture, (c) turning the mixture once the temperature reaches 55-60 degrees C at a interval of 8-12 hours and turning once, until the fermentation is complete, (d) mixing the mixture and granulating using granulator, (e) drying the granules at 180-200 degrees C, and (f) cooling the dried granules, screening and packing to obtain the product.
NOVELTY - Preparing vanillin, comprises (1) dissolving phenol oil containing 4-methyl guaiacol in sodium hydroxide solution, (2) freezing, crystallizing, centrifuging the reaction mixture to obtain 4-methyl guaiacol sodium chloride crystal, (3) reducing and drying the 4-methyl guaiacol sodium chloride crystal to obtain a 4-methyl guaiacol sodium, (4) dissolving 4-methyl guaiacol sodium with alcohol solvent, and adding catalyst, then oxidizing using oxygen containing gas to obtain oxidized material, and (5) adding carbon dioxide and water for distillation of alcohol solvent, and crystallizing.    USE - The method is useful for preparing vanillin (claimed).    ADVANTAGE - The method simply prepares the non-toxic vanillin in an environmentally friendly manner.
NOVELTY - A microbial agent contains 5-7 pts. wt. long bristles coir, 4-6 pts. wt. Trichoderma koningii, 3-5 pts. wt. circular leaven Chaetomium, 3-5 pts. wt. green Trichoderma viride, and 2-3 pts. wt. Geotrichum candidum.    USE - Microbial agent for preparing cattle manure organic fertilizer (claimed).    ADVANTAGE - The microbial agent shortens fermentation process and improves cellulose degradation efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) preparation of microbial agent which involves heating potato dextrose agar (PDA) culture medium and malt extract agar culture medium at 121 degrees C for 20 minutes, cooling to not greater than 30 degrees C, inoculating long bristle coir, T. koningii, circular leaven Chaetomium, and green T. viride strains in 4 PDA culture mediums, inoculating fungal strain in malt extract agar culture medium at 28 degrees C, shaking for 24 hours to obtain female ferment, preparing 10% skimmed milk by mixing skimmed milk, 2% glycerol, 1% xylose, and 1% glucose, sterilizing at 121 degrees C for 20 minutes, cooling to 30 degrees C, inoculating 2 vol.% female ferment at 28 degrees C , shaking for 48 hours to obtain production leaven, feeding in 5 glass ampoule bottles under sterile condition, sealing, performing freeze-drying treatment to obtain lyophilized strain powder, and storing in vacuum bag; and (3) use of microbial agent for preparing cattle manure organic fertilizer which involves mixing fresh cattle manure, straw, peat, beet pulp, soybean curb residue and zeolite powder to obtain organic material, adding 50 g organic material to every 1000 g water at temperature of 30-35 degrees C, adding 10-20 g brown sugar, standing at room temperature for 10-14 hours, uniformly spraying in organic material, fermenting at room temperature for 12 days, stirring once in every 3 days.
NOVELTY - Decomposing agent comprises (in colony-forming unit): xylan poly sugar Clostridium xylanolyticum (25-35), cellulose xylan Xylanimonas cellulosilytica (25-30), Pseudomonas (20-30) and bud holding Bacillus subtilis (15-20).    USE - Decomposing agent used for decomposing rice straw (claimed).    ADVANTAGE - The decomposing agent is prepared in simple, cost-effective and quick manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing microbial inoculum, which involves:    (A) culturing Clostridium xylanolyticum, Xylanimonas cellulosilytica, Pseudomonas and Bacillus subtilis to obtain product; and    (B) mixing adsorption carrier with product to obtain the microbial inoculum.
NOVELTY - An abamectin is prepared by dissolving abamectin powder in acetone, filling in octadecylsilane bonded silicon glue reverse phase chromatography packing column, performing gradient elution using polar solvent and water mixed solution as eluent, collecting, detecting liquid phase, combining, condensing, and drying in which obtained product contains avermectin B1 with 98.5-99.5% purity, and greater than or equal to 97% avermectin B1a with greater than or equal to 95% purity.    USE - Preparation of abamectin (claimed).    ADVANTAGE - The preparation is simple and environment-friendly, and has high yield, no high toxic solvent, such as chloroform and toluene, low cost, and pharmaceutically acceptable raw materials which provide safer level of technical support, and product is stable and has controllable mass.
NOVELTY - Device for a non-feed biogas system, which is provided with a fermenter and a stationary supply device, during shutdown of the fermenter due to a revision or a defect of the stationary supply device, is claimed. The device is designed as a roller container with a standard lower frame and a tank on the lower frame. The tank is provided with a tube connection, a bidirectionally operable pump, a stirrer, and a level sensor.    USE - The device is useful for a non-feed biogas system, which is provided with a fermenter and a stationary supply device, during shutdown of the fermenter due to a revision or a defect of the stationary supply device.
NOVELTY - Device (10) comprises: a film sealingly attached with a container (1); a receiving pocket into which the film is inserted and attachable to the container; and a clamping element, with which the film in the receiving pocket is clampingly fixed, preferably at least two clamping elements which are relatively movable and expandable for clamping the film set in the receiving pocket.    USE - The device is useful for gas-tight sealing of a container, preferably a biogas reactor (claimed).    ADVANTAGE - The device ensures continued safe closure of the container with simplified installation and/or maintenance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a container, preferably a biogas reactor, comprising a device for gas-tight sealing of the container, where the device is fixed to or near the top edge of an outer wall of the container.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic side view of the container.    Container (1)    Longitudinal axis (2)    Container wall (4)    Foundation plate (6)    Device (10)
NOVELTY - Method of producing a wood biomass fuel involves applying calcium carbonate to wood biomass to form a mixture; and forming wood biomass fuel from the mixture at 550-650 degrees F.    USE - For producing a wood biomass fuel used to form wood pellets as source of fuel in alternative fuel industry.    ADVANTAGE - The method produces clean burning wood biomass fuel and results in neutralization of organic acids found in the wood biomass. This enables a significant reduction in the volatile organic compound (VOC) or acid levels in the smoke when the wood biomass fuels are burned. Accordingly, upon combustion of the clean burning wood biomass fuel, environmentally friendly byproducts are produced and solid waste byproducts in the form of ash are reduced. The byproducts are essentially, water, carbon dioxide, and calcium salts, all of which may be recycled. The method of producing clean burning wood biomass fuels utilizes fewer starting material ingredients, fewer parts or components in the assembly line, thus expediting the rate of production, and thus reduces the time from production to user. These wood biomass fuels burn cleaner, have few, if any, impurities that would adversely affect a clean burn, and may even utilize typically inferior wood biomass and still produce the beneficial clean burning wood biomass fuels. Furthermore, the method of incorporating calcium carbonate into a wood biomass fuel results in reduction of the level of acid and environmental contaminants, e.g. greenhouse gases, methane gas, nitrogen oxides, and carbon monoxide.
NOVELTY - Conversion of a lignin biomass feedstream to a converted lignin stream involves: combining the lignin biomass feedstream with a catalyst comprising nickel oxide and a liquid solvent in a reaction vessel; hydrogenating the lignin biomass feedstream at a hydrogenation temperature and a hydrogenation pressure for a hydrogenation time, where the hydrogen is derived from the group consisting of a hydrogen donor and direct hydrogen gas addition; and deoxygenating the hydrogenated lignin biomass at a deoxygenation temperature and pressure for a deoxygenation time.    USE - For conversion of a lignin biomass feedstream to a converted lignin stream (claimed).    ADVANTAGE - The present method enables continuous lignin conversion in high yields, in particular from biomass feedstock, where 80% of the available lignin in the feedstock is recovered as usable products.
NOVELTY - Process to convert a converted lignin feedstream to a converted lignin product comprised of aromatic compounds, comprises exposing the converted lignin feedstream to at least one catalyst in the presence of many hydrogen donor molecules at 190-350 degrees C for at least 30 minutes, where the converted lignin feedstream comprises phenol oil, and at least some of the hydrogen donor molecules are donated during the exposure of the converted lignin feedstream and donor molecules to the catalyst.    USE - The process is useful for converting converted lignin feedstream to a converted lignin product (claimed) comprising carbon dioxide, methane, ethane, phenols, benzene, toluene, and xylenes that are used in jet fuel.    ADVANTAGE - The process: provides high yields, and recovers 80% lignin as usable product; produces less than 2.5 wt.% aliphatic carbons having number of carbons greater than 11; and removes much of the contaminants from the water of the stillage.
NOVELTY - Preparing fulvestrant (I), comprises: either oxidizing position 6 of tetralin-1-ol compounds (A) using Dess-Martin periodinane oxidizing agent and then adding the side chain in two steps; or oxidizing hydroxy group of (A) using the Dess-Martin periodinane oxidizing agent, alkylating tetralin-1-one compounds (B) with 1,9-dibromononane in a solvent in presence of a base, reacting alkylated derivative (C) with 4,4,5,5,5-pentafluoropentane phenyl thioester in the solvent in presence of a base, and converting 1,1,1,2,2-pentafluorobutane compounds (D) to the fulvestrant by any conventional methods.    USE - The process is useful for preparing (I) (claimed), which is useful for treating locally advanced or metastatic breast cancer in women. No biological data given.    ADVANTAGE - The process provides (I) with high yield and reduced unwanted 7 beta epimer in an environmental friendly manner.    DETAILED DESCRIPTION - Preparing fulvestrant of formula (I), comprises: either oxidizing position 6 of tetralin-1-ol compounds of formula (A) using Dess-Martin periodinane (DMP) oxidizing agent and then adding the side chain in two steps; or oxidizing hydroxy group of (A) using the Dess-Martin periodinane oxidizing agent to obtain tetralin-1-one compounds of formula (B), alkylating (B) with 1,9-dibromononane in a solvent in presence of a base to obtain alkylated derivative of formula (C), reacting (C) with 4,4,5,5,5-pentafluoropentane phenyl thioester in the solvent in presence of a base to obtain 1,1,1,2,2-pentafluorobutane compounds of formula (D), and converting (D) to the fulvestrant by any conventional methods. INDEPENDENT CLAIMS are included for:    (1) the compound (C); and    (2) use of (C) for the preparation of fulvestrant.
NOVELTY - Oil is heated (S1) to a temperature more than the melting temperature of the oil component. An oil modifier containing silicon sol is added to the oil, maintained and stirred (S3) at a temperature more than the melting temperature of the oil component, to obtain modified oil. The silicon sol comprises a silicon-containing solute containing silicon and calcium.    USE - Oil modification method used for improving fluidity of oil e.g. plant oil, animal oil or fat used as raw material for biodiesel fuel and mineral oil.    ADVANTAGE - The oil modification method is economical and capable of improving the fluidity of oil, by a simple process. The modification and purification process are performed simultaneously by a simple and economical process even when waste edible oil is used as a raw material of biodiesel fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for oil modifier, which consists of silicon sol which dissolved the silicon-containing solute which mixed and heat-processed the silicon containing material and the alkaline substance containing calcium in an acid solvent.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart for oil modification method. (Drawing includes non-English language text)    Heating oil or fat (S1)    Dilute and add to oil or fat (S2)    Maintaining oil and fat temperature and stirring (S3)    Adding acetic acid-containing liquid (S4)    Leave to stand and cool (S5)
NOVELTY - An active-hydrogen-permeation-preventing layer consists of a hydrogen-permeation-preventing film for splitting hydrogen gas into protons and electrons to prevent hydrogen gas from permeating the preventing film, and a proton scavenger layer capable of capturing protons passing through the hydrogen-permeation-preventing film to prevent permeation of hydrogen gas. The active-hydrogen-permeation-preventing layer consists of polymer layers.    USE - Active-hydrogen-permeation-preventing layer is used for blocking hydrogen generated from e.g. hydrogen-storage container and semiconductor manufacture.    ADVANTAGE - The active-hydrogen-permeation-preventing layer consists of polymer layers and thus can ensure weight lightening and convenience of processes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for proton scavenger layer.
NOVELTY - The invention relates to a process and an installation for harvesting edible and therapeutical mushrooms cultivated on a germination bed consisting of a cylinder-shaped perforated bag filled with compost. According to the invention, the process also comprises the manipulation of a sporophore bag by a manipulation effector of a double portal robot with 5 axes which is digitally controlled, which also comprises another effector for the sporophore harvesting proper, the bag manipulated by the manipulating effector and harvesting effector being initially reciprocally positioned in preset coaxial and radial positions, further on, by a positive motion of the harvesting effector on the direction of the longitudinal axis of the bag, the sporophore cutting being achieved. The installation, as claimed by the invention, comprises a double portal robot with 5 axes with digital control, provided with some manipulation effectors and some harvesting effectors with coordinated action, the effector for the manipulation of a bag (1) having three electrically-actuated tanks (2), a mobile slide (3), a mobile carriage (4) on a cross member and on some mobile sledges (5.1 and 5.2), respectively, representing the vertical and horizontal positioning system, respectively, the harvesting effector having two electrically-actuated tanks (6), another mobile slide (7) and another mobile carriage (8) on the vertical positioning cross member.
NOVELTY - Solid fuel prepared by mixing livestock feces having a water content of 30-60% with a carbon powder at a ratio of 1:0.1-1 and then molding, is claimed.    USE - Solid fuel.    ADVANTAGE - The solid fuel can be easily prepared in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the solid fuel comprising removing impurities from livestock feces in a housing, primary drying the feces for adjusting its water content to 30-60%, mixing the carbon powder and additive in the dried feces, molding the mixture, and heat-pressing the molded mixture.
NOVELTY - Processing lignin during hydrothermal digestion of cellulosic biomass solids, involves: providing cellulosic biomass solids in a digestion solvent; at least partially converting the biomass solids into a phenolics liquid phase comprising lignin, an aqueous phase comprising an alcoholic component derived from the biomass solids, and an optional light organics phase; combining the phenolics liquid phase and the aqueous phase with one another to form a combined phase; and separating at least a portion of the alcoholic component from at least a portion of the combined phase.    USE - The method is useful for processing lignin during hydrothermal digestion of cellulosic biomass solids (claimed) to produce fuel blends such as biofuels including gasoline hydrocarbons (e.g. straight run gasoline, naphtha, fluidized or thermally catalytically cracked gasoline, VB gasoline, and coker gasoline), diesel fuels and jet fuels.    ADVANTAGE - The method ensures: adequate slurry catalyst distribution, thus reducing thermal gradients that may occur during hydrothermal digestion; and more rapid digestion and efficient conversion rate of cellulosic biomass into fuel blends under elevated temperature and pressure conditions with less energy consumption and reduced loss in catalytic activity of slurry catalyst in an economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composition comprising: water; an organic portion derived from cellulosic biomass solids; and a sulfided cobalt molybdate slurry catalyst, where the organic portion comprises ethylene glycol, propylene glycol and isopropanol.
NOVELTY - The spark plug (1) has a cylindrical metal shell (3), a ground electrode (27) joined to front end portion (26) of metal shell, and a nickel layer formed on ground electrode. The ground electrode has a base material exposed region in which base material of ground electrode is exposed. The nickel layer has outer-lateral-side nickel layer located on outer lateral surface of ground electrode so as to be adjacent to base material exposed region of ground electrode and satisfies a predetermined condition.    USE - Spark plug for use in combustion apparatus e.g. internal combustion engine, fuel cell processing device. Can also be used in alternating-current plasma spark plug.    ADVANTAGE - The nickel layer is applied to ground electrode so as to effectively reduce stress difference between outer-lateral-side nickel layer and the ground electrode and assuredly prevent separation of the nickel layer from ground electrode.    DETAILED DESCRIPTION - The predetermined condition is LA greater than or equal to 25 micrometers in which LA is a length from first part of outer-lateral-side nickel layer having thickness equal to 80 percent of maximum thickness of outer-lateral-side nickel layer to second part of outer-lateral-side nickel layer having thickness equal to 20 percent of the maximum thickness of outer-lateral-side nickel layer in longitudinal direction of the ground electrode (27).    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of the spark plug.    Spark plug (1)    Metal shell (3)    Front end portion (26)    Ground electrode (27)    Spark discharge gap (30)
NOVELTY - Oxygen purification of a supply gas flow (1) comprising 45% of carbon dioxide and 10% of oxygen, comprises (a) performing catalytic oxidation of the supply gas flow in the presence of a fuel, and (b) recovering the oxygen-depleted gas flow.    USE - The method is useful for the oxygen purification of a supply gas flow comprising 45% of carbon dioxide and 10% of oxygen (claimed).    ADVANTAGE - The method enables economic oxygen purification of the supply gas flow in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an installation for the purification of supply gas flow, comprising (i) a unit for heating the supply gas flow at a temperature of 400-500 degrees C, (ii) a first catalytic oxidation reactor for the combustion of oxygen of gas flow heated in presence of methane, (iii) a second catalytic oxidation reactor for the combustion of oxygen of gas flow obtained from the first reactor in present of hydrogen, (iv) a unit for recovering the heat from the reaction of gas flow exiting from the second reactor, and (v) a unit (6) for drying the gas flow exiting from the heat recovery unit.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a catalytic oxidation unit.    Supply gas flow (1)    Heater (2)    First reactor (3)    Second reactor (4)    Drying unit. (6)
NOVELTY - The vehicle has a left-right paired pivot bracket (33) joined to a lower end of a rear-end part of a left-right paired mainframe (32), and a down tube (35) connected to a head tube (31). A fuel tank (5) storing the fuel exhibits a cylindrical shape extended substantially parallel with respect to the down tube, and a fuel cell (2) generates electric power with the fuel supplied from the fuel tank. A motor (3) is made to generate the driving force with the electric power supplied from the fuel cell.    USE - Fuel cell two-wheeled vehicle for off-road travel such as dual per path and motocrosser.    ADVANTAGE - The configuration of the vehicle improves operativity of the fuel cell two-wheeled vehicle in an efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of main parts of a fuel cell two-wheeled vehicle from diagonally left forward.    Fuel cell (2)    Motor (3)    Fuel tank (5)    Head tube (31)    Left-right paired mainframe (32)    Left-right paired pivot bracket (33)    Down tube (35)
NOVELTY - Manufacture of aromatic ester compound involves performing primary process by mixing (S1) a formate ester compound or a formamide compound and a strong base compound with an aromatic compound, carrying out secondary process by mixing an oxidizing agent, an alcohol, and a weakly basic compound, and generating (S2) aromatic ester compound from the aromatic compound in a pot.    USE - Manufacture of aromatic ester compound used as raw material for manufacture of pharmaceuticals and agrochemicals.    ADVANTAGE - The method enables the manufacture of aromatic ester compound having high yield with efficient removal of intermediate products, by simple and economical process, and is non-toxic and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of aromatic amide compound.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart explaining the manufacture of aromatic ester compound. (Drawing includes non-English language text)    Mixing formate ester compound or formamide compound and strong base compound with aromatic compound (S1)    Generating aromatic ester compound from aromatic compound (S2)
NOVELTY - A methane fermentation gas containing methane gas and carbon dioxide gas is purified, and the methane gas is enriched. The carbon dioxide gas is separated from the methane fermentation gas by a pressure-swing adsorption method, to prepare a purified gas. A town gas preparation process is carried out using the prepared purified gas, to obtain the town gas having predetermined composition, calorie amount, and pressure. The pressure of methane fermentation gas is lower than the pressure of the obtained town gas.    USE - Manufacture of town gas (claimed).    ADVANTAGE - The method enables the efficient manufacture of town gas from organic waste e.g. surplus sludge, organic refuse, and organic waste water, by town gas manufacturing system with reduced energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for town gas manufacturing system (1). The system consists of a purifier (6), a recycle gas supply line, a supply blocking mechanism, a control apparatus, and a purified-gas densitometer. The recycle gas supply line supplies the recycle gas into the adsorption tower. The supply blocking mechanism blocks the supply of recycle gas to the adsorption tower. The concentration of methane gas or carbon dioxide gas in the purified gas is measured using the purified-gas densitometer. The control apparatus controls the movement of the supply blocking mechanism and circulation time of recycle gas into the adsorption tower.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of town gas manufacturing system. (Drawing includes non-English language text)    Town gas manufacturing system (1)    Methane fermentation processing apparatus (2)    Purification mechanism (3)    Town gas preparation mechanism (4)    Purifier (6)
NOVELTY - Method for producing combustible gas by anaerobic fermentation, involves (a) taking raw material chosen from corn straw and potatoes, (b) adding corn straw and 5-6 pts. milk in reactor, adding 20-30% the above-mentioned mixture and remaining raw material to activated sludge, fermenting the mixture at 35 degrees C and stirring the fermented mixture, and (c) collecting gas using saturated brine discharging unit.    USE - The method is useful for producing combustible gas by anaerobic fermentation (claimed).    ADVANTAGE - The method changes waste into valuable thing.
NOVELTY - Method for fermenting corn cob for producing hydrogen involves weighing cow dung, corn cob granules, and nutrient solution, adding the weighed materials into reactor, adjusting initial pH to 8 using dilute acid or alkali solution, blowing oxygen and nitrogen, sealing using rubber stopper, maintaining 36 plus minus 1 degrees C, removing carbon dioxide gas through a solution of sodium hydroxide at a predetermined time interval, collecting gas and determining hydrogen content using meteorological chromatography.    USE - The method is useful for fermenting corn cob used for producing hydrogen (claimed).    ADVANTAGE - The method enables fermentation of corn cob for producing hydrogen using waste materials at less energy.
NOVELTY - Method for producing hydrogen by anaerobic fermentation of animal manure and straw, involves naturally drying straw, crushing dried straw into 1-2 cm particles, processing livestock manure, adding the straw, livestock manure and nutrient solution to reaction flask, adjusting pH of added materials to 6-7 using dilute acid or alkali solution, purging the materials with nitrogen, sealing the flask, incubating the flask in shaker, collecting hydrogen gas, and measuring hydrogen content by gas chromatography.    USE - The method is useful for producing hydrogen by anaerobic fermentation of animal manure and straw (claimed), where the hydrogen can be used as clean energy.    ADVANTAGE - The method prevents environmental pollution caused by straw waste and animal waste.
NOVELTY - Method for production of fuel ethanol using papermaking sludge, involves (a) preprocessing papermaking sludge, neutralizing and drying to obtain product, (b) fermenting culture medium comprising peptone, yeast powder and wheat, (c) adding fermented culture medium into conical bottle, adding 5-6 g good papermaking sludge, steam sterilizing, cooling to room temperature, adding cellulose and seed, plugging upper bottle with rubber plug, rotating, and synchronously saccharifying and fermenting mixture, and (d) treating mixture.    USE - The method is useful for production of fuel ethanol using papermaking sludge (claimed).    ADVANTAGE - The method changes waste into valuable products and is environmentally-friendly.    DETAILED DESCRIPTION - Method for production of fuel ethanol using papermaking sludge, involves (a) preprocessing papermaking sludge, neutralizing and drying to obtain product, (b) fermenting culture medium comprising 5 g/l peptone, 3 g/l yeast powder and 3 g/l wheat, (c) adding 50-60 ml fermented culture medium into 250 ml conical bottle, adding 5-6 g good papermaking sludge, steam sterilizing at 121 degrees C for 20 minutes, cooling to room temperature, adding cellulose and seed, plugging upper bottle with rubber plug, rotating at 100-150 revolutions per minute (rpm) and 36 degrees C, and synchronously saccharifying and fermenting mixture, and (d) treating mixture at 4000-5000 rpm.
NOVELTY - Environmental protection septic multi-using marsh gas tank, septic relates to marsh gas tank technology field. The other end in the tank body (1) of upper end side is symmetrically provided with two feeding port (2), tank body (1) of upper end middle part is set with a marsh gas outlet (3), the tank body (1) is provided with a first clapboard (4) and second clapboard (5), first clapboard (4) and the second clapboard (5) are provided with upper liquid fermentation convection hole (6), first clapboard (4) and the second clapboard (5) of upper end are provided with a marsh gas convection hole (7), the tank body (1) of one end is provided with a waste water inlet (8), tank body (1) is provided with a biogas outlet (9) of the tank body (1) is provided with a waste liquid of water level line (10). It has reasonable structure design, simple installation, it is convenient and fast, function diversification, strong abiligy, the size can be freely, can satisfy the life requirement of people.
NOVELTY - Fertilizer composition comprises (in pts.wt.): yeast agent (5-10), colloidal microbial inoculum of Bacillus spores (5-10), phosphate-dissolving microbial inoculum of giant Bacillus spores (5-10), Bacillus subtilis culture (10-15), Aspergillus awamori culture (1-5) and Lactobacillus agent (1-4).    USE - Fertilizer composition.    ADVANTAGE - The fertilizer composition has abundant nutrition and high content of organic matter, and improves micro-ecological environment of soil and provides favorable conditions for the growth of crops.
NOVELTY - Oil sludge treatment involves screening sludge, performing three-phase separation and solvent extraction, adding extracting agent, mixing for 10-90 minutes, injecting additive, mixing 5-30 minutes, distilling to recover crude oil and solvent, floating, filtering using walnut shell, quartz sand or barite, coagulating, performing biological treatment using microbial inoculum, nutrient agent and mixed bacterial agent comprising Pseudomonas aeruginosa, Bacillus subtilis and Rhodococcus.    USE - Method for treating oil sludge(claimed).    ADVANTAGE - The method is environmental-friendly and saves petroleum resource.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of oil sludge treatment (Drawing includes non-English language text).
NOVELTY - Dry fermentation involves mixing pig, cow and chicken manure, performing activated sludge, adding straw, fermenting under water bath at 35 degrees C and collecting gas.    USE - Method for dry fermenting (claimed) used for biogas production.    ADVANTAGE - The method is convenient and does not generate secondary pollution.
NOVELTY - Drying sludge comprises collecting activated sludge in a trough and piling 0.3-2 m high, 0.3-10 m wide and 4-20 m long, fermenting for 1-4 days after the fermentation of activated sludge pile 0.3-2 m high at its bottom, 0.3-10 m wide, and long 4-20 m, and carrying out secondary fermentation for 1-4 days to produce biological fermentation material pile of sludge.    USE - Method for drying sludge (claimed).    ADVANTAGE - The method is environment-friendly, reduces energy consumption of more than 90%, and reduces production of harmful substances.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the method for drying sludge (Drawing includes non-English language text).
NOVELTY - Culture solution comprises 2-10 pts. wt. starch, 4-8 pts. wt. sodium carbonate, 20-50 pts. wt. potassium phosphate trihydrate, 5-10 pts. wt. sodium bisulfate and 1-3 pts. wt. yeast.    USE - The culture solution for fertilizer is useful for improving polysaccharide content and forming spores.    ADVANTAGE - The culture solution produces high quality product.
NOVELTY - Microbial inoculum comprises fermentation liquid having water content of not greater than 35%, and carrier.    USE - The microbial inoculum is useful as fertilizer for crop planting, or matrix (all claimed).    ADVANTAGE - The microbial inoculum increases soil organic substance, promotes rhizosphere microorganism propagation of crop, improves physical and chemical properties and biological activity of soil, provides balanced nutrition, and reduces occurrence of soil-borne disease, and enhancing yield and quality of crops.
NOVELTY - Matrix comprises 100-500 pts. wt. cow dung, 500-1000 pts. wt. corn straw, 50-100 pts. wt. zeolite powder, 100-500 pts. wt. peat, and 10-200 pts. wt. urea.    USE - As matrix for greenhouse soil.    ADVANTAGE - The matrix has good absorption rate and stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the matrix, which involves mixing corn straw powder, peat, urea, and cow dung, passing through 2-3 cm sieve, adjusting moisture content of mixture to 50-60 wt.%, fermenting at 40-50 degrees C, mixing, wetting the mixture using water, continuing fermentation for 5-7 days, turning the mixture when increase in temperature to 5-10 degrees C, turning and ventilating until the temperature dropped to 30-40 degrees C, adding zeolite powder, and stirring the fermented mixture.
NOVELTY - Fertilizer comprises raw materials comprising 60-65 pts. wt. organic fertilizer, 10-15 pts. wt. rare earth fertilizer, 6-10 pts. wt. peat, 3-4 humic acid, 2-3 pts. wt. diethyl aminoethyl hexanoate, 3-5 pts. wt. urea, 6-10 pts. wt. potash fertilizer, and 1-5 pts. wt. calcium-magnesium phosphate fertilizer.    USE - The fertilizer is useful for Jatropha curcas (claimed).    ADVANTAGE - The fertilizer improves conditions of soil, and increases fruit size of the J.curcas, as compared to existing fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned fertilizer, which involves (a) mixing organic fertilizer comprising chicken manure and other livestock and poultry excrement in a ratio of 1:5, sterilizing the mixture at low temperature, and stacking the mixture for 5-10 days, (b) inoculating 90% Bacillus megaterium to 0.2-0.6 wt.% obtained mixture, fermenting the mixture to obtain compost, turning the compost for every 6 days, controlling temperature of the compost to less than 65 degrees C, if the temperature of the compost is higher than 65 degrees C, the compost is turned and fermented for 35-40 days, (c) adding the above-mentioned rare earth fertilizer, peat, humic acid, diethyl aminoethyl hexanoate, urea, potash fertilizer and calcium-magnesium phosphate fertilizer to the fermented compost, and (d) granulating the obtained product at 85-95 degrees C for 10-45 minutes, and metering the product, and packing the product.
NOVELTY - Water retaining fertilizer comprises 49-85.5 wt.% agricultural waste materials, 5-15 wt.% microbial inoculum compound, 0.5-5 wt.% prepared rhizome of Rehmannia, 5-15 wt.% amino acids, 0.5-5 wt.% humic acid, 0.5-5 wt.% mineral elements, and 3-7 wt.% remainder raw materials.    USE - As water retaining fertilizer.    ADVANTAGE - The water retaining fertilizer improves soil structure and soil permeability, improves soil fertility, adjusts soil acid-base balance, improves microenvironment root system of plant, strengthens disease resistance and stress resistance of plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, which involves mixing above-mentioned raw materials, mixng carbon and nitrogen into the mixture in ratio of 20:30:1, fermenting the mixture, drying the mixture, crushing, screening, and obtaining retaining fertilizer.
NOVELTY - ( gamma -Hydroxypropyl)ethylmalonic acid is synthesized by taking sodium hydride, dissolving in organic solvent, adding diethyl ethylmalonate and 1-bromo-3-chloropropane, reacting, extracting with ethyl acetate, vacuum-concentrating, adding ethanol-water solution containing diethyl 2-( gamma -chloropropyl)-2-ethylmalonate and sodium hydroxide, refluxing, adding water, adjusting pH value to 1 by adding hydrochloric acid, crystallizing, and filtering.    USE - Method for synthesizing ( gamma -hydroxypropyl)ethylmalonic acid used as vinpocetine intermediate (claimed).    ADVANTAGE - The environment-friendly method uses cheap raw materials, and has short reaction steps, simple operation, and high product yield.
NOVELTY - Synthetic of nitroso compound (I) involves reacting carbomate compound (II) and benzyl formate compound (III).    USE - Synthetic of nitroso compound used as raw material for preparing dabigatran etexilate.    ADVANTAGE - The method environmentally-friendly provides nitroso compound.    DETAILED DESCRIPTION - Synthetic of nitroso compound of formula (I) involves reacting nitroso compound of formula (II) and benzyl formate compound of formula (III).
NOVELTY - A one sludge earthworm biological nitrogen removal device, comprising a digestion tank and upper side wall of the digestion tank is provided with a water inlet end and water outlet, the water inlet is higher than the water outlet, the bottom is provided with a sludge digestion tank, tank bottom part is further provided with a micro-pore aerator in the digestion tank is provided with a stirring device, the stirring device is hung around the plate-like filler is set between the spherical filler, the spherical filler and the micro-pore aerator of the digestion pool. This utility new type sewage treatment system in the high efficiency sludge decrement and the water outlet ammonia nitrogen, total nitrogen discharge standard, it has low operation cost, simple operation, does not produce second pollution of.
NOVELTY - A one earthworm biological filter pool, comprising a filter tank body, a filter tank body from up to down is provided with a first filter screen layer, earthworm processing layer, a filtering layer, a guide layer and a second filter layer, said earthworm processing layer as the substrate and wood mixed layer is connected with a substrate, said earthworm filter layer is of sawdust powder, said guide layer is gravel, above the first filter layer is provided with a sewage discharge pipe, the second filter layer is set with the liquid collecting tank, the bottom of the liquid tank is provided with a water outlet tube. This utility new type earthworm and microorganism DEG together, abiligy of organic matter greatly improves the filter tank, improves the sewage processing abiligy of filter tank, at the same time, it also increases the filter tank for removing nitrogen and phosphorus in of abiligy, it also overcomes the biological filter pool operation in mud blocking the serious of one.
NOVELTY - A Rhodococcus ruber strain ZHY1-6 (CGMCC 8173), is new.    USE - The R.ruber strain ZHY1-6 is useful for treating wastewater containing organic pollutant chosen from phenol, hydrocarbon, aromatic hydrocarbon, heterocyclic and chlorinated compound (all claimed).    ADVANTAGE - The R.ruber strain ZHY1-6 enables biological treatment of organic pollutant in wastewater and reduces salt concentration of wastewater and thus reduces cost of sewage treatment and protects the environment and people's health.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of the above-mentioned strain for treating wastewater containing organic pollutant.
NOVELTY - A 2,4,5-substituted thiazole ring derivative is synthesized by reacting benzoyl isothiocyanate, sec.-amine, and butynyl ester in organic solvent with enzyme catalyst i.e. Lipase AY30 (RTM: Butyrinase), pig pancreatic alpha -amylase, Aspergillus oryzae amylase, trypsin, or bovine serum protease.    USE - Synthesis of 2,4,5-substituted thiazole ring derivative (claimed).    ADVANTAGE - The synthesis of 2,4,5-substituted thiazole ring derivative is mild, environment-friendly, suitable for recrystallization, and has high yield, shorter reaction time, and easy removal of catalyst.    DETAILED DESCRIPTION - A 2,4,5-substituted thiazole ring derivative of formula (I) is synthesized by reacting benzoyl isothiocyanate of formula (II), sec.-amine of formula (III), and butynyl ester of formula (IV) in organic solvent with enzyme catalyst i.e. Lipase AY30, pig pancreatic alpha -amylase, A. oryzae amylase, trypsin, or bovine serum protease.    R1, R2=alkyl, benzyl, aryl, or heterocyclic aryl; and    R3=Me, or Et.
NOVELTY - The digester system comprises a heating system equipped with a closed water circulation system (100) including a reservoir of water (200), cold water pipe (201) and a hot water pipe (202), a motorcycle (300), a boiler (400) and a set of pipes or hoses (500). A biogas removal element (700) and respective biogas pipe are designed for power boiler. The stirring system is equipped with a loop that is divided into sectors comprising a pump and a set of records maneuver.    USE - Digester system for anaerobic digestion or fermentation for producing fuel gas and fertilizer from organic compounds, such as urban sewage, herbivores excrement or fruit and vegetables remains.    ADVANTAGE - The digester system is provided with feedback of thermal energy, optimized stirring and disposal of sediments, and shows constructive and relevant structure.    DETAILED DESCRIPTION - The digester system comprises a heating system equipped with a closed water circulation system including a reservoir of water, cold water pipe and a hot water pipe, a motorcycle, a boiler and a set of pipes or hoses. A biogas removal element and respective biogas pipe are designed for power boiler. The stirring system is equipped with a loop that is divided into sectors comprising a pump and a set of records maneuver. The loop comprises a suction pipe and an injection pipe. The sediment removal system is endowed with an access pipe to bottom of the digester. The access pipe is disposed for removing sediment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the heating system.    Closed water circulation system (100)    Water (200)    Cold water pipe (201)    Hot water pipe (202)    Motorcycle (300)    Boiler (400)    Hoses (500)    Biogas removal element (700)
NOVELTY - A cottonseed soy sauce is processed by degrading cottonseed using gossypol degradation bacterial strain and soy sauce-brewing cottonseed in which degradation efficiency is greater than or equal to 90%.    USE - Process for cottonseed soy sauce (claimed).    ADVANTAGE - The process is simple, effectively removes toxicity, and has high degradation rate, detoxification rate, and protein content, no chemical agent addition, short fermentation time, small investment, simple device, no wastewater pollution, and low cost.
NOVELTY - Decomposition of ammonia to hydrogen tube-type plasma reactor comprises two metal tubes of high-voltage electrode (1) and ground electrode (5), feeding port, decomposition gas discharge port, and reactor shell (2) with heat-insulating material (3).    USE - Decomposition of ammonia to hydrogen tube-type plasma reactor used for chemistry and energy technology field.    ADVANTAGE - The plasma reactor improves energy utilization rate of insulating layer and efficiency of gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of decomposition of ammonia to hydrogen tube-type plasma reactor.    High-voltage electrode (1)    Reactor shell (2)    Heat-insulating material (3)    Insulating seal device (4)    Ground electrode (5)
NOVELTY - Active carbon from rice straw anaerobic fermentation residue is prepared by drying rice straw anaerobic fermentation residue, crushing and sieving to obtain residue powder; adding powder into potassium hydroxide solution, uniformly stirring and mixing, impregnating, and performing solid-liquid separation; drying impregnated powder, activating in a muffle furnace, cooling activated powder, pickling using 1 M hydrochloric acid solution, and washing with hot distilled water; and drying activated powder, grinding and sieving to obtain active carbon finished product.    USE - Method of preparing active carbon used in treating cadmium-containing wastewater (claimed).    ADVANTAGE - The method has simple operation, low cost and less pollution. The obtained activated carbon has good metal ion adsorption with adsorption capacity for cadmium ion of 20.79-66.22 mg/g.
NOVELTY - Preparation of microbial fertilizer comprises adding nitrogen-fixing species of activated sterilized seeds into liquid medium, adjusting pH to 7.5, incubating at 31 degrees C for 5 hours, and inoculating 4% sterile medium at 31 degrees C for 15 hours; diluting 25 kg 90% sulfuric acid with 5 times water, adding 1000 kg biomass plant ash, and uniformly stirring; mixing with 500 l fermentation broth and stirring; adding molasses and bran; controlling water content at 50% and granulating; drying at 150-200 degrees C for 15-30 minutes until water content is not greater than 20% and particle intensity is more than 50 N; and packing.    USE - Method for preparing microbial fertilizer (claimed).    ADVANTAGE - The fertilizer has low impurity content of viable bacteria, does need not sterilizing treatment, and has low cost. The addition of molasses and bran can prolong shelf life to more than 12 months.    DETAILED DESCRIPTION - Preparation of microbial fertilizer comprises:    (A) adding nitrogen-fixing species of activated sterilized seeds into liquid medium, adjusting pH to 7.5, incubating at 31 degrees C for 5 hours, inoculating 4% sterile medium at 31 degrees C for 15 hours, where liquid seed medium is glucose, peptone and minerals and culture medium is sucrose, corn flour, yeast cream, peptone, and nutrients;    (B) diluting 25 kg 90% sulfuric acid with 5 times water, adding 1000 kg biomass plant ash, and uniformly stirring;    (C) mixing with 500 l fermentation broth and stirring;    (D) adding molasses and bran;    (E) controlling water content at 50% and granulating;    (F) drying at 150-200 degrees C for 15-30 minutes until water content is not greater than 20% and particle intensity is more than 50 N; and    (G) packing.
NOVELTY - A soluble hemostatic gauze contains gauze, sodium hydroxide, and methyl chloride in reaction solvent which is isopropanol reacted with methylcellulose in which weight ratio gauze:sodium hydroxide:methyl chloride is 1:1:1.2.    USE - Soluble hemostatic gauze for surgery, trauma, stopping bleeding, tooth extraction surgery, and skin wound protection.    ADVANTAGE - The gauze maintains wound humidity, accelerates tissue healing, stops bleeding quickly, has no medicine components and side effects, is non-toxic, and process is simple and reduces toxic raw materials, cost, and pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing process of soluble hemostatic gauze which involves washing gauze with purified water for 1 hour in which ratio gauze:purified water is 1:100, heating and alkalizing gauze, 45-50% sodium hydroxide solution, and isopropanol in high-pressure container at 25 degrees C and 5 atm for 0.5-1.5 hours, adding methyl chloride, heating to carry out etherification at 85 degrees C and 5 atm for 3-5 hours, discharging reaction solution, rinsing solution using 75 degrees C hot water for 20-40 minutes, discharging washing liquid, adding 75 degrees C hot water, acid-base indicator, and concentrated hydrochloric acid sequentially, neutralizing and rinsing until reaction solution is neutral, discharging washing solution, rinsing using 75 degrees C hot water for 20-40 minutes, removing generated salt, drying gauze at 40-50 degrees C, checking semi-finished product, weighing, and packaging.
NOVELTY - The design method involves making first layer the water layer of the secondary sedimentation. The fifth layer of the tank is a water inlet layer that is from the reaction tank through the mixed solution of entering into layer, the n-layer which is bottom layer, and a settling layer. The sludge concentration at maximum value is equivalent to the actual secondary sedimentation tank mud hopper in the bottom layer portion of the secondary sedimentation tank.    USE - Optimization design method for sewage treatment plant sedimentation tank.    ADVANTAGE - The optimization design method provides effective operation activity of sludge treatment process, and is suitable for sewage sedimentation optimization and operation.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the sedimentation tank. (Drawing includes non-English language text).
NOVELTY - A full-underground concrete interlayer one fermentation tank a cubic or more marsh gas fermenting device, marsh gas fermentation device belonging to the technical field of the current full-underground fermenting tank concrete marsh gas fermenting device of marsh gas fermentation tank construction, intensity is low, the marsh gas fermentation device integrated complex structure of. Marsh gas fermentation used it is interlayer composite poured concrete field of marsh gas fermenting tank body, inspection hole is further provided and connected instrument with a seal cover of integrated controller interface monitoring display device of the marsh gas fermentation tank body upper oval sealing head, and the top of the marsh gas fermentation tank are connected by center shaft part to the bottom of the tank body is provided with is sleeved on the center sleeve of biogas output tube and biogas output tube connecting port is set on upper body of marsh gas fermenting residue pump. The marsh gas fermentation device of the whole structure is simple, which is suitable for 500 m3 or more volume in raw material is large biogas fermenting production system of pure straw.
NOVELTY - Microbial fertilizer comprises 2-5 wt.% molasses, 3-5 wt.% wheat bran, 70-75 wt.% sugarcane residue, 5-10 wt.% tobacco powder, 4-8 wt.% maifanite, 1.5-0.5 wt.% bacteria for decomposition, 2-3 wt.% strain capable of fixing nitrogen and solubilizing phosphorus and potassium and 3.5-6.5 wt.% bentonite.    USE - As microbial fertilizer.    ADVANTAGE - The microbial fertilizer prepared by simple energy saving method is cost-effective and environmentally-friendly and has bran and molasses which maintains the activity of microorganisms and prolongs shelf-life to more than 12 months.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer which involves (a) weighing the raw materials, (b) mixing the raw materials in a tank, stirring at 45-55 revolutions per minute and 20-35 degrees , (c) fermenting the stirred raw materials at 40 degrees , raising the temperature daily by 10 degrees until the temperature reaches 90 degrees , stop heating and sealing the fermentation tank for 30 days, (d) confirming that the fermented product has no bacterial contamination by culture experiments, centrifuging and discarding supernatant to obtain precipitate containing wet cells, (e) sterilizing the wet cells at 120-150 degrees C for 2-3 hours and (f) granulating the cells obtained in step (e) using granulating machine by setting the temperature at 138-144 degrees C and drying in oven for 25-28 minutes until moisture content reaches not greater than 30% with a particle strength of 50 N.
NOVELTY - Compositing slag and pig manure using fermentative bacteria for producing organic fertilizer mix, involves (a) mixing fresh manure, straw, urea and glucose, regulating the moisture content to be 60-65%, stacking, fermenting for 20-30 days , and dry packing to obtain inoculum, (b) mixing fresh mushroom and fungus residue , fresh manure and straw, piling the mixture to a height of 2-3 m, fermenting at 60 degrees C, turning once in 2-3 days until composting, and obtaining organic fertilizers.    USE - The method is useful for compositing slag and pig manure using fermentative bacteria for producing organic fertilizer mix (claimed).    ADVANTAGE - The method enables rapid composting, to provide high temperature for long duration and to thoroughly kill bacteria and harmful spores, has short processing cycle, less nutrient loss and low investment, yields high-quality organic fertilizer, is simple to perform, and reduces waste and pollution of the environment, thus utilizes waste resource.    DETAILED DESCRIPTION - Method for compositing slag and pig manure using fermentative bacteria for producing organic fertilizer mix, involves (a) mixing fresh manure, straw, urea and glucose in a weight ratio of 500-600:400-500:4-6:9-11, regulating the moisture content to be 60-65%, stacking, fermenting for 20-30 days (turning once in every 2-4 days interval), and dry packing to obtain inoculum, (b) mixing fresh mushroom and fungus residue having moisture content of 60-65%, fresh manure having moisture content of 1-2% and straw having moisture content of 1-2% in weight ratio of 300-400:500-600:200-300, piling the mixture to a height of 2-3 m, fermenting at 60 degrees C, turning once in 2-3 days until composting, and obtaining organic fertilizers.
NOVELTY - Preparation of quinuclidine ring compound involves providing ethanol solution of aromatic aldehyde and ethanol solution of aromatic amine into primary microchannel of modular microchannel reactor, reacting the resultant product at 85-125 degrees C for 3-7 minutes under atmospheric pressure, then providing ethanol mixed solution of cyclohexenone and phosphotungstic acid, injecting primary resulatnt product, reacting at 100-140 degrees C for 10-25 minutes, separating the resultant product, and maintaining the resultant product to separate into layers.    USE - Preparation of quinuclidine ring compound (claimed).    ADVANTAGE - The method economically and environmentally-friendly provides safe quinuclidine ring compound having high conversion rate and excellent stability.    DETAILED DESCRIPTION - Preparation of quinuclidine ring compound involves providing ethanol solution of aromatic aldehyde and ethanol solution of aromatic amine into primary microchannel of modular microchannel reactor, reacting the resultant product at 85-125 degrees C for 3-7 minutes under atmospheric pressure, then providing ethanol mixed solution of cyclohexenone and phosphotungstic acid into secondary microchannel reactor, injecting primary resulatnt product, reacting at 100-140 degrees C for 10-25 minutes under atmospheric pressure, separating the resultant product, and maintaining the resultant product to separate into layers, in which the upper layer is isoquinoline ring compound.
NOVELTY - Extracting natural borneol involves collecting camphor leaves and branch, drying, coarse crushing, cutting the dried leaves and branch by using cutting device, sorting the raw material into air-separating device, finely dividing raw materials, using hammer chip crusher, crushing the particle through 20-mesh sieve, distilling and condensing the raw materials semi-finished product with water to form condensed natural borneol, using anhydrous alcohol extracting, filtering residue, distilling to remove water-free alcohol to form crude extract, then adding water, distilling and condensing.    USE - For extracting natural borneol (claimed).    ADVANTAGE - The method improves production efficiency and yield; has large scale of industrial production; and reduces energy consumption.    DETAILED DESCRIPTION - Extracting natural borneol involves collecting camphor leaves, and camphor branch, drying, coarse crushing, cutting the dried leaves, and branch by using cutting device, sorting the cut crushed raw material into air-separating device, separating branches and leaves, finely dividing raw materials of fine-particle by adopting different devices, using a hammer chip crusher, crushing the particle through 20-mesh sieve, fine crushing, distilling and condensing the raw materials semi-finished product with water to form condensed natural borneol, using anhydrous alcohol extracting, filtering residue, distilling to remove water-free alcohol to form crude extract of natural borneol, then adding water, distilling and condensing to obtain natural borneol. An INDEPENDENT CLAIM is included for natural borneol extraction device comprising pre-processing device, air conveying device, winnowing device, hammer chip crusher, leaf cutting device, discharging device, extracting device, filtering device, evaporating device, and distilling device.
NOVELTY - Manufacture of heat tabs involves collecting organic waste, crushing organic waste, pelletizing crushed material using pelletizing device, drying at 60-70 degrees C, pulverizing, fermenting organic waste using 20-30 volume% vinyl compound, leaching, drying, crushing, pelletizing and extruding.    USE - Manufacture of heat tabs (claimed).
NOVELTY - Method for treating food waste, involves sequentially supplying crushed food wastes to microorganism treating reservoirs through distribution unit, and decomposing the food wastes in microorganism treating reservoirs, where treated products are sequentially discharged.    USE - The method is useful for treating food waste (claimed).    ADVANTAGE - The method is suitable for kitchen waste, does not generate liquid garbage, and is rapid and convenient to perform.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for treating food waste.
NOVELTY - Producing biogasoline comprises: drying nyamplung seeds, steaming, cooling and mechanically squeezing to obtain dirty oil; adding phosphoric acid to the oil and performing esterification followed by a transesterification reaction to obtain fatty acid methyl ester; and performing stage 1 hydrocracking reaction i.e. hydrogenation reaction of the fatty acid methyl ester and stage 2 hydrocracking reaction i.e. hydrogenolysis of the fatty acid methyl ester.    USE - The method is useful for producing biogasoline (claimed).    ADVANTAGE - The method produces biogasoline with high-quality.
NOVELTY - Preparing ethyl 3-(5-(3-chloro-2-fluorobenzyl)-2,4-dimethoxy phenyl)-3-oxopropanoate, comprises: converting 5-(3-chloro-2-fluorobenzyl)-2,4-dimethoxybenzoic acid into 5-(3-chloro-2-fluorobenzyl)-2,4-dimethoxybenzoyl chloride (A1) in presence of a reagent; reacting (A1) with diethyl malonate to obtain 2-(5-(3-chloro-2-fluoro-benzyl)-2,4-dimethoxy-benzoyl)-malonic acid diethyl ester (A2); and decarboxylating (A2) to obtain (I).    USE - The process is useful for preparing (I) (claimed) which is useful for preparing elvitegravir, where the elvitegravir is useful for treating infection with the human (HIV).    ADVANTAGE - The process: provides (I) with improved purity and less difficulty and less by-products; and utilizes less costly reagents; and is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for (5-(3-chloro-2-fluoro-benzyl)-2,4-dimethoxy-benzoyl)-malonic acid diethyl ester.
NOVELTY - Production of cresol by phenol methanol gas-phase alkylation, involves after being pre-heating methanol with diluent gas, continuously passing through phenol and methanol alkylated catalyst bed layer, where the reaction temperature is 200-500 degrees C, under the condition of a gas-phase reaction to generate cresol, then mixing with binder, performing acid treatment and water vapor treatment process to give product.    USE - For the production of cresol (claimed).    ADVANTAGE - The method is environmentally friendly; does bot cause equipment corrosion; and has good industrial application prospect. The catalyst has good stability in the production process.
NOVELTY - Bacillus subtilis strain JF with the preservation number CGMCC NO. 7950, is new.    USE - The strain is useful in degrading phthalate compound (claimed).    ADVANTAGE - The strain: ensures degradation of phthalate in polluted soil, achieves bioremediation of water bodies or biological purification, protects ecological environment, and guarantees safety of agricultural product (claimed); and has fast growth speed, resistance for external environment, and has phthalate degradation rate of more than 90% at wide temperature of 30-45 degrees C and wide pH of 5-8.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of the strain in degrading phthalate compound.
NOVELTY - A microbial fertilizer, comprises: 20-25 wt.% pig manure, 5-6 wt.% sugarcane filter mud, 45-47 wt.% tobacco powder, 1-2 wt.% medical stone, 10-15 wt.% rhizome of rehmannia, 4-8 wt.% inoculant bacteria, 1-2 wt.% solid nitrogen, 1-2 wt.% potassium phosphorus, and 3-5 wt.% bentonite strain.    USE - As microbial fertilizer (claimed) used in agriculture.    ADVANTAGE - The process is simple and easy, energy-saving and environment-friendly. The microbial fertilizer has good effect of eliminating the hardening of the soil, inhibits soil disease, and has good upgrading effect. The process has positive agricultural practicability, is simple, cost is low, and is easy to carry out.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of microbial fertilizer, involving: (1) feeding the raw material in a feeding storage tank, stirring and mixing at 45-50 revolution per minute (rpm); (2) collecting the mixed material in the fermentation tank, fermenting at 25 degrees C, and raising temperature upto 70 degrees C, stop heating, sealing the fermentation tank for 10 days; (3) putting fermented material in fermentation expiration, experimenting pure bacterium from foreign bacteria pollution, centrifuging to remove supernatant, obtain concentrated thalli; (4) sterilizing thallus at 120-150 degrees C for 2-3 hours; (5) granulating the material in steam drum granulator by granulation treatment process; and (6) drying cylinder in air to obtain microorganism fertilizer.
NOVELTY - A refrigerant comprises carbon dioxide and ethane.    USE - Refrigerant is used for attaining low temperature (claimed).    ADVANTAGE - The refrigerant is environmentally-friendly, and efficiently attains low temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for attaining low temperature, which involves using refrigerant in two-stage refrigeration system.
NOVELTY - Making biodiesel involves: reacting rubber seed oil (Havea brasiliensis), and butanol using catalyst crude papaya lipase (CPL).    USE - For making biodiesel (claimed).    ADVANTAGE - The prepared biodiesel has density, viscosity and acid number of 1:2, 1:3, and 1:4. The density value of each comparison is 878.3 kg/m3, 870.5 kg/m3, and 871.1 kg/m3, viscosity is 5686 cSt, 4,285 cSt and 4,191 cSt and the acid value is 45 mg KOH/g, 40 mg KOH/g, and 32.1 mg KOH/g. The method uses the catalyst which avoids formation of byproducts. The method is environmentally friendly, with considerable selection of raw materials; uses catalyst CPL enzyme that will generate waste that is more environmentally friendly when compared to the base catalyst. The method is performed at a temperature of 50 degrees C and not at high temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the rubber seed oil involving: taking kg fruit seeds and rubber then smoothed by using ground and blended; sokhlet extraction using n-hexane in 1500 ml; evaporating the n-hexane from the extract using rotary evaporator to obtain pure rubber seed oil.
NOVELTY - A heteroatom-containing organic microporous material contains branched conjugated polymeric microporous material.    USE - Heteroatom-containing organic microporous material for preparing gas absorbing or storing functional material for nitrogen oxygen, hydrogen and/or carbon dioxide, and photoelectric material (all claimed).    ADVANTAGE - The heteroatom-containing organic microporous material has excellent optical performance, and simple preparation.    DETAILED DESCRIPTION - A heteroatom-containing organic microporous material contains branched conjugated polymeric microporous material of formula (I) or formula (II).    R=H, hydrophobic group, hydrophilic group, chiral group, ester, CN, NH2, or SH.    An INDEPENDENT CLAIM is included for preparation of heteroatom-containing organic microporous material which involves subjecting bromoiodobenzene or 2-bromo-4-iodopyridine initial raw material to Sonagashira-Suzuki coupling reaction to obtain diphenyl acetylene derivative, performing trimerization reaction catalyzed by cobalt carbonyl to obtain terpolymer precursor, subjecting to Scholl reaction with ferric chloride oxidizing agent to prepare high molecular polymer.    DESCRIPTION OF DRAWING(S) - The drawing shows solid nuclear magnetic resonance carbon spectrum (13CNMR) of heteroatom-containing organic microporous material.
NOVELTY - Preparation of imatinib or imatinib mesylate, involves (a) reducing a nitro pyrimidine intermediate (II) by hydrazine hydrate in the presence of a solvent to form an amino pyrimidine intermediate (III), (b) condensing (III) with a hydrochloride salt of benzoyl chloride intermediate (IV) in the presence of a solvent and pyridine to give imatinib, (c) optionally, purifying imatinib with a solvent, and (d) optionally, converting imatinib to its mesylate salt in the presence of a solvent.    USE - The process is useful for the preparation of imatinib or imatinib mesylate (claimed), which is useful for the treatment of chronic myeloid leukemia (CML) and gastrointestinal stromal tumors (GIST), and for the treatment of pediatric patients with Philadelphia chromosome positive (Ph+) chronic myeloid leukemia in chronic phase. No biological data given.    ADVANTAGE - The process rapidly provides imatinib with substantially free of genotoxic impurity (i.e. below 10 ppm) in a cost-effective, industrial and environmentally-friendly manner.    DETAILED DESCRIPTION - Preparation of imatinib or imatinib mesylate, involves (a) reducing a nitro pyrimidine intermediate of formula (II) by hydrazine hydrate in the presence of a solvent to form an amino pyrimidine intermediate of formula (III), (b) condensing (III) with a hydrochloride salt of benzoyl chloride intermediate of formula (IV) in the presence of a solvent and pyridine to give imatinib (I), (c) optionally, purifying imatinib with a solvent, and (d) optionally, converting imatinib to its mesylate salt in the presence of a solvent. INDEPENDENT CLAIMS are included for:    (1) the preparation of (IV), comprising reacting of 4-((4-methyl-piperazinyl)methyl) benzoic acid dihydrochloride with thionyl chloride in the presence pyridine in solvents-A; and    (2) the crystalline form of imatinib having powder X-ray diffraction pattern, as given in the specification.
NOVELTY - Composition comprises 100 pts. wt. organic sludge of food waste and marine waste, 35-45 pts. wt. sample, 55-65 pts. wt. sawdust, 0.5-1.5 pts. wt. purifying agent and 0.5-1.5 pts. wt. deodorizing agent. The purifying agent includes silver nitrate, auric chloride, borax, salt, and purified water.    USE - The composition is useful as organic fertilizer (claimed).    ADVANTAGE - The composition reduces amount of waste, improves fertility of soil by alkalinizing soil, enables continuous cropping and increases yield of agricultural product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the composition, which involves crushing organic sludge of food waste and marine waste, sample and sawdust, mixing the crushed components, drying the mixture till the water content of the mixture is 20-40%, transferring to the compost unit equipped with diffuser for controlling mixture to the thickness of 1.5-2 m, fermenting the mixture for 2-3 weeks, and mixing the fermented product with purifying agent and deodorizing agent to obtain product.
NOVELTY - The accumulator is attached to a fuel pick-up on a secondary side of a fuel tank at a top and a vacuum aspiration pump from a primary fuel pump module on a bottom to allow the accumulator to fill during straight line driving. The fuel is available to the primary fuel pump module to provide a fuel supply to the fuel pump and the engine during high speed at low fuel level turning maneuvers.    USE - Sealed accumulator for providing a reservoir of fuel for high performance vehicle applications.    ADVANTAGE - The accumulator is integrated into the fuel tank-mounted baffle for allowing for pre-fabrication and assembly into the fuel tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of a sealed accumulator integrated into the fuel tank-mounted baffle.
NOVELTY - The utility model claims a sewage purifying device, especially one kind of microorganism decomposing composite landscape plant absorbing purifier, comprising a sewage pump water inlet pipe upper is equipped with sewage purifying device on the water outlet end of the pump, wherein said sewage purifying device further comprises a slow release drug feeding tank and sewage purifying tank, said sewage purifying box and comprising a shell, at least one of the biological bed is placed in the shell, the upper mesh plate B is placed in the biological bed is provided with a bio-bed and bed set up water through hole of the box, the lower part is installed on the sewage purifying tank upper water distributor of the water diversion hole mesh plate B, the water distributor with the slow release medicine adding tank, the top part of the biological bed is placed in the said sewage purifying box is located at the upper layer is provided with a mesh plate, the mesh plate A and sewage purifying box of the top part to form the inner wall of the plant planting part. The said structure of the utility model has the advantages as follows: simple structure, reduces the energy consumption, improves the environmental protection and reduces the using cost.
NOVELTY - Preparing bio-organic fertilizer comprises adding fresh chicken manure, pig manure, azotobacter, ammonifying bacteria and yeast into a fermentation tank, then mixing, fermenting and transferring into a mixing machine, adding crushed bean, peanut cake, rape straw, monosodium glutamate and canal mud into the mixing machine, fermenting, and transferring to the mixing machine, crushing urea, calcium superphosphate, potassium sulfate, iron and copper amino acid chelates, humic acid chelated zinc, humic acid chelated calcium, phoxim granules and wet powder carbendazim.    USE - The bio-organic fertilizer is useful cultivating watermelon (claimed).    ADVANTAGE - The method is capable of the bio-organic fertilizer without bad odor. The fertilizer is convenient to use.    DETAILED DESCRIPTION - Preparing bio-organic fertilizer comprises adding 17-19 wt.% of fresh chicken manure, 35-37 wt.% of pig manure, 0.1 wt.% of azotobacter, 0.1 wt.% of phosphate dissolving fungi, 0.1 wt.% of phosphate dissolving bacteria, 0.1 wt.% of ammonifying bacteria and 0.1 wt.% of yeast into a fermentation tank, then mixing, sealing the fermentation tank, fermenting for 9-11 days to obtain bio organic mixture, transferring the mixture into a mixing machine, crushing 4 wt.% of bean cake, 4 wt.% of peanut cake, 10 wt.% of rape straw, 4 wt.% of monosodium glutamate and 8 wt.% of canal mud, adding into the mixing machine, then mixing, sealing and fermenting the mixture for 28-32 days, transferring the mixture into the mixing machine, crushing the 2 wt.% of urea, 8 wt.% of calcium superphosphate, 3 wt.% of potassium sulfate, 0.3 wt.% of iron amino acid chelates, 0.2 wt.% of copper amino acid chelate, 0.2 wt.% of humic acid chelated zinc, 0.3 wt.% of humic acid chelated calcium, 0.5wt.% of phoxim of 5 wt.% granules and 0.5 wt.% of wet powder of 50 wt.% carbendazim, adding the crushed mixture into the mixing machine, and uniform mixing.
NOVELTY - Making biodiesel from oil residues in soil in situ through two stages involves in situ esterification followed by in situ transesterification with methanol, the ratio of methanol/soil is 4/1 (vol./wt.).    USE - The process is useful for making biodiesel from oil residues in soil in situ through two stages (claimed).    ADVANTAGE - The process reduces the number of process steps required, and avoids the use of extraction solvents, for example hexane, thus significantly lowering the cost of the process.
NOVELTY - Preparation of hydrotalcite-like compound involves preparing brine water as main ingredient for processing hydrotalcite-like compound, removing calcium ions in brine water by adding a mixture of sodium carbonate and sodium bicarbonate and heating, separating precipitated calcium carbonate and obtaining precursor solution as filtrate, adding aluminum chloride hexahydrate to precursor solution, adding a solution of sodium carbonate to precursor solution, heating precursor solution, cooling, filtering, washing, and drying.    USE - Preparation of hydrotalcite-like compound used as catalyst for transesterification of palm oil into biodiesel.    DETAILED DESCRIPTION - Preparation of hydrotalcite-like compound involves preparing brine water as main ingredient for processing hydrotalcite-like compound, removing calcium ions in brine water by adding a mixture of sodium carbonate having concentration of 0.1 M and sodium bicarbonate having concentration of 0.2 M until equivalence is 1.2 and heating at 95 degrees C for 1 hour, separating the precipitated calcium carbonate with filter paper and obtaining precursor solution as filtrate, adding aluminum chloride hexahydrate to precursor compound such that the mole ratio of magnesium with respect to aluminum is 2, adding a solution of sodium carbonate having concentration of 0.1 M to the precursor solution until pH is 10.5, heating the precursor solution by stirring for 1 hour, cooling the obtained hydrotalcite-like compound to room temperature, filtering, washing until the compound is free of chloride ions, and drying at 105 degrees C for one night.
NOVELTY - The utility model belongs to the aquaculture industry, specifically one for circulating water pollution-free breeding loach pool, this utility model through the loach pool sludge digging the periphery annular groove, chicken manure fermenting tank, water well, the chicken manure slurry into annular ditch breeding plankton is loach feed quality, and well adjust the temperature and so on, basically prevents the loach the disease's possible, which greatly reduces the manual throwing fodders's time, the sixth, seventh, eighth three months for not throwing fodders, not only reduces the production cost, but also the output's loach is improved by 4 to 5 times, and the annular groove in generating's can be used as agricultural fertilizer to form the good's circular economy.
NOVELTY - Bio-fertilizer comprises 1-2 wt.% of composite probiotics, 27-35 wt.% of nutrients, 50-60 wt.% of yellow humic acid, and 10-15 wt.% of water.    USE - The bio-fertilizer is useful for inhibiting the invasion of pathogenic microorganisms in soil and on crops, and preventing maggot, blight, late blight and downy mildew.    ADVANTAGE - The bio-fertilizer has rich nutrient content and efficiently improves crop yield by 10-30%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the bio-fertilizer comprising adding composite probiotics, nutrients and water, and then mixing to obtain a mixture, adding yellow humic acid and the rest water to the mixture to obtain a mixed material, and fermenting the mixed material.
NOVELTY - Biofertilizer comprises 56-80 wt.% of organic fertilizer, 8-16 wt.% of nitrogen, 4-9 wt.% of phosphorus, 5-15 wt.% of potassium oxide, and 20-80 millions units/g of microorganisms.    USE - The biofertilizer is useful for: reducing plant diseases; controlling insects; and promoting plant growth.    ADVANTAGE - The biofertilizer can be economically prepared with high yield of 15% and quality, and improves the soil fertility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing the biofertilizer comprising adding organic fertilizer and microorganism, uniformly mixing, stirring, fermenting, crushing, adding nitrogen, phosphorus and potassium oxide, uniformly mixing, granulating, drying, checking and packing.
NOVELTY - Pretreatment method for anaerobic digestion liquid in pig farm, involves collecting anaerobic digestion liquid in marsh gas tank through pipeline, transferring into homogenizing adjusting tank, adding sodium carbonate solution, adjusting the pH, adding water into reaction tank, uniformly adding the modification residue, performing aeration, adding water, taking precipitate, precipitating supernatant, transferring sludge, concentrating sludge, centrifuging, dehydrating separated liquid into adjusting tank, and obtaining dehydrated residue.    USE - The pretreatment method is useful for anaerobic digestion liquid in pig farm (claimed).    ADVANTAGE - The method provides soil improved property.    DETAILED DESCRIPTION - Pretreatment method for anaerobic digestion liquid in pig farm, involves collecting anaerobic digestion liquid in marsh gas tank through pipeline, transferring into homogenizing adjusting tank, adding sodium carbonate solution, adjusting the pH of the liquid to 9.5, adding water into reaction tank, uniformly adding the modification residue, performing aeration for 2 hours, adding water into sedimentation tank, taking precipitate, precipitating for 30 minutes, precipitating supernatant to the next biochemical processing unit, transferring sludge to sludge concentrating tank and adjusting pool, concentrating sludge, centrifuging, dehydrating separated liquid into adjusting tank, and obtaining dehydrated residue as slow release organic fertilizer or soil conditioner.
NOVELTY - Preparing (S)-4,5-dimethoxy-1-(methylaminomethyl)-benzocyclobutane hydrochloride (I), comprises (a) carrying out chiral resolution of 4,5-dimethoxy-1-(aminomethyl)-benzocyclobutane (IV) to obtain (S)-4,5-dimethoxy-1-(aminomethyl)-benzocyclobutane (III), (b) acylating (III) to obtain (S)-4,5-dimethoxy-1-(formamidomethyl)-benzocyclobutane (II), and (c) reducing (II) to obtain (I).    USE - The method is useful for preparing (S)-4,5-dimethoxy-1-(methylaminomethyl)-benzocyclobutane hydrochloride (claimed).    ADVANTAGE - The method: has simple operation, high product purity and yield, less by-products, and mild reaction conditions; and is easy to control, easy to process, and environment-friendly.    DETAILED DESCRIPTION - Preparing (S)-4,5-dimethoxy-1-(methylaminomethyl)-benzocyclobutane hydrochloride of formula (I), comprises (a) carrying out chiral resolution of 4,5-dimethoxy-1-(aminomethyl)-benzocyclobutane of formula (IV) to obtain (S)-4,5-dimethoxy-1-(aminomethyl)-benzocyclobutane of formula (III), (b) acylating (III) to obtain (S)-4,5-dimethoxy-1-(formamidomethyl)-benzocyclobutane of formula (II), and (c) reducing (II) to obtain (I).
NOVELTY - A biological processing agent comprises microbial inoculum and carrier.    USE - As biological processing agent used in garbage processing application; used in centralized waste treatment.    ADVANTAGE - The biological processing agent is effectively degrade waste, especially food waste, degradation rate of 85%, improves the living environment and reduces pollution.
NOVELTY - Preparing furfural involves a) charging agricultural waste produce with particle size of 2-10 mm2 and comprising 2-35% of pentosan into pressure vessel with top man hole and bottom valve; b) impregnating sulfur trioxide gas into waste produce by supplying gas; c) pressurizing contents of vessel by injecting steam at pressure of 8-12 kg/cm2; d) maintaining temperature of contents of vessel at 120-160 degrees C for 4-10 hours at pH of 1-5; and e) subjecting generated vapors comprising furfural, acetic acid, acetone, methanol and steam to condensation followed by fractionation to obtain furfural.    USE - For preparing furfural from agricultural waste produce such as corn cobs, bagasse, rice husk, cotton seed, oat hulls, saw dust, wood residues, straw, bamboo, wood chips and olive press-cake (claimed) or from agro-industry waste; where furfural is used as raw material in pharmaceutical industry.    ADVANTAGE - The process is simple, economic and environmental friendly and produces furfural with higher yield which facilitates removal of by-products during reaction. The mass left after completion of reaction is comparatively non-acidic and non-corrosive. The process requires less water compared to prior art processes and is amenable to larger scale.
NOVELTY - A method of preparation of methane-oxidizing bacterial liquid involves: mixing mineralizing waste, percolation liquid and methane in presence of oxygen to obtain methane-oxidizing bacterial liquid, where the mineralized waste methane oxidation rate is more than 50%.    USE - In the preparation of methane-oxidizing bacterial liquid (claimed).    ADVANTAGE - The method has high landfill methane oxidation efficiency, and covers methane oxidation rate of more than 84% within 7 days; and protects environment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a garbage landfill site covering material, comprising: mineralized waste; and    (2) a method of reduction of landfill methane emission involving setting up the landfill's covering layer including garbage landfill site covering material.
NOVELTY - Food waste processing device with a precipitate discharging unit comprises a decomposition bath (12) equipped with a decomposed product outlet (16) and a food waste inlet (14), and a stirring unit (24) placed within an agitation tank (20), which is provided within the decomposition bath. The precipitate discharging unit is provided with a microbial inhabitation unit for degrading food waste using inhabited microorganisms, and a sediment outlet set on one side of the precipitate discharging unit for discharging the precipitate accumulated on the inner bottom of the decomposition bath.    USE - Used as a food waste processing device with precipitate discharging unit.    ADVANTAGE - The device quickly discharges precipitate without accumulating at the bottom of the decomposition bath, maintains optimum condition and ensures internal processing space of the decomposition bath, has improved performance and processing efficiency, and reduces the precipitate or sludge up to 20-25 wt.%.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the front view of internal cross section of the food waste processing device with precipitate discharging unit.    Decomposition bath (12)    Inlet (14)    Outlet (16)    Agitation tank (20)    Stirring unit (24)
NOVELTY - The apparatus has drum heater that is provided in the lower unit of main portion. An accommodating chamber is provided for accommodating the food waste while the humidity sensor regularly maintains the humidity of the accommodating chamber. An agitating blade is formed around the stirring axis into the different angle at constant interval for stirring the food waste. A control unit controls the rotation of agitated motor and the stirring axis.    USE - Food waste treating apparatus.    ADVANTAGE - The food waste can be easily disposed, since the temperature sensor maintains the temperature of the inner portion of main portion. The generation of the harmful microorganism and the production of the harmful material and bad smell can be suppressed effectively. The rotation of the blower can easily eject the air while sustaining the fixed humidity of accommodating chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the food waste treating apparatus.    Side cover (150)    Front cover (170)    Control block (172)    Door (230)
NOVELTY - Preparing Kopsia pauciflora Hook.f. corynxine, comprises crushing Kopsia pauciflora Hook.f. alkaloid B dried flower, transferring into carbon dioxide supercritical extraction tank, passing liquid carbon dioxide, introducing chloroform cosolvent, extracting at 30-50?o C at a pressure of 15-30 Mpa for 1-3 hours, analyzing to obtain an extract, dissolving extract in methanol solution, transferring into alumina short column, concentrating the eluate, carrying out high speed counter-current chromatography separation, online monitoring by UV detector, vacuum extracting and drying.    USE - The method is useful for preparing Kopsia pauciflora Hook.f. corynxine (claimed).    ADVANTAGE - The method: is simple and environmentally friendly; and provides high purity product.    DETAILED DESCRIPTION - Preparing Kopsia pauciflora Hook.f. corynxine comprises (a) crushing dried flower to 20-80 meshes, transferring into carbon dioxide supercritical extraction tank, passing liquid carbon dioxide at a flow rate of 5 ml/minute/g, simultaneously introducing chloroform cosolvent at a flow rate of 1-5 ml/minute/g, extracting at 30-50?o C, at a pressure of 15-30 Mpa for 1-3 hours, and analyzing to obtain an extract, (b) dissolving the extract in methanol solution, transferring into alumina short column, collecting the eluate and concentrating, carrying out high speed counter-current chromatography separation, online monitoring by UV detector at a detection wavelength of 227 nm, vacuum extracting and drying.
NOVELTY - Preparing taurine comprises (i) using sulfur ion (S4+) compounds to adjust the pH value of taurine solution, (ii) converting ethylene oxide to sodium isethionate, (iii) separating taurine crude product before or after the introduction of ethylene oxide, and (iv) regenerating taurine by adding sodium isethionate reaction solution with ammonia.    USE - The method is useful for preparing taurine (claimed).    ADVANTAGE - The method uses sodium-base balance in the system; recycles the mother liquor to regenerate taurine; makes full use of raw materials; solves the problem of using large amount of liquid alkali with concentrated sulfuric acid in the traditional technique and high risk chemical raw material; avoids the generation of solid waste sodium sulfate; solves the problem that the mother liquor can not be concentrated repeatedly, which is not good to use, and is discharged causing environmental pollution problem; reduces the mother liquor concentration; improves the yield; and reduces the production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing taurine derivatives of formulae (RNHCH2CH2SO3H) and (RN(R')CH2CH2SO3H).    N.B.: R and R' are not defined in the claims.
NOVELTY - The apparatus has a feeding system (10) feeding wet biomass at pressure of 22.1 MPa. A reactor (32) is provided with a reaction tube and a heating device. The reaction tube includes a connection for pressurized fluid with a power system. The reaction tube is adapted to contain a bed of solid particles suspended in fluid and receive information from the power system. The heating device is adapted to heat water in presence of the bed of solid particles suspended in the fluid. The reaction tube is adjusted to adjust flow of the heating fluid in a heating jacket.    USE - Apparatus for gasification of wet biomass. Uses include but are not limited to fermentation residues, sewage sludge, sediment sludge, algae, animal manure and mixtures.    ADVANTAGE - The reaction tube is adapted to allow biomass to pass along longitudinal direction. The apparatus is environmentally friendly. The apparatus can reduce the energy supply to the gasification process to be favored. The apparatus is provided with a feeding pump that pumps biomass at low pressure into a cylinder and increases the methane content of the fluid gasification product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for gasification of wet biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus for gasification of wet biomass.    Feeding system (10)    Hydraulic pump (20)    Valves (22)    Reactor (32)    Heat exchanger (35)
NOVELTY - This utility model claims a planting pig excrement recycling treatment device, comprising a ground hog house is provided with a slope, wherein, further comprising a fermentation bed and marsh gas tank, the pigsty fermenting bed, is connected with the excrement of the excrement in hog house to ferment in the ferment bed between the fermenting bed and marsh gas tank is provided with a pipe, the excrement and fermentation enter into marsh gas tank to marsh gas produced by the first pipe, the marsh gas tank is further provided with a pipe and slag discharging system are connected with each other. This utility model claims a pig excrement recycling treatment device for feeding pig feces and generated in the process of waste to be utilized at least a waste water to the environment. With the excrement sewage is used for producing marsh gas, marsh gas generated by the use of , the use of a resource in the piggery is dependent, the external energy source.
NOVELTY - This utility model claims one kind of with auxiliary pushing mud device for suction dredge, comprising a track, a saddle, a working bridge, a driving device, a main pushing mud bucket, a pipeline system, an electric control box and an auxiliary pushing mud device, the track is set on the passage of the two sides, the air outlet of the working bridge and saddle combination under the driving of the driving device walking on the track, the electric control box is connected with the driving device of the main pushing one end of the mud bucket is fixed on the working bridge, and the other end is located on the bottom of the precipitation tank, the air outlet pipe and a silt funnel by a bolt on the main sliding mud, the auxiliary pushing mud device is set on the sedimentation tank. The utility model suction dredge with auxiliary pushing mud device has simple structure, the secondary mud bucket pushing movement of the pushing is composed of an electric control box, solves the problem that the original sedimentation tank so as to generate , a sludge anaerobic fermentation to generate marsh gas mud deposition because of a series of problems.
NOVELTY - This utility model claims a kind of containing microbiological fuel cell of organic sewage treatment device, the microbiological fuel cell comprises at least one anode, a cathode, and an ion exchange film layer applied for the composite electrode, wherein the battery further comprises a inlet and a sewage to be processed and sewage outlet, the sewage to be processed with a liquid inlet of the pushing device, which is used for controlling the flow rate of the sewage to be treated of the pushing power device is connected with the energy storage device of the microbiological fuel cell, at the same time also connected with external power supply. The device can be used for processing multiple organic sewage, has the following beneficial effects: it realizes the organic sewage processing temperature is controlled through self capacity, so as to better realize the microorganism to a conversion process, which effectively improves the output power and the COD removing effect.
NOVELTY - This utility model claims a marsh gas generating device, it solves the problem that the existing biogas generating set in marsh gas generating amount is less, the cost is high; The marsh gas generating device comprises multiple groups of marsh gas collecting device, each group of marsh gas collecting device comprises a gas collecting tube, a branch pipe, a main pipe, a spraying head and a biogas electric generator set, the gas collecting tube is set on the side wall of the through-hole, the spray head is set with a collecting tube at one end of the upper part of the collecting tube, a branch pipe, and the other end is connected with the main pipe, and the pipe with the air inlet of the biogas electric generator set. The utility model is provided with marsh gas generating rate, low cost and so on.
NOVELTY - Acai palm biomass core comprises 100% natural acai seeds.    USE - Acai palm biomass core.    ADVANTAGE - The acai palm biomass core facilitates new source of sustainable energy in a reduced cost, enables reuse of waste into a value-added product that is currently discarded as waste, burns faster, and provides longer duration of fire in a simple and cost-effective manner.
NOVELTY - Producing ethanol involves fermentation of carbohydrates from multiple byproduct feedstocks simultaneously during the same fermentation batch by application of a bacterial microbe which converts carbohydrates to ethanol.    USE - For producing ethanol (claimed) useful as renewable fuel.    ADVANTAGE - The bacterial microbe converts multiple carbohydrate types into ethanol without the addition of enzymes and without pre-treatment. The method produces industrial quantities of ethanol. Advantageously, the current method does not require sterilization of the byproduct feedstocks because the microbe used is robust and will out compete contaminating microbes. Thus, strict sterilization is not required. As a result, the method results in a significant cost savings.
NOVELTY - Producing ethanol, comprises contacting hydrogen with a feed stream comprising acetic acid and/or ethyl acetate in a reactor at a temperature greater than 225 degrees C in presence of a catalyst, under conditions effective to form ethanol or to achieve steady state ethyl acetate concentration, provided that the liquid hourly space velocity of the feed stream to the reactor is 0.2-1/hour. The catalyst comprises a precious metal and at least one active metal on a modified support. The modified support comprises support material, and a support modifier. The active metals comprise e.g. copper and iron.    USE - The process is useful for producing ethanol (claimed) which is useful e.g. in fuels, solvents, chemical feed-stocks, pharmaceutical products, cleansers, sanitizers or hydrogen transport.    ADVANTAGE - The process: utilizes hydrogenation catalyst which is highly selective to ethanol and exhibits minimized selectivity to ethyl acetate; reduces the production of undesirable by-products; and provides higher yields of ethanol.    DETAILED DESCRIPTION - Producing ethanol, comprises contacting hydrogen with a feed stream comprising acetic acid and/or ethyl acetate in a reactor at a temperature greater than 225 degrees C in the presence of a catalyst, under conditions effective to form ethanol and achieve steady state ethyl acetate concentration, provided that the liquid hourly space velocity of the feed stream to the reactor is 0.2-1/hour. The catalyst comprises a precious metal and at least one active metal on a modified support. The modified support comprises support material, and a support modifier comprising a metal comprising tungsten, molybdenum, vanadium, niobium or tantalum. The active metals comprise copper, iron, cobalt, vanadium, nickel, titanium, zinc, chromium, molybdenum, tungsten, tin, lanthanum, cerium and/or manganese.
NOVELTY - Method (M1) for hydrothermal digestion of cellulosic biomass solids, comprises: (a) providing cellulosic biomass solids in a solvent system comprising a polyol organic solvent; (b) converting at least a portion of the cellulosic biomass solids and the polyol organic solvent into a reaction product comprising a glycol; and (c) at least partially transforming the glycol into a monohydric alcohol or a higher molecular weight compound.    USE - The methods are useful for hydrothermal digestion of cellulosic biomass solids (claimed) to produce biofuel such as gasoline, diesel and jet fuels.    ADVANTAGE - The method: converts both the cellulosic biomass solids and the glycerol into glycol reaction product for subsequent processing without the need for further solvent separation, and thus it is energy efficient; utilizes the fluid flow for the distribution of the slurry catalyst in the cellulosic biomass solids, thus ensuring adequate catalyst distribution and reduce thermal gradients that may occur during hydrothermal digestion; and is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method (M2) for hydrothermal digestion of cellulosic biomass solids, comprising providing cellulosic biomass solids and a slurry catalyst in a hydrothermal digestion unit, heating the cellulosic biomass solids in the hydrothermal digestion unit in the presence of the slurry catalyst, molecular hydrogen and the solvent system, to form soluble carbohydrates, and at least partially converting the soluble carbohydrates and the glycerol into a reaction product comprising a glycol within the hydrothermal digestion unit.
NOVELTY - Converting a biomass, comprises contacting a biomass with a catalytic cracking catalyst at more than 400 degrees C in a catalytic cracking reactor to produce a product stream containing one or more cracked products, and supplying a biomass to the reactor via a feed nozzle having a feed nozzle outlet (122) located between a first section (104) and a second section (106) of the reactor and downstream of an opening of a catalyst supply pipe connected to the first section.    USE - The process is useful for converting a biomass (claimed), such as partially or fully deoxygenated pyrolysis oil, to chemicals and fuel products.    ADVANTAGE - The process is capable of effectively converting a biomass to large scale of chemicals and fuel products in a simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a catalytic cracking reactor comprising the first section; the second section having a fluid connection to and located downstream of the first section, where the second section has an inner diameter which decreases in a downstream direction; a third section (108) having a fluid connection (105) and located downstream of the second section; a catalyst supply pipe being connected to the first section for supplying a fluid catalytic cracking catalyst to the first section between a first level and a second level, where the second level is located downstream of the first level; and the feed nozzle.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a reactor.    First section (104)    Fluid connection (105)    Second section (106)    Third section (108)    Feed nozzle outlet. (122)
NOVELTY - Method for digesting cellulosic biomass solids involves providing cellulosic biomass solids in a digestion solvent; at least partially converting the cellulosic biomass solids into a phenolics liquid phase comprising lignin, an aqueous phase comprising an alcoholic component derived from the cellulosic biomass solids, and an optional light organics phase; and separating the phenolics liquid phase from the aqueous phase.    USE - For digesting cellulosic biomass solids (claimed) such as processing phenolics liquid phase comprising lignin.    ADVANTAGE - The present method is a relatively simple; provides low cost engineering solution; and reduces the energy-efficiency of the biomass conversion process.
NOVELTY - A method of harvesting hydrocarbon hydrate deposits, involves: providing a gas hydrate conversion system (100); inducing release of methane from an oceanic hydrate deposit (4); capturing the methane from a primary methane capture zone (51) and/or a secondary methane capture zone (52); and converting the methane to hydrogen and carbon.    USE - In harvesting hydrocarbon hydrate deposits, for producing hydrogen and carbon use for producing durable goods and energy (claimed).    ADVANTAGE - The method averts potentially catastrophic releases of greenhouse gases to the atmosphere; harvests gas hydrates to reduce their effects on the atmosphere; and converts the gas hydrates to usable sources of energy and durable goods.    DESCRIPTION OF DRAWING(S) - The figure shows an end view of a gas hydrate conversion system that extracts methane from gas hydrate deposits.    Floating factory (2)    Hydrate deposit (4)    Primary methane capture zone (51)    Secondary methane capture zone (52)    Gas hydrate conversion system (100)
NOVELTY - Motor vehicle comprises a motor, a fuel tank with a system for supplying fuel to the motor, a container (1) for hydrogen with a system for supplying hydrogen to the motor, an electrical system that includes a controlled-board computer and an accumulator (5). The motor vehicle is additionally equipped with a battery (4) of photoelectric elements arranged on the outer surface of the motor vehicle and are connected to the electrical system; and a system for water electrolysis and for pumping the hydrogen obtained in it into the existing container for hydrogen connected to the electrical system.    USE - Used as a motor vehicle.    ADVANTAGE - The motor vehicle comprises the system for water electrolysis, which makes it possible to use the solar energy for the production of alternative fuel (hydrogen) and to use the fuel for the movement, which will reduce fuel consumption. The use of hydrogen as a fuel improves the ecology of the automobile, where only water is formed during the combustion of hydrogen without harmful emissions.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the motor vehicle.    Container for hydrogen (1)    Battery (4)    Accumulator (5)    Electrolyzer (8)    Compressor (13)
NOVELTY - Method (M1) for capturing carbon dioxide, comprises: (a) providing a cellulosic material which carries an amino compound; and (b) contacting the cellulosic material with a composition comprising carbon dioxide, where a portion of the heat energy produced in step (b) is captured.    USE - The method is useful for capturing carbon dioxide onto a material, which is useful for storing carbon dioxide, as a fertilizer, and for transporting carbon dioxide (all claimed).    ADVANTAGE - The method: results in at least 10 % on mass of fiber of uptake of carbon dioxide on the cellulosic material (claimed); is highly efficient and significantly improves the efficiency of a power station; utilizes natural fibers, thus it is environmentally-friendly; can be used to directly capture carbon dioxide from the flue gases of a power station; and provides material that is weatherproof.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a material obtained by the method (M1);    (2) a method (M2) for capturing carbon dioxide, comprising the steps (a) and (b) as above per se, and using a portion of the heat energy produced in step (b) to heat fibers previously treated according to step (a) and step (b); and    (3) a method (M3) for capturing carbon dioxide, comprising the steps (a) and (b) as above per se, optionally transporting the material obtained following step (b), and heating the cellulosic material, thus releasing carbon dioxide from the material.
NOVELTY - An antiviral agent-containing thin paper product has primary base paper layer, bactericide film layer, hydrophilic nonwoven fabric layer, antiviral agent-containing film layer, and second base paper layer, in order. The bactericide film layer is obtained by film-forming water soluble carrier, and garlic extract located in film-forming water soluble carrier. The antiviral agent-containing film layer comprises film-forming water-soluble carrier, and antiviral agent located in film-forming water soluble carrier.    USE - Antiviral agent-containing thin paper product (claimed).    ADVANTAGE - The antiviral agent-containing thin paper product has excellent water absorption property and antibacterial property, and improves sanitary environment safety.
NOVELTY - Method of splitting S-configuration pregabalin involves mixing racemic pregabalin with benzene sulfonyl amino-D-phenylglycine or amino-benzene sulfonyl-D-phenylglycine, adding oxypricin, resolving in alcohol solution containing water, separating p-methyl phenyl benzene sulfonyl amino-D-phenylglycine or amino-benzene sulfonyl-D-phenylglycine and S-configuration chiral pregabalin salt complex, suspending complex of p-methylphenyl benzene sulfonyl amino-D-phenylglycine or benzene sulfonyl-D-phenylglycine and S-configuration chiral salt complex in water, regulating pH and depolymerizing.    USE - Method of splitting S-configuration pregabalin (claimed).    ADVANTAGE - The method enables efficient splitting of S-configuration pregabalin with high resolution, excellent productivity, and reduced environmental pollution, by simple method.    DETAILED DESCRIPTION - Method of splitting S-configuration pregabalin involves mixing racemic pregabalin with benzene sulfonyl amino-D-phenylglycine or amino-benzene sulfonyl-D-phenylglycine as resolving agent, adding oxypricin, resolving in alcohol solution containing water, separating p-methyl phenyl benzene sulfonyl amino-D-phenylglycine or amino-benzene sulfonyl-D-phenylglycine and S-configuration chiral pregabalin salt complex, suspending complex of p-methylphenyl benzene sulfonyl amino-D-phenylglycine or benzene sulfonyl-D-phenylglycine and S-configuration chiral salt complex in water, regulating pH and depolymerizing.
NOVELTY - This utility new type provide a one garden garbage treatment, comprising a treatment tank, processing tank main body outer layer is non-porous layer in the treatment tank main body porous layer treatment tank main body upper part is provided with multiple supporting beam, treatment tank main body is set with several water discharging pipe. This utility new type has the advantages and positive effects of reasonable design, low cost, easy operation, easy management, and convenient to be spread and applied.
NOVELTY - This utility new type relates to a the treating sewage using one of putting to lake in germ cell of gene engineering of engineering bacteria dispenser. Comprising a shell, a water pump, a propeller drive,, a drain pipe and a propeller, a water pump is set in the shell, the inlet and outlet of the water pump comprises a water pump, a water pump inlet is connected with the shell of water pumping pipe is connected with the water pump outlet and the shell of pipe, a screw driver is set in the shell, through the transmission pole and the shell of propeller. This utility new type of engineering bacteria for directly extracting engineering bacteria liquid and adding in lake from the container, and it does not need human turning container through liquid pouring process, at the same time stirring for water process of adding enzyme, the engineering bacteria to the whole area, fast dispersing speed up water body treatment process.
NOVELTY - This utility new type relates to one for a production system of pure cypress biomass particle fuel, comprising a saw powder storage hopper, a belt conveying device, a roller sieving machine, a lifter, a material distribution hopper, a closed sakei, air flow rotary drying machine, cooling and absorbing device, a central dust collecting distribution hopper, a granulator, screening device and product particles. This utility new type produce of dust, high moulding rate and high yield, for device of small abrasion.
NOVELTY - This utility new type relates to a large-scale one by microalgae to purify the livestock and poultry cultivation waste water treatment of production device, wherein the system comprises a livestock and poultry cultivation of front processing system, system, photo-biological reactor system, the algae solution concentration online detect system, collecting system, a water circulating system, a temperature control system, a light system. This utility new type large-scale livestock and poultry cultivation in the produce of the modulated later cultivation waste water micro-algae, which greatly reduces the culture microalgae of production cost and of nitrogen phosphorus in waste liquid as micro-algae culture of nutrient substance, each index in the waste water of purifying sewage improving water quality.
NOVELTY - This utility new type relates to a hydraulic one-type automatic-circulation biogas tank, feeding port of one side is provided with a sand, the other side of the discharge is provided with controllable material outlet and ladder discharge hole, the discharge hole of ladder bottom one side is equipped with sewage pump, in part of tank body is provided with arch plate, two end of arch plate are respectively installed on the flexible base, telescopic base seal is installed on the beam, a base beam and post support fixing. By the drain pump in the cleaning bottom sludge, using movement of flexible base, the water pressure of the water pressure by the telescopic base of two ends of arch plate process, prolongs the service life of arch plate, prolongs the service life of the long 5 times, the device operation safety and reliability, a large flow amount continuous feeding, continuous feeding, used for a long time without the characteristics of large discharge, which is suitable for taking the large farm building, school, and factory and so on.
NOVELTY - This utility new type relates to a novel hydraulic-type automatic-circulation biogas tank is set with arch in the part of the tank body, the two end of arch plate are respectively installed on the flexible base, the flexible base seal is installed on the beam, a base beam and post support fixing. Using moving of extension base, the water pressure of the water pressure by the telescopic base of two ends of arch plate process, prolongs the service life of arch plate, prolongs the service life of the long 5 times, the device operation safety and reliable, using the marsh gas tank by movement formed by fermenting biogas automatic circulation, pool bottom stirring and the fermentation room for abiligy, futher bottom solves the problem that the pool surface shell, a tank of the strain, the raw material distribution uniformity, large flow amount continuous feeding, continuous feeding, used for a long time without the characteristics of large discharge, which is suitable for taking the large farm building, school, and factory and so on.
NOVELTY - A spiral one residue from the biogas fermentation tank, comprising a coaxial set of outer tank and inner tank body, the tank body of the outer wall and of the inner wall of the outer tank body is provided with a spiral flow guide plate, the top end of the outer tank body is set with marsh gas output tube, the positon of the top end of the outer tank body is set with biogas liquid overflow tube, the bottom of the outer tank body is set with a feeding port, the feeding port is connected with the feeding pump, the outer of upper half part of the tank body and the outer tank body of the lower half part of middle part positon, respectively along the circumferential direction is provided with a multi-residue discharging pipeline, biogas discharge pipeline is connected with the inner cavity of the tank body and the slag sedimentation barrel of inner cavity, the top end of sedimentation barrel residue sedimentation barrel are respectively provided with return gas tube cavity of outer tank body is provided with a residue discharge valve opening at the bottom of biogas residue sedimentation barrel. This utility new type has simple structure, safety and reliable to realize smoothly finish the generating of biogas fermentation at the same time, it can successfully of the biogas residue of automatically cleaning, so as to realize the production of marsh gas circulation.
NOVELTY - This utility new type claims a intestinal one marsh gas generator system matched using biogas material gradually lifting device, belonging to the biogas slurry conveyer device field, comprising a sewage collector and connected end to end of multi-stage sewage lifting unit, each of the sewage lifting unit comprises a conveying gas tube, sewage storing tank, a water pump, a lifting tube, a gravity tank, gas conveying tube and the sewage pre-stored tank, water pump is set in the sewage tank and pre-stored by the lifting tube and the gravity tank, gravity tank and the gas conveying tube of the next sewage lifting unit. This utility new type can make the biogas terrain at gradually from low to high terrain, the slope, forest, terrace and so on , it does not need high pressure pump, a low pressure pump, energy-saving and environment-friendly, low noise.
NOVELTY - Can be measured discharge positon of CSTR reactor, relating to CSTR reactor field. This utility new type to solve the problem that the existing large-middle biogas engineering CSTR reactor discharge positon of hard to determine. The reactor comprises a multi-root feeding and discharging tube, the upper CSTR anaerobic fermentation tank outer wall is equipped with multi-root height different of inlet and outlet tube, and multi-inlet tube and the discharging CSTR anaerobic fermentation tank is connected with, one end the hopper and the feeding tube, and the other end of the feeding tube of the feeding and discharging tube. This utility new type of anaerobic fermentation in a biogas engineering.
NOVELTY - The new type claims a one biogas raw material feeding system, a methane raw material feeding system of rack, a storage bin, a storage tank, an air storage tank, an air compressor and control system is composed of storage hopper, a storage tank, an air storage tank, an air compressor and control system are installed on the rack up between the storage hopper and the storage tank by the conveying tube, and the air storage tank is respectively connected with the air compressor, a storage tank through the air tube, and the upper storage tank exhaust port, another intelligent electronic level meter is provided at least one of control valve, upper manhole and feeding port, the feeding port is further feeding tube, a material conveying tube, an air tube, a feeding tube and feeding tube, an electronic liquid level meter and control valve are connected with the control system electrically connecting. The new type has stable structure, high degree of automation, and feeding and stable uniformity of characteristic, which greatly improves the feeding of operability, reduces the labour intensity of manual operation, and greatly expands the raw material concentration range, so as to effectively avoid the blocking phenomenon of feeding pipeline, helpful for marsh gas of continuously and stably.
NOVELTY - Fertilizing banana involves: before planting for 1-3 months, making planting base fertilizer containing animal manure, stems and leaves, and fertilizer and pile up together, and 5-15 kg planting before 2-7 days; after planting, using manure, fertilizer, and phosphate fertilizer and applying fertilizer seedlings at a distance of 0.1-0.5 meters of 5-10 kg per fertilizer per plant with twice fertilization interval for 1-2 months; evacuating the bud with banana, rapidly agent, potassium dihydrogen phosphate spray, water and spraying for specific time.    USE - For fertilizing banana (claimed).    ADVANTAGE - The method provides soil containing quartz sand in the multi-, soil, water and fertilizer-keeping, and soil saves planting cost, comprehensive utilization and valid.    DETAILED DESCRIPTION - Fertilizing banana involves: before planting for 1-3 months, making planting base fertilizer containing 20-30 pts. wt. animal manure, 40-60 pts. wt. stems and leaves, and 1-5 pts. wt. fertilizer and pile up together, and 5-15 kg planting before 2-7 days; after planting, using 60-85 pts. wt. manure, 5-12 pts. wt. fertilizer, and 1-3 pts. wt. phosphate fertilizer and applying fertilizer seedlings at a distance of 0.1-0.5 meters of 5-10 kg per fertilizer per plant with twice fertilization interval for 1-2 months; evacuating the bud with 50-60 pts. wt. banana, 10-20 pts. wt. rapidly agent, 0.5-1 pts. wt. potassium dihydrogen phosphate spray, 80-90 pts. wt. water and spraying to configuration of liquid fertilizer for plant spraying, of 250-300 kg/ mu between two adjacent spraying of interval time of 7-15 days, and continuously spraying for 3-5 times.
NOVELTY - Vegetable soil-less culture medium comprises organic matter, beneficial microorganism and trace element. The organic matter comprises 30 wt.% of plant straw, mushroom slag, marsh, saw milling and hull, 20 wt.% of chicken manure, 25 wt.% of pig manure, 25 wt.% of fine sand or fine coal slag. The trace element is 0.1-1.2 kg of nitrogen, 0.5-1.3 kg of phosphorus, 0.8-1.6 kg of potassium, 0.01-0.04 kg of copper, 0.03-0.07 kg of boron, 0.02-0.06 kg of calcium, 0.02-0.05 kg of magnesium, 0.02-0.08 of sulfur, 0.06-1.4 kg of manganese, 0.05-0.09 kg of zinc, 0.06-1 of iron, 0.02-0.07 kg of chlorine.    USE - Vegetable soil-less culture medium.    ADVANTAGE - The vegetable soil-less culture medium is eco-friendly, reduces farm chemical, shortens production time and has less energy consumption and high yield.    DETAILED DESCRIPTION - Vegetable soil-less culture medium comprises organic matter, beneficial microorganism and trace element. The organic matter comprises 30 wt.% of plant straw, mushroom slag, marsh, saw milling and hull, 20 wt.% of chicken manure, 25 wt.% of pig manure, 25 wt.% of fine sand or fine coal slag. The mass ratio of beneficial microorganism and organic matter is 1-1.5 kg. The trace element is 0.1-1.2 kg of nitrogen, 0.5-1.3 kg of phosphorus, 0.8-1.6 kg of potassium, 0.01-0.04 kg of copper, 0.03-0.07 kg of boron, 0.02-0.06 kg of calcium, 0.02-0.05 kg of magnesium, 0.02-0.08 of sulfur, 0.06-1.4 kg of manganese, 0.05-0.09 kg of zinc, 0.06-1 of iron, 0.02-0.07 kg of chlorine. An INDEPENDENT CLAIM is included for producing vegetable soil-less culture medium comprising uniformly mixing plant straw, sawdust, marsh gas, saw milling, hull, chicken manure and dairy manure, uniformly stirring the mixed material at humidity of 65-80%, then adding trace element and beneficial microorganisms, piling and fermenting for 30-45 days, then adding fine coal slag or fine sand.
NOVELTY - Fertilizer composition comprises (in wt.%): wheat bran (2-3), pig manure (3-5), husk (15-17), sugarcane filtered product (5-6), orange flower water (45-47), tobacco powder (1-2), maifanite (10-15), inoculant bacteria (4-8), Rehmannia rhizome (1-2), nitrogen, phosphorus and potassium strain (1-2) and bentonite (3-5).    USE - Fertilizer composition.    ADVANTAGE - The fertilizer composition is easy to use, has prolonged shelf life, and eliminates soil compaction and increases soil disease suppression. The fertilizer composition is prepared by simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer composition, which involves:    (A) feeding wheat bran, pig manure, husk, sugarcane filtered product, orange flower water, tobacco powder, maifanite, inoculant bacteria, Rehmannia rhizome, nitrogen, phosphorus and potassium strain and bentonite in a storage tank, and then stirring and mixing them uniformly at speed of 45-50 revolutions per minute to obtain mixed material;    (B) placing the mixed material in a fermentation tank, and then heating at 25 degrees C and increasing temperature to 70oC;    (C) sealing the fermentation tank for 10 days, centrifuging to remove supernatant to obtain concentrated product;    (D) sterilizing product at 120-150 degrees C for 2-3 hours, and then performing steam-granulator process to obtain granules; and    (E) drying the granules in a box at 150-200 degrees C for 15-30 minutes to obtain the desired product.
NOVELTY - Fertilizer composition comprises (in pts.wt.): amino acid solution (100), copper sulfate (30), zinc sulfate (1-50), magnesium sulfate (1-60), ferrous sulfate (1-30), manganese sulfate (1-20), ammonium formate (1-20), sodium selenite (1-20), Borax (RTM: Sodium tetraborate decahydrate) (1-60), sodium nitrate (0.01-5), sodium citrate (1-30), metasilicate salt (1-30) and urea (1-20).    USE - Fertilizer composition used for preventing wilt fungal disease of cotton caused by Fusarium oxysporum.    ADVANTAGE - The fertilizer composition prevents plants from cold damage and hail, and is rich in silicone, glutathione peroxidase, superoxide dismutase and catalase content.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for preparing fertilizer composition by adding amino acid solution in a stillage, mixing copper sulfate, zinc sulfate, magnesium sulfate, ferrous sulfate, manganese sulfate, ammonium sulfate, sodium selenite, Borax, sodium nitrate, sodium silicate and urea with amino acid solution to obtain mixture, heating mixture at 80-95 degrees C for 30-45 hours and filtering the obtained solution to obtain desired product; and    (2) a method for agricultural ecological cycle development involves mixing chicken meat, egg, feather product and waste cultivation with earthworm excretion waste to obtain mixture, mixing obtained mixture with water, sulfuric acid (98% and 85%), phosphoric acid, sodium sulfide and calcium hydroxide to obtain mixture, adding copper sulfate, zinc sulfate, magnesium sulfate, ferrous sulfate, manganese sulfate, ammonium sulfate, sodium selenite, Borax, sodium nitrophenolate, citrate, silicate and urea to obtain mixture for fertilizing the crops and farmland.
NOVELTY - Manufacturing fertilizer involves weighing (in pts.wt.): chicken manure (35-45), dairy manure (20-30), pig manure (15-25), straw powder (10-15), rice (5-10), quicklime (1-3), cotton seed hull (0.5-2) and water content (60-70%) and then mixing to obtain mixture. The obtained mixture is stirred 2-3 times a day and then mixture is fermented for 25-30 days, where controlling fermenting device temperature is 60-700 degrees C. The pile of fertilizer is continued to ferment for another 25-30 days to obtain the product.    USE - Method for manufacturing fertilizer (claimed).
NOVELTY - Culture medium comprises sunflower disk debris, sunflower stem debris, sunflower hulls, wheat bran, sunflower seed meal, gypsum powder and lime powder in mass ratio of 22-28:16-20:30-40:15:5:1:1.    USE - Culture medium for cultivating Tremella fuciformis (claimed).    ADVANTAGE - The culture medium is rich in nutrition and increases yield of fungus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing culture medium for cultivating Tremella fuciformis, which involves:    (A) drying raw materials using ultraviolet light for l-2 days to kill bacteria;    (B) pre-wetting dried sunflower disk debris, sunflower stem debris and sunflower hulls using 1% of lime aqueous solution;    (C) piling high wet material into ladder-shaped stack, where each stack contains 300-500kg of dry material;    (D) sticking obtained stack on stick (10-15cm) and then covering it with grass for fermentation;    (E) turning stick twice at interval of 2,2,1 days for 5 days;    (F) adding gypsum powder, wheat bran and sunflower seed meal to stack material and then adding water to rehydrate stack, where water content of obtained product is 63-65wt.%;    (G) packaging obtained product into high pressure polyethylene bag cylinder, where each bag contains 1.2-1.3kg of wet material; and    (H) sterilizing bag material at 100 degrees C for 10-12 hours and then cooling sterilized product to 25 degrees C to obtain desired product.
NOVELTY - Liquid fertilizer composite material preparation involves separating biogas slurry and liquid obtained from anaerobic fermentation by using solid-liquid separation method. Humic acid is used as flocculating agent for liquid purification process. Activated carbon is used to remove odorant substance from liquid. The obtained liquid is sterilized thermally. Temperature of the obtained material is reduced to room temperature, and then organic material and inorganic are added and mixed. Ethylenediaminetetraacetic acid and polysorbate-80 are added and mixed uniformly to obtain finished product.    USE - Method for preparing liquid fertilizer composite material (claimed).    ADVANTAGE - The method enables to produce product that is rapidly dissolved in water, easily absorbed by crops, and easy in storage, transportation and application.
NOVELTY - Producing fertilizer involves utilizing (in pts.wt.): pine bran (30-60), plant ash (10-20), peanut (8-15), bat dung (8-15), urea (3-5), calcium and magnesium phosphate fertilizer (2-5), ferrous sulfate (1-2) and fermented biogas residue (10-20). Raw materials are mixed and heated at 100-110 degrees C, and then heated product is treated with steam to obtain product. The product is fermented by utilizing a marsh gas tank in which water (50-80%) is added, and then sealed by a pithos.    USE - Method for producing fertilizer used for plantingDendrobium candidum (claimed).    DETAILED DESCRIPTION - Producing fertilizer involves utilizing (in pts.wt.): pine bran (30-60), plant ash (10-20), peanut (8-15), bat dung (8-15), urea (3-5), calcium and magnesium phosphate fertilizer (2-5), ferrous sulfate (1-2) and fermented biogas residue (10-20). Raw materials are mixed and heated at 100-110 degrees C, and then heated product is treated with steam to obtain product. The product is fermented by utilizing a marsh gas tank in which water (50-80%) is added, and then sealed by a pithos. Fermentation process is carried out for 30-60 days, and then slow releasing agent such as aqueous solution of polyvinyl alcohol is added in the fermented product in ratio (5-8:1). The fermented product is turned into granules by utilizing a granulator.
NOVELTY - Production of protease comprises condensing Enterococcus faecium, Lactobacillus acidophilus, Bacillus subtilis, and Bacillus natto; fermenting food processing leftover, and strains, crushing into paste when pH reaches 3-5, continuously fermenting to obtain upper layer oil, middle layer mucus enzyme preparation, and lower layer paste; mixing dry material and enzyme preparation at a ratio of 1:1, fermenting at 38 degrees C for 48 hours, drying at 50 degrees C, crushing into 60-mesh powder, and packing.    USE - Production of protease used for treating livestock manure for preparing nutrient soil (claimed).    ADVANTAGE - The livestock manure has no malodor, contains probiotics, and degrades quickly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for enzyme treatment of livestock manure comprising mixing protease with water, fermenting at room temperature for 12-24 hours, and feeding livestock.
NOVELTY - Purifying floating leaved plant vegetation using wetland system, comprises introducing sewage into a tank, primary filtering sewage through filter screen, removing sewage in water and then entering into floating island planting area and interlaced area of turf planting area, and secondary filtering and purifying coral sand.    USE - The method is useful for purifying floating leaved plant vegetation (claimed).    ADVANTAGE - The method is capable of conveniently and economically purifying the floating leaved plant vegetation in an eco-friendly manner with improved water quality and high efficiency and stability.
NOVELTY - Fertilizing low yielding double cropping field in central China, involves (a) cutting fresh rice straw, and scattering the rice straw uniformly on the field, (b) dividing the rice straw for early rice stage and late rice stage, mixing rice straw and nitrogenous fertilizer (for summer early rice period), scattering the obtained mixture on field, mixing rice straw and nitrogenous fertilizer (for winter late rice period), and applying mixture on the field, and (c) plowing land with rotary tillage and mixing the soil, and maintaining humidity.    USE - The method is useful for fertilizing low yielding double cropping field in central China (claimed).    DETAILED DESCRIPTION - Method of fertilizing low yielding double cropping field in central China, involves (a) cutting fresh rice straw using harvester directly from the field, where the length of straw is 3-5 cm, and scattering the rice straw uniformly on the field at the amount of 180-220 kg dry weight/acre, (b) dividing the rice straw for early rice stage and late rice stage, adjusting carbon and nitrogen (C/N) ratio in the field, mixing rice straw and nitrogenous fertilizer (for summer early rice period), scattering the obtained mixture on field in the amount of 1.9-2.1 kg/acre, adjusting carbon and nitrogen (C/N) ratio in the field to 25:1, mixing rice straw and nitrogenous fertilizer (for winter late rice period), applying obtained mixture on the field, adjusting carbon and nitrogen (C/N) ratio in the field to 25:1, and (c) plowing land with rotary tillage and fully mixing the soil, maintain plowing depth at 15-20 cm, and maintaining proper humidity in soil for next rice transplanting, and specifically maintaining field moisture content of early rice period at 90-100%, and late rice period at 35-45%.
NOVELTY - Aquaculture sewage and solid waste composting method, involves (a) collecting sewage in a closed sewage tank and solid waste in sewage pool near composting plant, (b) pumping the sewage and solid waste into composting system, (c) adjusting solid waste content in the composting system, performing aerobic composting process, pumping sewage pool to the composting tank, and adding auxiliary materials, and (d) aerating compost, discharging gas and dust generated in the tank through draught fan and deodorizing the compost.    USE - As aquaculture sewage and solid waste composting method (claimed).    ADVANTAGE - The method reduces sewage treatment pressure.    DETAILED DESCRIPTION - Aquaculture sewage and solid waste composting method, involves (a) collecting sewage in a closed sewage tank and solid waste in sewage pool near composting plant through an underground pipe, (b) pumping the sewage and solid waste into composting system through water pump, (c) adjusting solid waste content in the composting system, maintaining carbon and nitrogen ratio at 25-30:1 and moisture content at 50-60%, performing aerobic composting process, pumping sewage pool to the composting tank, and adding auxiliary materials through the slot at the top, and (d) aerating compost in bottom port of aeration tank, discharging gas and dust generated in the tank through draught fan and deodorizing the compost.
NOVELTY - The method involves providing a charging device having a charging steel pipe (1), an inflating pipe (2) and an air pump (3) for monitoring of a pressure gauge (4). A rear end of the charging steel pipe is inserted in a middle portion of a fermentation stack, when the inflation pressure for stop charging is set for 3 to 10 minutes. The charging time is set to directionally proportional to material pile volume.    USE - Ventilation method of organic fertilizer.    ADVANTAGE - The production floor space for organic fertilizer can be reduced, and the large scale production of organic fertilizer can be realized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a large-scale production method for organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the charging device.    Charging steel pipe (1)    Inflating pipe (2)    Air pump (3)    Pressure gauge (4)    Gas filled switch valve (5)
NOVELTY - The device has a feeding port, a storage unit, a discharge hole, a rotating shaft (5), and a wheel (4). The storage unit is configured in a barrel-shape, and an upper feeding port is installed on an upper portion of storage unit. One end of the storage unit is provided with a discharging port. The internal surface of the storage unit is provided with the rotating shaft, and the wheel is installed on the upper portion of the rotating shaft.    USE - Organic fertilizer fermenting device.    ADVANTAGE - The structure of the organic fertilizer fermenting device is simple. The fermentation temperature can be maintained effectively. The labor cost can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the organic fertilizer fermenting device.    Wheel (4)    Rotating shaft (5)
NOVELTY - Biological organic fertilizer comprises 10-30 pts. wt. bamboo charcoal powder, 15-30 pts. wt. bamboo powder, 8-15 pts. wt. soybean, 30-50 pts. wt. organic yeast material, and 0.2-1 pts. wt. biological strain. The fertilizer is in the form of powder or granular.    USE - As biological organic fertilizer.    ADVANTAGE - The fertilizer is environmentally-friendly, is highly nutritious, leaves no chemical residue, absorbs soil heavy metal and pesticide residue, improves soil environment, prevents soil hardening, and improves quality of crop.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the biological organic fertilizer, which involves (a) selecting bamboo, cutting and crushing bamboo, naturally or artificially drying the bamboo, performing high temperature carbonization, and cooling the carbonized bamboo to obtain bamboo charcoal powder, (b) selecting, cutting and crushing the bamboo, and naturally or artificially drying the crushed bamboo to obtain bamboo powder, (c) mixing the bamboo charcoal powder, bamboo powder, soybean, organic yeast material and biological strain using agitator to obtain powdery fertilizer, or mixing the above-mentioned components and pelletizing the mixture using pelletizer to obtain granular fertilizer.
NOVELTY - An acetylglucosamine imidazole-4,5-trione (I), is new.    USE - New acetylglucosamine imidazole-4,5-trione is used for inhibiting bacteria e.g. Escherichia coli, Staphylococcus aureus and Bacillus subtilis (all claimed).    ADVANTAGE - The acetylglucosamine imidazole-4,5-trione has excellent antibacterial property, and is economically prepared by simple and environmentally-friendly process.    DETAILED DESCRIPTION - An acetylglucosamine imidazole-4,5-trione of formula (I), is new.    R=C6H5-, 4-ClC6H4-, 3-ClC6H4-, 4-BrC6H4-, 4-FC6H4-, 2,4-di-ClC6H3-, 3-Cl-4-FC6H3-, 4-CH3C6H4-, 3-CH3C6H4-, 2-CH3C6H4-, 4-CH3OC6H4-, 3-CH3OC6H4-, 2-CH3OC6H4-, 3,4,5-tri-CH3OC6H2-, 2,5-di-CH3OC6H3-, 4-OCH2CH3C6H4-, 3-Cl-4-CH3C6H3-, C10H7-, HOCH2CH2-, or C6H5CH2-.    An INDEPENDENT CLAIM is included for synthesis of acetylglucosamine imidazole-4,5-trione (I).
NOVELTY - A restored polluted soil conditioning agent comprises 8-15 pts. wt., preferably 14-15 pts. wt. calcium superphosphate, 18-23 pts. wt., preferably 18-20 pts. wt. calcium-magnesia phosphate fertilizer, 55-65 pts. wt., preferably 55-60 pts. wt. organic material, 5.5-6.5 pts. wt., preferably 5.5-6 pts. wt. microbial fertilizer, 2.5-3.5 pts. wt., preferably 2.5-3 pts. wt. tillage fertilizer, 0.3-0.5 pts. wt., preferably 0.3-0.4 pts. wt. composite fertilizer and 0-0.5 pts. wt., preferably 0.3-0.4 pts. wt. water retention agent.    USE - Restored polluted soil conditioning agent (claimed).    ADVANTAGE - The restored polluted soil conditioning agent is efficiently prepared with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of restored polluted soil conditioning agent.
NOVELTY - 4-Androstene-3,17-dione preparation involves inoculating fermentation strain into a liquid phase culture medium. The preparation is maintained at set temperature and controlled pH value, and then plant phytosterin is added and stirred.    USE - Method for preparing 4-androstene-3,17-dione (claimed).    ADVANTAGE - The method enables preparation of 4-androstene-3,17-dione in a simple, eco-friendly manner with high conversion rate, and is suitable for industrial production.
NOVELTY - Biofertilizer comprises 65-80 wt.% humic acid, 1-4 wt.% effective microorganisms (EM) bacteria, 5-15 wt.% nitrogen fertilizer, 5-11 wt.% phosphate fertilizer and 5-11 wt.% potash fertilizer.    USE - The biofertilizer is useful for reducing soil salinity (claimed).    ADVANTAGE - The biofertilizer reduces pH by 0.8 in a year and thus makes the soil pH normal by using the biofertilizer for three consecutive years and improves the survival of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for Method for preparing the fertilizer which involves (a) fermenting by mixing humic acid with EM bacteria, stirring at 20-30 degrees C for 72-96 hours until the number of bacteria/g of the mixture is not less than 0.2 hundred million to obtain fermented material, (b) adding nitrogen, phosphate and potash fertilizers to the material obtained in step (a) and mixing to obtain product.
NOVELTY - A biodegradable organochloride hybrid membrane comprises iron-noble metal nanoparticle, polyacrylic acid microgel or microsphere, and polyvinylidene fluoride (PVDF).    USE - Biodegradable organochloride hybrid membrane used for dechlorinating chloroacetic acid, dichlorophenol trichloroethylene, tetrachloromethane and polychlorinated biphenyl.    ADVANTAGE - The convenient pH-responsive hybrid membrane has high catalytic activity, and good reusability. Its preparation is simple and low-cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biodegradable organochloride hybrid membrane comprising:    (A) taking 8 g acrylic acid, 0.1 g N,N'-methylenebisacrylamide and 0.2 g potassium persulfate, dissolving in 100 mL absolute ethanol, and reacting at 80 degrees C for 8 hours in nitrogen;    (B) taking 1.0 g acrylic acid, 1.0 g ethylene glycol dimethacrylate and 0.04 g azobisisobutyronitrile, dissolving in 80 mL acetonitrile, reacting at 83 degrees C for 1.5 hours, centrifuging, settling, and vacuum-drying;    (C) taking PVDF powder, adding N,N-dimethylformamide, dispersing, vacuum degassing, and casting;    (D) pouring on glass plate, scraping, soaking in distilled water, and solidifying for 12 hours;    (E) soaking in 0.1-1 mol/L sodium hydroxide for 4 hours, soaking in distilled water for 2 hours, soaking in 0.01-10 mol/L ferrous chloride for 4-12 hours, and washing; and    (F) reducing in 1.5 g/L sodium borohydride for 30 minutes, washing with oxygen-free distilled water, soaking in 5-30 mmol/L noble metal salt ethanol solution, reacting for 2 hours, washing, and removing impurities.
NOVELTY - The method involves performing waste fermentation gas purifying unit washing process at temperature of about 25-40 degrees centigrade. Microorganism microbial inoculum is filled in a porous organic carrier and a box body. The box body is divided into multiple layers. Multi-stage series municipal rubbish fermentation gas purification operation is performed. The microorganism microbial inoculum is formed as nitrobacteria and thiobacillus. The porous organic carrier is formed as rice bran, dry bark, hay and fiber. Height of a tellurium (Te) layer is about 0.15-25 m.    USE - Multi-stage series municipal rubbish fermentation gas purifying method.    ADVANTAGE - The method enables avoiding porous organic carrier collapsing phenomenon under deterioration air condition, improving malodorous gas purifying efficiency and avoiding generation of municipal rubbish fermentation gas smell.
NOVELTY - The device has a washing air recycling unit provided with a liquid connecting tube that is connected with a bottom part of an air washing tower. The air washing tower is connected with an air floatation tower by a circulating pump. A top part of the air floatation tower is connected with an exhaust port. A rear part of the exhaust port is connected with a bioreactor by a pipeline. A liquid distributor is provided with a waste gas inlet device. A top part of a filler part is fixed with the exhaust port. The bioreactor is formed as a bio-filter, a bio-scrubber and/or biological trickling filter.    USE - Integrated organic exhaust gas processing device.    ADVANTAGE - The device is simple in structure, and improves processing capacity and effectively realizes recycling process and organic waste gas processing operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an integrated organic exhaust gas processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an integrated organic exhaust gas processing device.
NOVELTY - This utility new type claims a one town domestic sewage filter pool, one layer is set at the bottom of filter tank, a stone paving anti-seepage film upper the said gravel, one layer of cobblestone A is set up on the said anti-seepage film, uniformity is paved the collector pipe in said upper cobble A, is provided with a through hole on the said upper collecting tube wall, paving one pebble B up the said layer, paving one layer sand up the said pebble B in the sand layer is paved with a water replenishing tube is provided with a through hole in a water replenishing tube upper tube wall. Sand in the surface layer, according to processing contamination of different planting different variety of purification plant, by co-action of the substrate, the quality of purification, for BOD in sewage, COD, TSS, TP, TN, algae and so on has obvious removal efficiency of fluid and structure of filter tank form of good filtering, compact structure, high filtering efficiency, and garden greening is combined with the upper flange.
NOVELTY - A fixing bed microorganism carrier contains carrier main body (1) containing mesh (3) cylinder which is composed of cylindrical wire (2) formed through weaving in which cylindrical wires are uniformly distributed with burr on outer surface.    USE - A fixing bed microorganism carrier for sewage treatment (claimed).    ADVANTAGE - Product provides excellent growth environment and has large water impact load for microorganisms and has good treatment effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a fixing bed microorganism carrier.    Carrier main body (1)    Cylindrical wire (2)    Mesh (3)
NOVELTY - An unpowered domestic sewage is treated by hydrolyzing water insoluble macromolecular pollutants in water soluble small molecular substance, producing organic acid, fermenting methane, degrading small molecular substance, organic acid, water, and carbon dioxide, producing methane gas, removing insoluble impurities precipitate, absorbing by biomembrane activity and/or aerobic/anaerobic biodegradable organic matter, filtering bioactive material to obtain filtrate, fully contacting with oxygen, oxidizing organic matter, and collecting oxidized and degraded filtrate.    USE - Treatment of unpowered domestic sewage (claimed).    ADVANTAGE - Treatment process does not need external power and has reduced solid impurities, prevented clogging of device, purified domestic sewage, and low energy consumption.    DETAILED DESCRIPTION - An unpowered domestic sewage is treated by hydrolyzing water insoluble macromolecular pollutants in water soluble small molecular substance, producing organic acid, fermenting methane, degrading small molecular substance, organic acid, water, and carbon dioxide, producing methane gas, removing insoluble impurities precipitate, absorbing by biomembrane activity and/or aerobic/anaerobic biodegradable organic matter, filtering bioactive material to obtain filtrate, fully contacting with oxygen, oxidizing organic matter, and collecting oxidized and degraded filtrate or collecting oxidized, degraded, and disinfected filtrate.
NOVELTY - Preparation of organic fertilizer comprises fermenting traditional Chinese medicine residue, western medicine residue and food residue.    USE - Method for preparing organic fertilizer (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the fermenting device comprising fermentation tank, ventilation pipe, biofilter and draft fan.
NOVELTY - The system has a fermentation tank (1) and a raw material circulating system (29). Fermentation devices are respectively located on fermentation tank having an exhaust port (4) connected with a marsh gas circulating system (28). The fermentation tank is provided with a sewage port (5) and a slag discharging port (6) connected with a biogas residue tank (2). A pump (18) and a raw material circulating pump (20) are connected with a signal output end of controller. A pressure meter (24) and a multi-temperature sensor (25) are connected with a signal input end of a controller.    USE - Hierarchical bottom blowing stirring force-based marsh gas fermentation system for fermentation of livestock manure, crop straw, agricultural waste and urban domestic garbage.    ADVANTAGE - Space of the fermentation tank is heating uniformly, so raw material reacts fully to obtain high fermentation efficiency. The system is energy-saving, environment-friendly, highly safe and reliable, and has strong practicability and wide application range.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hierarchical bottom blowing stirring force-based marsh gas fermentation system.    Fermentation tank (1)    Biogas residue tank (2)    Exhaust port (4)    Sewage port (5)    Slag discharging port (6)    Pump (18)    Raw material circulating pump (20)    Pressure meter (24)    Multi-temperature sensor (25)    Marsh gas circulating system (28)    Raw material circulating system (29)
NOVELTY - A Bacillus muralis D6 (CCTCC NO: M2013461) with high flocculation ability, is new.    USE - The B.muralis D6 with high flocculation ability is useful for degrading slaughtered waste (all claimed).    ADVANTAGE - The B.muralis D6 enables to degrade slaughtered waste with chemical oxygen demand rate (CODCr) of 92.19%, suspended solid rate of 93.06%, turbidity rate of 97.23%, total nitrogen rate of 35.91%, and ammonium nitrogen content removal rate of 38.82%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage method of the B.muralis D6 which involves preparing fermentation culture medium using the above-mentioned strain, performing culturing process at constant temperature of 30 degrees C, and rotating speed of 160 revolutions/minute (rpm) for 72 hours, centrifuging the cultured solution at 4000 rpm for 30 minutes, obtaining supernatant, where the supernatant is microbial flocculating agent, and adding the microbial flocculating agent and calcium chloride to the slaughtered waste, and adjusting the pH value.
NOVELTY - This utility new type design agricultural organic fertilizer of fermenting steam exploded wood fibre straw preparation technology, specifically a one by using crop straw, sophora alopecuroide plant, livestock excrement and so on agricultural waste composting fermentation process of device. The device comprises one of a container which can be sealed are respectively set with blade in the container (10) of upper rotating shaft, the rotating shaft is set with multi-root distributing tube, upper gas distributing tube is arranged with multi-exhaust hole, gas distribution tube of an overall exterior container of an air inlet and an exhaust pipe connecting the intake and exhaust pipeline is provided with two paths, one path through the valve connecting the air pump, which is used for introducing air into the container, and the other path through the valve connecting vacuum pump for pumping of gas in the container. This utility new type of device can make the straw, agricultural waste and fermenting, and can make the temperature of in the fermentation process, gas control, fermenting, the fermentation speed is fast, the labour intensity is low, the process can be selected anaerobic fermentation and aerobic fermentation.
NOVELTY - Manufacture of (3S,4S)-methoxy-phenyl-3-((R)-1-hydroxyethyl)-4-acetyl-2-azetidinone involves dissolving (2R,3R)-N-(phenyl)-N-(2-oxo-propyl)-2,3-epoxybutyl amide in organic solvent, adding Lewis acid as catalyst, cooling, adding sodium tert-butoxide or potassium tert-butoxide, and reacting.    USE - Manufacture of (3S,4S)-methoxy-phenyl-3-((R)-1-hydroxyethyl)-4-acetyl-2-azetidinone used as intermediate for meropenem.    ADVANTAGE - The (3S,4S)-methoxy-phenyl-3-((R)-1-hydroxyethyl)-4-acetyl-2-azetidinone is manufactured efficiently and economically with high yield and reduced environmental pollution, by simple method under mild reaction conditions.
NOVELTY - Microbial inoculum is prepared by mixing Clostridium thermocellum, Geobacillus stearothermophilus, Pseudoxanthomonas taiwanensis, Brevibacillus agri, and Bacillus licheniformis. The colony forming unit ratio among Clostridium thermocellum, Geobacillus stearothermophilus, Pseudoxanthomonas taiwanensis, Brevibacillus agri and Bacillus licheniformis is (3-5:1-2:1-2:1-2:1-2).    USE - Microbial inoculum used for obtaining fertilizer by composting organic waste materials (claimed).    ADVANTAGE - The microbial inoculums enhances the fermentation process, does not require air in large amount, and also reduces the loss of nitrogen in a simple and cost-effective manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included:    (1) a method for preparing microbial inoculum, which involves culturing bacterial strains such as Clostridium thermocellum, Geobacillus stearothermophilus, Pseudoxanthomonas taiwanensis, Brevibacillus agri, and Bacillus licheniformis along with an auxiliary material; and    (2) a method for preparing compost, which involves mixing microbial inoculum and raw materials in molar ratio of (0.2-0.5:100); recording first three days of composted material, where the process is performed at 50 degrees C; recording the status of the composted material on twelfth day, where the process is performed at 50 degrees C; reducing the temperature to 40 degrees C after thirteenth day of the composted material; and stopping the process, where the obtained compost material comprises carbon and nitrogen element as finished product.
NOVELTY - A multi-one a reproducible energy sources for complementary of distributed energy system, comprising a system control unit, a solar heat collecting unit, a marsh gas fermentation unit, biomass gas treatment unit, a micro gas turbine power generation unit, the absorption refrigeration unit and so on. System by the solar heat collector of the solar radiation energy is converted into hot water hot energy, and then heating the marsh gas fermentation tank maintain the constant temperature. Produce marsh gas of the hot air mixing rear in the micro gas turbine as ' to drive the generator to generate electricity, a micro gas turbine driven by engine afterheat absorption refrigerating system produce, wherein the marsh gas fermenting process generated biogas with the micro gas turbine tail gas can be respectively used as culture medium carbon source, culturing microalgae to realize reuse of resource.
NOVELTY - A one with a stirring function of marsh gas device, relating to marsh gas device technology field, comprising a marsh gas tank, marsh gas tank well cover, a feed port, a discharge port, a marsh gas tank bottom part is provided with a lower bearing, the upper well cover is provided with a marsh gas tank with composite gear box device of drive motor, in the marsh gas tank well cover is vertically set with a shaft hole, further comprising a rotating shaft, a rotating shaft connecting the lower end upper bearing, upper rotating shaft rear end passes through the shaft connecting the upper power output end of composite gear box device, composite gear box device capable of driving the rotating shaft to rotate, the lower rotating shaft is provided with a stirring impeller, a rotating upper stirring impeller shaft is set up between the shaft hole and the rotating shaft is provided with a seal pad, in the marsh gas device with stirring function of the is provided with a stirring device, the machinery stirring principle static solution into a solution, with improved dirt-removing abiligy, abiligy and prevent the floating residue incrustation and blockage, deposition of produce.
NOVELTY - This new type utility claims one a biochemical processing sewage solid-liquid separation module, belonging to the sewage treatment device, aiming at providing a simple structure, one mud and water separating effect is good, the anti-impact load abiligy of strong sewage treatment device. It is composed of several rectification separating sheet fixing chunk plate between the two is composed of each rectifying separating sheet (8) is a V-shaped structure. This utility new type not only has simple structure, high efficiency sedimentation, anti-impact load abiligy is strong, and the sludge reflux in time, reduces the possibility of the sludge expansion is a solid-liquid separation device of a one sewage treatment.
NOVELTY - This utility new type relates to using of rural domestic sewage purifying device, especially a one can solve the rural sewage is directly discharged by sewage purifying tank double-layer structure of environmental pollution. For vast rural areas lacking simple and feasible, low in cost of sewage treatment device, so that a great amount of living sewage discharging randomly around river and pond pollution environment, and it is harmful to human body health of technical problem, this utility new type provides a double layer structure one sewage purifying tank, comprising a tank body of one top surface opening, the side wall of the upper part is provided with drain hole, wherein the plant layer and absorption layer is provided of a inner cavity of the bath in said plant layer is capable of floating of floating plant, the absorbing layer is biological floating band. This utility new type has simple structure, convenient operation, convenient maintenance and management, and does not need power drive, it can completely change rural domestic sewage can not reach the standard of discharge, effectively improve rural domestic environment, protect rural water source.
NOVELTY - Wastewater from oil refinery is treated by reacting wastewater with dibutyl phthalate-degrading Elizabethkingia sp. bacterial strain D8 (CCTCCM2012088).    USE - Treatment of wastewater from oil (claimed).    ADVANTAGE - The treatment method uses bacteria which effectively degrades dibutyl phthalate and organic matter in wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph depicting the nature of bacterial degradation of dibutyl phthalate. (Drawing includes non-English language text).
NOVELTY - Microorganism in wastewater is denitrified by adding hydrogen-containing supernatant of anaerobic sludge microorganisms in influent wastewater to improve anti-biocathode denitrification rate of nitrifying bacteria while maintaining stable reactor cathode pH values.    USE - Electrochemical denitrification of microorganism in wastewater (claimed).    ADVANTAGE - The denitrification method has high nitrogen removal rate and simultaneously produces hydrogen while performing denitrification.
NOVELTY - Chinese cabbage seedlings fertilizer is prepared by mixing vegetable compost, seaweed powder, stone powder and chicken manure in a volume ratio of 3-4:4-6:2-3. The vegetable compost comprises tomato, cabbage leaves and tobacco waste in a volume ratio of 3:2:2.    USE - AS Chinese cabbage seedlings fertilizer.    ADVANTAGE - The fertilizer improve physical and chemical properties of cabbage seedlings, is cost-effective and reduce environmental pollution.
NOVELTY - Pharmaceutical composition comprises 5-10 pts. wt. wormwood, 2-4 pts. wt. Astragalus polysaccharides, 2-4 pts. wt. cinnamic aldehyde, 2-4 pts. wt. multi-fertilizer, 4-6 pts. wt. virgate wormwood herb, 6-8 pts. wt. fortune Eupatorium herb, and 3-5 pts. wt. 40% propiconazole emulsion in water.    USE - The pharmaceutical composition is useful for treating anthracnose in eggplant (claimed).    ADVANTAGE - The composition has simple structure, is convenient to use, and exhibits good sterilizing effect and average effective rate of 92.1%.
NOVELTY - Sulfur trioxide and methylene dichloride are injected into mixer (A) in a ratio of 1:3. The obtained mixture is then introduced into mixer (B), and fast reaction is carried out at 80-110 degrees C for 0.2 seconds, under pressure of 0.6-0.9 MPa. The reaction mixture is mist-sprayed to sulfonated reactor with flow rate of 0.9 m/s. The resulting mixture is then introduced into autoclave, 4% acid is dropped into autoclave, and hydrolysis reaction is carried out at 35-40 degrees C with a flow rate of 800 l/h. The resulting product is hydrolyzed, and separated, to obtain cyclized acesulfame.    USE - Continuous production of cyclized acesulfame (claimed).    ADVANTAGE - The method economically provides cyclized acesulfame having reduced energy consumption, high stability, and high productivity, within a short period of time. The reactor used for producing cyclized acesulfame has prolonged-shelf life.
NOVELTY - Preparation of oil-saving agent involves adding corn straw-decomposed biomass oil, decomposing agent, isooctyl nitrate, petroleum benzene, stabilizer and polyoxymethylene dimethyl ether into a reactor, stirring the mixture for 4-6 hours, and cooling the reaction mixture to room temperature.    USE - Preparation of oil-saving agent used for diesel oil (claimed).    ADVANTAGE - The method enables economical and efficient preparation of oil-saving agent by simple process.
NOVELTY - The biogas collector comprises a PVC marsh gas collecting tube and an elbow fitting installed or connected with an anaerobic fermentation gas indoor tank. A tee pipe is connected with a bottom end of film opening seal and the PVC marsh gas collecting tube. An upper part of the PVC marsh gas collecting tube is connected with drilling numerous holes. A connecting rim is connected with a covering film.    USE - Biogas collector.    ADVANTAGE - The biogas collector is stable to use.
NOVELTY - The device has an anaerobic fermentation tank that is set on the upper portion of a pre-processing tank, and is provided with an air outlet (14) connected to a marsh gas pipe (20). A discharge port (15) of the pre-processing tank is provided with a spiral conveying device. The bottom of anaerobic fermentation tank is connected with liquid collecting tube (18). The anaerobic fermentation tank is provided with a spraying plate (16) and a sieve plate (17). The bottom of feeding port is provided with anaerobic fermentation tank provided with a filter layer (13).    USE - Anaerobic reaction device or processing high solid organic garbage used as fertilizer and soil conditioner.    ADVANTAGE - The crushing and pre-processing of material can be performed reliably. The uniformity of fermentation liquid adjusting material can be ensured to realize the stable fermentation of organic waste. The processing efficiency, compact arrangement and stable operation of the device can be improved. The floor space occupied by the device can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an anaerobic reaction method or processing high solid organic garbage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic reaction device for processing high solid organic garbage.    Filter layer (13)    Air outlet (14)    Discharge port (15)    Spraying plate (16)    Sieve plate (17)    Liquid collecting tube (18)    Marsh gas pipe (20)
NOVELTY - A Mucor circinelloides (CBS 131818), is new.    USE - The M.circinelloides or method is useful in preparation of enzyme for producing fuel ethanol (all claimed).    ADVANTAGE - The M.circinelloides prepares enzyme capable of reducing the potato tuber fermented mash viscosity within short duration to simplify fuel ethanol fermentation of sweet potato and lower production costs.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) enzyme preparation involves inoculating the M.circinelloides in fermentation medium and culturing at 30 degrees C and 130 revolutions per minute (rpm) for 4-5 days to obtain crude enzyme solution, where the fermentation medium is (a) medium (pH 5) comprising 20 g/l dry corn core, 3 g/l peptone, 0.5 g/l yeast extract, 2 g/l potassium dihydrogen phosphate, 1.5 g/l ammonium sulfate, 0.15 g/l magnesium sulfate heptahydrate, 0.3 g/l calcium chloride, 0.0005 g/l iron (II) sulfate heptahydrate, 0.0014 g/l zinc sulfate heptahydrate, 0.0016 g/l manganese (II) sulfate monohydrate, 0.0016 g/l cobalt (II) chloride hexahydrate and 3.3 g/l Tween 80 (RTM: Polysorbate 80), or (b) 4.4 g/l dry corn core, 10.7 g/l L-sorbitol, 0.5 g/l yeast extract, 4.9 g/l potassium dihydrogen phosphate, 0.15 g/l ammonium sulfate, 0.15 g/l magnesium sulfate heptahydrate, 0.3 g/l calcium chloride, 0.0005 g/l iron (II) sulfate heptahydrate, 0.0014 g/l zinc sulfate heptahydrate, 0.0016 g/l manganese (II) sulfate monohydrate, 0.0016 g/l cobalt (II) chloride hexahydrate and 3.3 g/l Tween 80 (RTM: Polysorbate 80); and (2) production of fuel ethanol, involves adding the obtained enzyme to the potato tuber pulp and reacting at 30-50 degrees C and 180 rpm for 2 hours.
NOVELTY - The device has a single-stage or multi-stage gas compressor (1) that is connected with a catalyzer (7) that is arranged in flow of compressed natural gas. A dryer (9) is arranged downstream of catalyzer. A cooler (13) is arranged in downstream of the dryer. The compressor is arranged to generate heat during compressing of natural gas, such that temperature of compressed natural gas is in range between 200-400 degrees .    USE - Natural gas compressing device.    ADVANTAGE - The natural gas compressing device can be designed in simple and compact manner, as catalyst is arranged inside the compressor. The removal of hydrogen and carbon dioxide from the natural gas can be enabled. By providing catalyzer and dryer, the carbon dioxide and hydrogen can be converted to methane in simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing methane from hydrogen and carbon dioxide using natural gas compressing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the natural gas compressing device.    Gas compressor (1)    Gas outlet (5)    Catalyzer (7)    Dryer (9)    Cooler (13)
NOVELTY - Soil-pollution processing method involves carrying out ventilation process for maintaining soil gap at aerobic conditions with respect to mixed soil of organic materials and contaminated soil by raising temperature to more than 55 degrees C, accelerating contaminant in the contaminated soil, and collecting contaminants decomposed using microorganisms stable at raised temperature.    USE - Soil-pollution processing method (claimed).    ADVANTAGE - The method enables soil-pollution processing economically and efficiently by a simple process.
NOVELTY - Producing enzymes involves preparing an inoculum with filamentous fungus i.e. Penicillium echinulatum, where mycelium of fungus is grown in a bioreactor comprising a carbon source, a nitrogen source and a culture medium. The pH value of the medium is maintained at 5-6. The enzyme complex is then recovered.    USE - Method for producing enzymes used for enzymatic hydrolysis of lignocellulosic biomass such as agricultural residues such as straw, corn cobs, rice husk, wood waste, bagasse or sugarcane (all claimed).
NOVELTY - Manufacture of 4-hydroxy-2-hydroxymethyl-2-cyclopentene-1-one (I) involves using water as a solvent, and obtaining 2-deoxy-aldohexose as starting material.    USE - Manufacture of 4-hydroxy-2-hydroxymethyl-2-cyclopentene-1-one derivative used as raw material for crude-like cyclopentenone, and used for pharmaceutical field.    ADVANTAGE - The method enables the manufacture of 4-hydroxy-2-hydroxymethyl-2-cyclopentene-1-one derivative by a simple process with high yield, and is environmentally-friendly.    DETAILED DESCRIPTION - Manufacture of 4-hydroxy-2-hydroxymethyl-2-cyclopentene-1-one derivative of formula (I) involves using water as a solvent, and obtaining 2-deoxy-aldohexose as starting material.
NOVELTY - A primary alcohol solution is contacted with a solid acid catalyst, to obtain alkyl ether. The reaction is carried out in liquid phase in a continuous fixed bed reactor. The catalyst is a synthetic acidic zeolite having silica-to-alumina molar ratio of 20-300.    USE - Production of alkyl ether e.g. diethyl ether used for manufacturing bulk chemical, fuel and fuel component.    ADVANTAGE - The method economically provides alkyl ether with high conversion rate. The catalyst used in the production process has high stability and is regenerated, and the non-reacted primary alcohol is recycled back to the feed. The production of alkyl ether using bio-ethanol as primary alcohol solution is an environmentally-friendly process.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view illustrating the production of alkyl ether from primary alcohol e.g. sugar-containing materials.    Sugar-containing material (1)    Fermentation (2)    Ethanol solution (3)    Dewatering unit (4)    Concentrated ethanol solution (5)
NOVELTY - Strains of microalgae belonging to green algae and blue-green algae of genus comprising Nannochloropsis, Chlorella, Scenedesmus or Synechococcus, are new.    USE - The strains of microalgae are useful for the production of biofuels and value added products including vitamins, pigments, antioxidants, omega -3 and omega -6 polyunsaturated fatty acids, docosahexaenoic acid (DHA) or eicosapentaenoic acid (EPA), where the strains are Nannochloropsis sp. IOC-105, Chlorella vulgaris IOC-106, Chlorella protothecoides IOC-107, Chlorella emersonii IOC-108, Chlorella pyrenoidosa IOC-109, Scenedesmus sp. IOC-110, and Synechococcus sp. IOC-111 (all claimed).    ADVANTAGE - The strains of microalgae can be rapidly cultivated in a cost-effective manner. The strains tolerate high salinity, pH, heavy metal contamination, temperature and light intensity. The strains have high lipid content, growth rate, carbon dioxide utilization ability and biomass.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the preparation of the strains of microalgae; and    (2) enhancing the biomass and lipid content of microalgae, comprising (A) culturing the microalgae in a medium comprising of algae culture medium, (B) adding auxins and cytokinins in the amount of 0.25-10 ppm during the lag phase of the microalgae culture, (C) exposing microalgae of step (B) to UV for 2 hours in log phase, (D) adding sodium thiosulfate in the amount of 0.05-2% in the late log phase for microalgae of step (C), (E) incubating the microalgae of step (D) at 10 degrees C for 6 hours, (F) adding hot water extract from different plants to microalgae of step (E), and (G) obtaining microalgae with high lipid content and biomass.
NOVELTY - Treating organic waste involves introducing a feed stream comprising organic waste into a first reactor; generating an effluent from the first reactor; and providing the effluent from the first reactor to a second reactor, where the first reactor is maintained at a pH of 6.5-10.    USE - For treating organic waste comprising biodegradeable solids, sludge, food waste, oily waste, solid waste with a high organic content, secondary sludge, oily sludge, industrial sludge and sewage sludge; and in wastewater treatment plant (claimed).    ADVANTAGE - The method is improved method of sludge treatment to enhance the degradation of biosolids and biogas generation; and more consistently produces methane and volatile fatty acids (VFAs).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a waste treatment plant using the process; and    (2) a reactor system for the treatment of biodegradeable waste, comprising a first reactor and a second reactor that is downstream of the first reactor and is in fluid connection with it, where the first and second reactors are adapted to use the process.
NOVELTY - Electrochemical reforming of oxygenate mixture comprises performing electrolysis on an alkaline oxygenate mixture to produce hydrogen, where the electrolysis does not form any significant amounts of oxygen.    USE - The process is useful for electrochemical reforming of oxygenate mixture.    ADVANTAGE - The process: forms less than 33 mol.% or less than 100 ppm of oxygen; and does not form any significant amounts of carbon dioxide or forms less than 500 ppm of carbon dioxide (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) alkalinizing oxygenate mixture comprising alkalinizing the oxygenate mixture to produce the alkaline oxygenate mixture, and performing electrolysis on the alkaline oxygenate mixture to produce hydrogen, where the electrolysis does not form any significant amounts of oxygen; and    (2) continuously alkalinizing the oxygenate mixture, comprising a biomass of a biomass derived stream, and performing electrolysis with an anode and a cathode comprising a conductive metal or a conductive metal alloy of the group comprising platinum, palladium, gold and/or nickel, where the anode and the cathode are supported on carbon-based materials and the electrolysis occurs at greater than 150 degrees C, pressures greater than 200 psig and at an applied voltage less than 1.23 volts to produce hydrogen, and the electrolysis does not form any significant amounts of oxygen or carbon dioxide and the current density of the electrolysis is greater than 15 mA/cm2.
NOVELTY - The fuel cell system has a fuel generation unit (1) that generates fuel gas. A fuel cell unit (2) produces electric power using fuel gas supplied from generation unit. A gas flow path circulates gas between fuel generation unit and fuel cell unit. A circulating system (8) circulates gas between fuel generation unit and cell unit. A control unit controls the amount of gas circulation of circulating system so that the fuel gas generation amount in the generation unit becomes below minimum value of the maximum amount range of gas circulation, during electric power generation.    USE - Fuel cell system.    ADVANTAGE - Since the control unit controls the amount of gas circulation of the circulating system so that the fuel gas generation amount in the fuel generation unit becomes below minimum value of amount range of gas circulation of circulating system that becomes maximum, at the time of electric power generation of fuel cell unit, the increase in the amount of gas circulation can be prevented. Thus the useless energy to the drive of circulating system can be avoided, and the energy efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system. (Drawing includes non-English language text)    Fuel generation unit (1)    Fuel cell unit (2)    Heater (3)    Container (5)    Circulating system (8)
NOVELTY - The system has a piping (7) that is provided for circulating gas between fuel generation element (1) and fuel electrode (2B) of fuel cell portion (2). A switch unit is positioned on the piping for circulation, and provided to switch a flow path to either of a first state which supplies the gas discharged from the fuel generation element to the fuel electrode of fuel cell portion, or the second state which supplies the gas introduced from the outside to the fuel electrode of the fuel cell portion. The gas discharged from the fuel generation element is discharged outside.    USE - Solid oxide fuel cell system.    ADVANTAGE - The fuel cell system can be provided with high durability. Since the flow path is switched either to first state which supplies the gas discharged from fuel generation element to the fuel electrode of fuel cell portion or the second state which supplies the gas introduced from the outside to the fuel electrode of fuel cell portion, the high concentration oxidizing gas discharged from the fuel generation element can be supplied effectively to the fuel electrode of fuel cell portion. Therefore, the fuel electrode of solid oxide fuel cell can oxidize with a high concentration oxidizing gas. The crack of fuel electrode and peeling can be avoided, and the performance of solid oxide fuel cell can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system. (Drawing includes non-English language text)    Fuel generation element (1)    Fuel cell portion (2)    Fuel electrode (2B)    Piping (7)    Gas introduction port (10)
NOVELTY - A copolymer (I), hexachloro iridium acid and its salt, and water are mixed, and an iridium oxide precursor solution is prepared. At least one portion of water is vaporized from the iridium oxide precursor solution, to obtain mesoporous iridium oxide.    USE - Manufacture of mesoporous iridium oxide used for oxidation catalyst of water, mesoporous iridium oxide electrode (all claimed) and anode catalyst in field of hydrogen generation and energy conversion.    ADVANTAGE - The mesoporous iridium oxide is efficiently manufactured with excellent oxidation-catalyst activity of water.    DETAILED DESCRIPTION - A copolymer of formula: H-(OCH2CH2)x-(OCH(CH3)CH2)y-(OCH2CH2)z-OH (I), hexachloro iridium acid and its salt, and water are mixed, and an iridium oxide precursor solution is prepared. At least one portion of water is vaporized from the iridium oxide precursor solution, to obtain mesoporous iridium oxide.    x=97-106;    y=65-70;and    z=97-106.    INDEPENDENT CLAIMS are included for the following:    (1) mesoporous iridium oxide;    (2) oxidation catalyst of water; and    (3) mesoporous iridium oxide electrode, which has mesoporous iridium oxide layer containing mesoporous iridium oxide on electroconductive substrate.
NOVELTY - Fermentation of methane involves throwing in organic waste containing ammonia nitrogen such that a state in which the carrier is immersed in a methane fermentation liquid, performing methane fermentation treatment after immersing the hydrophobic porous carrier which can support microorganisms in a methane fermentation liquid, and advancing methane fermentation reaction.    USE - Fermentation of methane (claimed).    ADVANTAGE - The method enables fermentation of methane without removing ammonia nitrogen.
NOVELTY - A solubilization mixture containing acid and water-soluble component is prepared under controlled temperature and pressure, by solubilization process (S3). The solubilized liquid extracted from solubilization mixture is then hydrolyzed with water using carboxylic acid as an acid catalyst by saccharification process (S5), to obtain saccharified liquid. The crystallinity degree of biomass feedstock containing cellulose is reduced.    USE - Saccharification method of cellulose biomass feedstock used for production of biofuel e.g. bioethanol.    ADVANTAGE - The method enables economical and efficient production of saccharified liquid without using acidic catalyst of strong inorganic acid.    DESCRIPTION OF DRAWING(S) - The drawing shows saccharification method of cellulose biomass feedstock. (Drawing includes non-English language text)    Crushing process (S1)    Moisture-content adjustment process (S2)    Solubilization process (S3)    Solid-liquid separation process (S4)    Saccharification process (S5)
NOVELTY - A hydrogen generating apparatus (100) consists of modifier (1) which generates hydrogen-containing gas, hydride-sulfurization device (2) which removes the sulfur compound, recycle flow path (3) which supplies hydrogen-containing gas to the device (2), condenser (4), combustor (5), combustion exhaust gas flow path (6) through which combustion exhaust gas from the combustor (5) flows, condenser (7), and thermal medium flow path (8). The condensers (4, 7) are arranged in such a way that the thermal medium in the thermal medium flow path recovers heat from them.    USE - Hydrogen generating apparatus is used for fuel cell for electric power generation (claimed).    ADVANTAGE - The condenser provided in the upstream gas flow path from the recycle flow path, and the recycle flow path which supplies the hydrogen-containing gas to the hydrodesulfurization device are appropriately arranged in the hydrogen generating apparatus.    DETAILED DESCRIPTION - A hydrogen generating apparatus consists of modifier which generates hydrogen containing-gas using raw material, hydride-sulfurization device which removes the sulfur compound in the raw material, recycle flow path which supplies hydrogen-containing gas to the device, condenser provided in the upstream gas flow path from recycle flow path, combustor which heats the modifier, combustion exhaust gas flow path through which combustion exhaust gas from the combustor flows, condenser provided in the gas flow path, and thermal medium flow path. The condensers are arranged in such a way that the thermal medium in the thermal medium flow path recovers heat from them.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic structure of the hydrogen generating apparatus. (Drawing includes non-English language text)    Modifier (1)    Hydride-sulfurization device (2)    Recycle flow path (3)    Condensers (4, 7)    Combustor (5)    Gas flow path (6)    Thermal medium flow path (8)    Hydrogen generating apparatus (100)
NOVELTY - An intermediate layer (118) is laminated on an anode layer (116). The baking process is performed at 1400 degrees C or more after the lamination of intermediate layer on the anode layer. An electrolyte layer (112) is laminated on the intermediate layer. The baking process is performed at 1300 degrees C or more after the lamination of electrolyte layer on the intermediate layer.    USE - Method for manufacturing fuel cell of electric power generation fuel cell system.    ADVANTAGE - The increase of the interfacial resistance of the fuel cell is suppressed by enlarging the diameter of metal particles and suppressing diffusion of nickel oxide.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the manufacture of laminated block of fuel cell.(Drawing includes non-English language text)    Electrolyte layer (112)    Anode layer (116)    Intermediate layer (118)    Lanthanum doped ceria layer (118a)    Laminated blocks (S2,S2a,S2b,S2c)
NOVELTY - The system (1) has a gas-liquid separation tank (41) that carries out gas-liquid separation of water currently accompanied to hydrogen generated at time of water-electrolysis operation and flows out of hydrogen exit. A hydrogen supply path for storage portion supplies hydrogen separated by gas-liquid separation tank (62) to a hydrogen storage tank (HT). An oxygen supply path for cell stacks (2) supplies oxygen from oxygen storage tank (OT) to oxygen inlet port. The hydrogen supply path for cell stacks supplies hydrogen from hydrogen storage tank to hydrogen inlet port.    USE - Charging-discharging system used as electric power storage system.    ADVANTAGE - The quantity of the gas exhausted out of the system can be decreased, when changing from charging operation to discharge operation. The power consumption of the system can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the outline of the charging/discharging system.    Charging/discharging system (1)    Cell stack (2)    Gas-liquid separation tanks (41,62)    Hydrogen storage tank (HT)    Oxygen storage tank (OT)
NOVELTY - The apparatus has a mixer (146) for receiving air stream (114) and fuel stream (116). A reformer (118) includes a partial oxidation catalyst to react mixed fuel stream to produce hydrogen-enriched stream (120). A suppression device (142) adds effective amount of water (122) to the hydrogen-enriched stream to produce combined stream, where the effective amount of water has amount of water sufficient to reduce a rate of reaction to form carbon from carbon monoxide in the combined stream. A solid oxide fuel cell (SOFC) (126) generates electricity (128) from the combined stream.    USE - Apparatus for providing liquid fuel to a solid oxide fuel cell with low water consumption in a stationary application e.g. industrial location application and portable skid application, in remote locations.    ADVANTAGE - The apparatus combines amount of water with the reformed fuel mixture to reduce formation of carbon from the carbon monoxide. The apparatus adds water to the reformed fuel mixture such that reaction to form elemental carbon from carbon monoxide and hydrogen is reduced by factor of 2, so that Vapor phase water added to hot gas mixture can suppress formation of elemental carbon and prevent degradation of SOFC stack in an effective manner.    DETAILED DESCRIPTION - The air stream is cathode-side air stream. The reformer is a partial oxidation catalyst reformer. An INDEPENDENT CLAIM is also included for a system for providing fuel to a solid oxide fuel cell with low water consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a system for providing fuel to a solid oxide fuel cell with low water consumption.    Air streams (114, 127)    Fuel stream (116)    Reformer (118)    Hydrogen-enriched stream (120)    Water (122)    SOFC (126)    Electricity (128)    Suppression device (142)    Mixers (146, 148)
NOVELTY - A catalyst (C1) comprising: a zirconia carrier (ZrO2), ruthenium, iron oxide (Fe2O3), at least one promoter (A) selected from the oxides of metals of groups IB, IIB and IIIa, and at least one promoter (B) containing V, Ti, Hf, and/or Zr, obtained by hydrolysis of at least one precursor selected from metal arenes, is new.    USE - As catalyst for selective hydrogenation process of aromatic or polyunsaturated compounds (claimed) such as benzene, toluene, xylenes and cyclohexene and dienes such as unsaturated carbonyls used as intermediate product in the production of polymeric materials.    ADVANTAGE - The catalyst improves the yield of compounds and allows effective selective hydrogenation of aromatic or polyunsaturated compounds.    DETAILED DESCRIPTION - A catalyst (C1) comprising: a zirconia carrier (ZrO2), ruthenium, iron oxide (Fe2O3), at least one promoter (A) selected from the oxides of metals of groups IB, IIB and IIIa, and at least one promoter (B) containing V, Ti, Hf, and/or Zr, obtained by hydrolysis of at least one precursor P-B selected from the following metal arenes: V0(arene)2 (I), V(arene)2 AlCl4 (II), M( eta 6-arene)pAlqXr (III), M( eta 6-arene)p'Alq.Xr-Rs (IV), is new.    V=vanadium;    Al=aluminum;    M=zirconium (Zr), hafnium (Hf) and/or titanium (Ti);    arene=benzene optionally substituted by 1 to 6 linear or branched 1-6C alkyl;    X=halo selected from Cl, Br, F, and I, preferably Cl;    R=linear or branched 1-15C alkyl;    p=1 to 2;    q=2 to 6, preferably 2 to 3;    r=8 to 20, preferably 8-11;    p'=1 to 2;    q'=2 to 6, preferably 2 to 3;    r'=2 to 20, preferably 6 to 9;    s=1 to 6, preferably 2.    INDEPENDENT CLAIMS are included for the following:    (1) a process for preparing the catalyst; and    (2) a selective hydrogenation process of aromatic or polyunsaturated compounds involving putting the aromatic or polyunsaturated compound in contact with hydrogen in the presence of the catalyst.
NOVELTY - Protecting material processing equipment involves conveying a biomass material under an electron beam on a conveyor, and enclosing components or motor components in a radiation opaque equipment enclosure.    USE - The method or system is useful for protecting material processing equipment (claimed).    ADVANTAGE - The method or system can treat feedstock materials, such as cellulosic and/or lignocellulosic materials, in a vault in which the equipment is protected from radiation and hazardous gases by equipment enclosures. The equipment enclosures are effective in protecting processing equipment/components utilized in radiation processing of materials. The equipment enclosures also provide a volume within which the atmosphere can be easily controlled, e.g., exchanged or evacuated for ozone free air and/or other inert gases. The equipment enclosures can be easy to construct and durable presenting an economical solution to the incidental, accidental and or unintentional degradation of processing equipment due to radiation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for protecting a motor and other motor components of a vibratory conveyor, comprising a vibratory conveyor having motor components mounted on a structure; and a substantially radiation opaque equipment enclosure configured to be positioned over the motor and having an open end that is dimensioned so as to provide a gap between the equipment enclosure and the structure when the equipment enclosure is in place.
NOVELTY - Insecticide composition comprises Ginkgo biloba leaves extract prepared by drying leaves, crushing to particle size of 100-300 mu m, adding water, and aging at 25-50 degrees C.    USE - The composition is useful as insecticide, fungicide and virucide in fertilizer composition for preventing plant disease caused by: insects such as peach aphid, cotton aphid, Tetranychus urticae, greenhouse whitefly, thrips, cabbage worm, Agromyza oryzae, Spodoptera exigua, slug, Chilo suppressalis, grass leafroller, coccid, pear fruit moth, apple leaf sucker, Laodelphax striatellus, diamondback moth, moth larvae, mole crickets, fall armyworm, cutworm, and Agrotis segetum; soil pests and soil nematodes such as Fusarium oxysporum, Cylindrocarpon destructans, Botrytis cinerea, Colletotrichum gloeosporioides, Sclerotium cepivorum, Sclerotinia sclerotiorum, Penicillium hirsutum, Pectobacterium carotovorum, Rhizoctonia solani, Pythium ultimum, and Pythium debaryanum, and virus such as tobacco mosaic virus, cucumber mosaic virus and potato virus (all claimed), in crops such as tomato, cucumber, lettuce and ginseng.    ADVANTAGE - The composition increases plant growth by preventing pests causing damage to the crops, increase income of farmhouse due to seed proliferation enlarging effect, and can be produced in an environment-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing Ginkgo biloba leaves extract comprising: preparing Ginkgo biloba leaf powder having particle size of 100-300 mu m; adding 100-500 pts. wt. of water; and aging at 25-50 degrees C.
NOVELTY - The system has multiple wind turbines (21) that are provided with generators that produce electricity. The salt water is received, and purified to purified water by multiple desalination units. The hydrogen is generated between 2-2000 Nm3/hour by multiple electrolytic cells. The amount of energy between 2-7 kWh of energy is used by the electrolytic cells to produce 1 Nm3 of hydrogen. The hydrogen is received by a hydrogen purification, storage and pressurization system from an electrolyzer unit.    USE - System for producing hydrogen at hydrogen wind farm such as grid-independent wind farm of hydrogen production facility located adjacent to water area.    ADVANTAGE - Since the additional units in the system can be activated, the water flow rates from the transfer pump system to the desalination system and electrolyzer system can be increased. Hence the hydrogen can be produced at greater rate. Since the combustion system can reduce or eliminate the production of greenhouse gases, the efficiency of the power plant can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen production facility.    Power distribution system (2)    Desalination system (4)    Electrolysis system (5)    Wind turbine (21)    Salt water storage tank (25)
NOVELTY - Producing biogas, comprises: providing at least one solid fermenter (2) for fermenting organic solids and at least one liquid fermenter (3); adding percolate to the percolation of the organic solids in the solid fermenter and the liquid fermenter; repeatedly applying the percolate on the organic solids in the solid fermeter; collecting the percolate at a bottom of the solid fermenter and feeding back into the liquid fermenter; and controlling the chemical, biological and/or physical properties of the percolate in the liquid fermenter.    USE - The method is useful for producing biogas (claimed) that is useful for heat generation and/or cogeneration plants for coupled electricity and heat production.    ADVANTAGE - The method allows the economical production of the biogas with less energy consumption of energy and high yield in an environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for producing the biogas, comprising the solid fermenter for the digestion of organic solids, and the liquid fermenter for receiving the percolate to the percolation of the organic solid absorbed in the solid fermenter, and a unit for controlling the chemical, biological and/or physical properties of the percolate in liquid fermenter.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a device for producing biogas.    Solid fermenter (2)    Liquid fermenter (3)    Overflow tank (6)    Sensor (7)    First solid fermenter box. (20)
NOVELTY - Composition comprises anhydrous ethanol fuel, biodiesel, glycerin, BK-2110 type additive and 2-propanone.    USE - Composition for formulation of biofuel mixture of ethanol used in diesel engines.    ADVANTAGE - The composition is eco-friendly.
NOVELTY - A comprehensive application process of straw is performed by crushing harvested corn straw by crusher, adding cellulose-decomposing bacteria, uniformly mixing, spraying water, maintaining temperature at 25-40 degrees C for 2 days while stirring, washing decomposed corn straw, filtering, pumping filtrate in fermentation tank, adding activated yeast, fermenting at 30-38 degrees C for 2 days, transferring in rectifying tower, distilling fermentation liquid to obtain alcohol, drying filter residue, adding additives, granulating in feed forming machine to prepare granular feed, and packing.    USE - Comprehensive application process of straw (claimed).    ADVANTAGE - The process eases pressure of tight energy resources, reduces feed production cost, overcomes mildew and bad palatability in feeding livestock, prevents air pollution, and increases straw added value.
NOVELTY - A fuel is produced from straw elemental carbon by crushing dried straw to fineness of 10-24 mesh, dipping in acidic salt aqueous solution, performing low temperature carbonization, graphitizing refining, ultrafining, dispersing, and stabilizing to obtain black oil.    USE - Production of fuel from straw elemental carbon for diesel engine and other internal combustion engine (all claimed).    ADVANTAGE - Fuel from straw elemental carbon is flowable and easily ignited, and has long-term storage stability and high energy density.
NOVELTY - Producing biomass fuel using efficient solar energy converting blue algae, comprises (i) culturing algae, (ii) inducing photosynthetic hydrogen production, and (iii) collecting hydrogen.    USE - The method is useful for producing biomass fuel using efficient solar energy converting blue algae (claimed).    ADVANTAGE - The method can improve biomass fuel production by maximizing algal cell photosynthesis process by conversion of solar energy, thus by regulating algal cell for oxygen-releasing activity of photosynthesis, the photosynthetic hydrogen-producing ability is increased by 200 times, and after hydrogen-production, the activated sludge by anaerobic degradation process is further transformed into methane and clean energy-marsh gas; and solves the problem that the blue algae having low efficiency conversion of solar energy.
NOVELTY - Improving straw hydrolysis efficiency comprises dissolving straw in alkali solution, magnetically stirring, then washing, and suction filtering to obtain alkaline straw; adding alkaline straw powder into a reactor, dissolving modifier low-boiling solvent and placing in constant pressure funnel, adding alkali to adjust the pH, then slowly dropwise adding into a reactor, controlling the temperature to 0-20 degrees C, filtering product, washing, and freeze drying the resulting solid; and adding modified straw into a reactor, adding inorganic acid, hydrolyzing, centrifuging, and testing the hydrolysate.    USE - The method is useful for improving straw hydrolysis efficiency (claimed).    ADVANTAGE - The hydrolyzing efficiency of straw is improved upon proper chemical modification.    DETAILED DESCRIPTION - Improving straw hydrolysis efficiency comprises (i) dissolving 1 pts. straw in 50-100 pts. alkali solution (1-5%), magnetically stirring at room temperature for 24 hours, then washing with deionized water, and suction filtering to obtain alkaline straw; (ii) adding alkaline straw powder into a reactor, dissolving 1/3-1 pts. modifier in 1/3-10 pts. low-boiling solvent and placing in the constant pressure funnel, adding alkali to adjust the pH to 8-9, then slowly dropwise adding into a reactor, controlling the temperature to 0-20 degrees C, for 2-6 hours, filtering the product, washing with deionized water until neutral, and freeze drying the resulting solid for 12-24 hours; and (iii) adding 1 pts. modified straw into a reactor, adding 20 pts. inorganic acid (of 30% concentration), hydrolyzing at 50 degrees C for 2 hours, centrifuging, and testing the hydrolysate. The modifier is cyanuric chloride; the low-boiling solvent is acetone, diethyl ether, tetrahydrofuran or dioxane; the alkali is sodium carbonate, sodium phosphate, sodium hydroxide, potassium hydroxide or calcium hydroxide; and the inorganic acid is sulfuric acid or hydrochloric acid.
NOVELTY - A biological material contains 25-30 pts. wt. corn straw powder, 25-30 pts. wt. soybean straw powder, 25-30 pts. wt. potato straw powder, 0.001-0.003 pts. wt. phosphorus bacteria powder, 0.001-0.003 pts. wt. potassium bacteria powder, 0.001-0.003 pts. wt. silicate bacteria powder, 4-6 pts. wt. sodium hydroxide, 3-7 pts. wt. potassium hydroxide, 1-8 pts. wt. calcium hydroxide, 1-2 pts. wt. nano granular inorganic material, 2-7 pts. wt. calcium carbonate, 1-6 pts. wt. calcium sulfate, 1-4 pts. wt. diatomite, 2-4 pts. wt. acrylic fibers, and 3-9 pts. wt. anti-aging agent.    USE - Biological material for wastewater treatment (claimed).    ADVANTAGE - The biological carrier is highly efficient, microporous, and conducive to microbial biofilm; has large surface area and good wetting properties; and improves wastewater treatment speed. Manufacture process is simple and easy.
NOVELTY - An integrated cultivation sewage treatment device which is steel box type shell has 1st level oxidation tank (1), 2nd level oxidation tank (2), secondary sedimentation tank (3), sludge tank (4), and sand filtering and sterilizing tank (5) in which box body has aeration device connected to 1st level oxidation tank and 2nd level oxidation tank by gas distribution pipe.    USE - Integrated cultivation sewage treatment device for pig cultivation sewage wastewater treatment by biogas fermentation process (claimed).    ADVANTAGE - The device is convenient to install, use, and detect process, saves earth waste resources, has no peculiar smell during operation, and can be buried underground without affecting appearance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of integrated cultivation sewage treatment device for pig cultivation sewage wastewater slurry treatment by biogas fermentation process in which device has 1st level oxidation tank, 2nd level oxidation tank, secondary sedimentation tank which uses vertical flow and has triangular weir, sludge tank, sand filtering and sterilizing tank, aeration device, gas pipe set in box-type shell, and power supply control switch connected to aeration device inside the box to control aeration.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of an integrated cultivation sewage treatment device.    1st level oxidation tank (1)    2nd level oxidation tank (2)    Secondary sedimentation tank (3)    Sludge tank (4)    Sand filtering and sterilizing tank (5)
NOVELTY - Processed anionic wastewater obtained from natural plant material comprises 55-80 pts. wt. crop straw, 0.0003-0.0006 pts. wt. lactic acid bacterial powder, 0.0003-0.0006 pts. wt. nitrifying bacteria powder, 1-3 pts. wt. nanogranular inorganic material, 2-6 pts. wt. calcium carbonate, 1-8 pts. wt. mica powder, 3-8 pts. wt. hollow glass bead, 1-3 pts. wt. graphite powder, 2-7 pts. wt. talc, 3-7 pts. wt. gypsum powder , 1-3 pts. wt. highly dense polyethylene, 3-4 pts. wt. toughening agent ethyleneoctene copolymer (EOC), and 1-3 pts. wt. stearic acid.    USE - As processed anionic wastewater.    ADVANTAGE - The processed anionic wastewater is prepared simply, and cost-effectively, and has excellent absorbing effect.
NOVELTY - A gelatin micro-sphere framework chitosan fiber composite bone cement is prepared by enzymatically hydrolyzing gelatin micro-sphere, chitosan fiber, calcium phosphate bone cement powder and solidifying liquid, where the gelatin micro-sphere and chitosan fiber mass ratio is 7:1, and rear cross-linking the solution to obtain micro-fiber frame structure, where the mass ratio of calcium phosphate bone cement powder and micro-fiber frame structure is 3:1. The micro-fiber frame structure is put in a hydraulic molding machine for biomass solidification to obtain the bone cement.    USE - Gelatin micro-sphere framework chitosan fiber composite bone cement.    ADVANTAGE - The cement has high porosity and mechanical strength, and improves performance of the drug-loading micro-pore.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a gelatin micro-sphere framework chitosan fiber composite bone cement, which involves preparing gelatin microsphere and chitosan fiber according to mass ratio of 7:1, cross-linking genipin solution for 3 days, freezing and drying for 24 hours to obtain micro-sphere fiber frame structure, putting the micro-sphere fiber frame structure in a hydraulic molding machine for biomass solidification and stirring for 5 minutes to obtain the finished product.
NOVELTY - Usage method of film-anaerobic bioreactor for sewage treatment involves introducing nitrate and/or nitrite and sulfide-containing to-be-treated sewage into anaerobic reactor containing removing nitrogen-sulfur-removing bacteria-containing activated sludge, contacting Thiobacillus denitrifican with the bacteria, removing obtained nitrogen, sulfur and sulfur compound by the bacteria, contacting obtained product with separation film in membrane module, filtering and treating obtained filtrate.    USE - Usage method of film-anaerobic bioreactor for sewage treatment (claimed).    ADVANTAGE - The nitrogen is effectively removed from the sewage by energy-saving and simple method.    DETAILED DESCRIPTION - Usage method of film-anaerobic bioreactor for sewage treatment during desulfurization for removing nitrogen involves providing anaerobic reactor containing removing nitrogen-sulfur-removing bacteria-containing activated sludge, introducing nitrate and/or nitrite and sulfide-containing to-be-treated sewage into the anaerobic reactor, contacting Thiobacillus denitrifican with the nitrogen-sulfur-removing bacteria using nitrate as electron acceptor, such that sulfide in sewage is oxidized into elemental sulfur, and at same time, nitrate and/or nitrite is reduced to nitrogen, removing obtained nitrogen, sulfur and sulfur compound by the bacteria, contacting obtained product with separation film in membrane module, such that several Thiobacillus denitrifican and other suspended particulate material are trapped in separating film, filtering Thiobacillus denitrifican and other suspended particulate material retained in the reactor, and treating obtained filtrate.
NOVELTY - Method for preparing medicine, involves (a) mixing nucleotide salt and trace element and does not contain glucose, where the nucleotide salt includes e.g. 5'-adenylate, sodium or potassium, guanosine 5'-adenylate, sodium or potassium, cytidine 5'-dipotassium or sodium and uridine 5'-potassium or sodium, and trace element is chosen from zinc, manganese, magnesium, iron, and boron, preferably zinc sulfate, manganese sulfate, magnesium sulfate and ferrous sulfate, and (b) crushing the mixture, adding microelement to the crushed mixture and crushing the mixture.    USE - The method is useful for preparing medicine which is useful for promoting nutrients in skin (claimed).    ADVANTAGE - The method is environmentally-friendly, prepares medicne which increases resistant to disease, and improves quality of the medicine.    DETAILED DESCRIPTION - Method for preparing medicine, involves (a) mixing 30-70 wt.% nucleotide salt and 30-70 wt.% trace element and does not contain glucose, where the nucleotide salt is chosen from 5'-adenylate, sodium or potassium, guanosine 5'-adenylate, sodium or potassium, cytidine 5'-dipotassium or sodium, uridine 5'-potassium or sodium and 5'-nucleotide mixture of potassium or sodium, and trace element is chosen from zinc, manganese, magnesium, iron, and boron, preferably zinc sulfate, manganese sulfate, magnesium sulfate and ferrous sulfate, and (b) crushing the mixture, adding microelement to the crushed mixture, crushing the mixture to mesh of 50-150.
NOVELTY - Fertilizer comprises 250-300 pts. wt. urea, 130-150 pts. wt. monoammonium phosphate, 100-l20 pts. wt. potassium sulfate, 250-300 pts. wt. ammonium sulfate, 250-300 pts. wt. humic acid, 0.015-0.2 pts. wt. auxin (sodium nitrophenolate), 1-3 pts. wt. beneficial bacteria, 1-3 pts. wt. anti-caking powder, 1-2 pts. wt. anti-caking oil, 10-20 pts. wt. ammonia and 10-30 pts. wt. sulfuric acid.    USE - As fertilizer for wheat.    ADVANTAGE - The fertilizer has increased efficiency, provides fertilization effect for longer period of time, improves soil, does not causes soil hardening even when used for longer period of time, increases yield of wheat by 15-20% per acre and reduces required amount of fertilizer by 20%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production method of the above-mentioned fertilizer, which involves crushing and mixing the above-mentioned raw materials except ammonia, auxin, beneficial bacteria and sulfuric acid, adding obtained mixture to granulator at 3 MPa, granulating the mixture, drying obtained granules at 200-250 degrees C for 15-20 minutes, sieving dried granules through 2.8-4.75 mm meash size sieve, separating fine granules and coarse granules, subjecting the fine granules and coarse granules continuously through the above-mentioned steps, cooling obtained semi-finished product, adding anti-caking powder, anti-caking oil, auxin and beneficial bacteria in the above-mentioned weight proportions to the semi-finished product, mixing components uniformly, sieving mixture, packaging fertilizer product and storing packed product.
NOVELTY - The apparatus has an acid-producing fermentation section which includes an acid fermentation reactor (21), and a methane production which includes a methane reactor (22). A feeding port (1) is provided on fermentation reactor. An oxidation-reduction electrode (2) is provided on feeding port. A discharging port (7) is provided on other side of acid fermentation reactor which includes a temperature control temperature probe (9) on lower portion. A slag-drip opening (19) is provided on methane reactor connected to a connecting pipe (20) to attach with fermentation reactor.    USE - Two-stage anaerobic fermentation apparatus for biomass waste.    ADVANTAGE - The fermentation apparatus shortens the start-up time, saves energy consumption, improves operation efficiency, and is highly effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an anaerobic fermentation method of methane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the two-stage anaerobic fermentation apparatus.    Feeding port (1)    Oxidation-reduction electrode (2)    Discharging port (7)    Temperature control temperature probe (9)    Slag-drip opening (19)    Connecting pipe (20)    Acid fermentation reactor (21)    Methane reactor (22)
NOVELTY - Culturing oil-producing microalgae using brewery wastewater comprises: (i) inoculating oil-producing microalgae into BG culture medium and culturing; (ii) adding the BG culture medium into a membrane bioreactor containing brewery wastewater, inoculating above cultured microalgae, placing in an incubator under light, incubating and culturing under light; (iii) inoculating oil-producing microalgae into BG culture medium-containing brewery wastewater, placing in a dark incubator, culturing under dark; and (iv) filtering via filter membrane, and collecting oil-producing microalgae by filtration.    USE - The method is useful for culturing oil-producing microalgae using brewery wastewater (claimed).    ADVANTAGE - The method completely utilizes brewery wastewater (claimed) and thus is environmentally friendly, is simple, economical and has fast operation.    DETAILED DESCRIPTION - Culturing oil-producing microalgae using brewery wastewater comprises: (i) inoculating 20% (vol./vol.) oil-producing microalgae into BG culture medium and culturing at 25-35 degrees C to a concentration of 2x 107-1x 108 cfu/ml; (ii) adding the 40-60% BG culture medium into a membrane bioreactor containing brewery wastewater, inoculating 20-50% (vol./vol.) above cultured microalgae, placing in an incubator under light, incubating at 25-35 degrees C with a pH of 7-10, an illumination period of 10-16 hours, an illumination intensity of 2000-5000 lux, aeration rate of 0.01-0.2 VVm and culturing for 48-144 hours under light; (iii) inoculating 20-50% (vol./vol.) oil-producing microalgae into 40-60% BG culture medium-containing brewery wastewater, placing in a dark incubator, culturing at 25-35 degrees C with a pH of 7-10 under aeration rate of 0.01-0.2 VVm for 48-72 hours under dark; and (iv) filtering via filter membrane having a pore size of 0.5-2.5 mu m at 20-35 degrees C with a pressure of 0.01-0.1 MPa and pH of 5-8, and collecting oil-producing microalgae by filtration.
NOVELTY - Gemmobacter aquaticus strain ZYEM-P1 having preservation number of CGMCC NO. 7925, is new.    USE - The Gemmobacter aquaticus strain ZYEM-P1 is useful in sewage treatment, preferably oil-containing sewage treatment (all claimed).    ADVANTAGE - The Gemmobacter aquaticus strain ZYEM-P1 has high sewage treatment efficiency, good processing effect, and simple culture conditions; and is easy to store, and suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of Gemmobacter aquaticus strain ZYEM-P1 in sewage treatment, preferably oil-containing sewage treatment.
NOVELTY - Method for improving saccharification of rape straw, involves (a) crushing rape straw into powder, (b) treating the powder using X-ray irradiation, (c) adding sulfuric acid to powder obtained in step (b), mixing uniformly and subjecting to water bath, cooling, filtering, washing the residue using water, until the residue reach netural state, and drying, and (d) adding citric acid, sodium citrate buffer solution and cellulase and performing enzymolysis, and filtering to obtain the product.    USE - The method is useful for improving saccharification of rape straw (claimed).    ADVANTAGE - The method is simple and cost-effective, and reduces pollution and develops renewable energy resources.
NOVELTY - Saline-alkali soil improvement involves planting Sesbania flowering plants in field in 20-40 cm depth. 2500-4500 kg per acre of manure, ferrous ammonium sulfate, fulvic acid, citric acid, humic acid, Tween (RTM: Polysorbate 20) and one or multiple modifying agents are also mixed in the soil before sowing the crops. The organic matters are mixed in water and then heated.    USE - Method for improving saline-alkali soil (claimed).    ADVANTAGE - The method improves saline-alkali soil by adjusting structure and physical and chemical state in a simple and cost-effective manner.
NOVELTY - Biodiesel oil is prepared by reacting 0.10 mol N-methylimidazole and 0.10 mol N-bromobutane at 80 degrees C, stirring for 5 hours, pouring into separating funnel, washing with 30 mL ethyl acetate, distilling, vacuum drying at 70 degrees C for 24 hours, dissolving in 40 mL acetone, adding sodium bisulfate, distilling, washing with 30 mL ethyl acetate, distilling, evaporating at 70 degrees C for 8 hours to obtain solution A, reacting Xanthoceras sorbifolia and methanol, adding solution A, heating, cooling, distilling, standing to obtain upper and lower layers, taking upper layer, drying, and filtering.    USE - Method for preparing biodiesel oil (claimed).    ADVANTAGE - The environment-friendly method has easy separation and high stability.    DETAILED DESCRIPTION - A biodiesel oil is prepared by reacting 0.10 mol N-methylimidazole and 0.10 mol N-bromobutane at 80 degrees C, magnetically stirring for 5 hours, pouring into separating funnel, washing with 30 mL ethyl acetate, distilling, evaporating, vacuum drying at 70 degrees C for 24 hours, dissolving in 40 mL acetone, adding sodium bisulfate at 80 degrees C, magnetically stirring for 12 hours, cooling to room temperature, filtering, distilling, washing with 30 mL ethyl acetate, distilling, evaporating at 70 degrees C for 8 hours to obtain solution A, reacting Xanthoceras sorbifolia and methanol, adding solution A, seal opening, heating, cooling to room temperature, distilling, cooling, standing to obtain upper and lower layers, taking upper layer, drying, and filtering.
NOVELTY - The device has an upper overflow port (3) and a lower overflow port (6) that is connected with upper port and a lower overflowing opening of overflowing channel (5). A marsh gas tank (10) of overflow wall is connected with overflow pipe (8). The overflow pipe of overflow water is connected with the marsh gas tank to sediment at the bottom of cleaning water seal. A water seal bending slag removing valve (12) is installed at the bottom, so as to seal overflowing pipe and water seal bent (13) of overflowing port valve.    USE - Anti-freezing anti-scab overflowing device of large and medium-sized methane tank.    ADVANTAGE - By changing the overflowing material of overflow pipe, the crust layer in the tank can be removed and also the overflow freezing of overflowing pipe in winter can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the large and medium biogas tank.    Overflow ports (3,6)    Overflowing channel (5)    Overflow pipe (8)    Marsh gas tank (10)    Water seal bending slag removing valve (12)    Water seal bent (13)
NOVELTY - A bio-energy generator has microbial biomass filter which filters energy produced by discharging waste from farms, family and apartment.    USE - Bio-energy generator (claimed).
NOVELTY - The method involves performing selective absorption of hydrogen sulphide relative to carbon dioxide by bringing a gas effluent (1) such as natural gas, into contact with a solution (5) comprising water and nitrogen compound. The compound is provided with a tertiary amine function or hindered secondary amine function. The selective absorption of hydrogen sulphide is controlled by adding a viscosifying agent such as polyacrylamide, to the absorbent solution. The absorbent solution is provided with a nitrogenized compound such as methyldiethanolamine triethanolamine.    USE - Method for selectively eliminating hydrogen sulphide from a gaseous effluent such as natural gas, synthesis gas, combustion smoke, refinery gas, acid gas, Claus process output gas, biomass fermentation gas, cement factory gas, and incinerator smoke (all claimed), comprising carbon dioxide for treatment applications.    ADVANTAGE - The selective absorption of hydrogen sulphide is controlled by adding the viscosifying agent to the absorbent solution, thus efficiently improving selective absorption of hydrogen sulphide with respect to carbon dioxide without deteriorating the speed of absorption of hydrogen sulphide. The method improves dynamic viscosity of the absorbent solution from 80% with regard to a same solution without the viscosifying agent.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a structure used for processing waste gas including acid compounds using an amine absorbent solution.    Gas effluent (1)    Acid compounds (2)    Absorbent solution (4)    Water and nitrogen compound solution (5)    Regenerated absorbent solution (6)
NOVELTY - (5Z)-5-((3-Methoxy-1H-pyrrol-2-yl)methylene)-2-methyl-3-pentyl-pyrrole compounds (I) are new.    USE - (I) are useful as anticancer, immunosuppressive, antidiabetic, antirheumatic, antibacterial, antifungal and antiparasitic agents. Test details are described but no results are given.    ADVANTAGE - (I) can be easily and economically prepared in an eco-friendly manner.    DETAILED DESCRIPTION - (5Z)-5-((3-Methoxy-1H-pyrrol-2-yl)methylene)-2-methyl-3-pentyl-pyrrole compounds of formula (I) and their salts, polymorphs and derivatives are new.    R3 = 1-10C-alkyl, 1-10C-alkene, 1-10C-alkyne or optionally substituted aliphatic or aryl hydrocarbyl, preferably 1-pentene.    An INDEPENDENT CLAIM is included for the preparation of (I).
NOVELTY - A polymer supported-ionic liquid catalyst (I) is new.    USE - New polymer supported-ionic liquid catalyst is used for preparing synthetic biodiesel by catalytic esterification of methanol or ethanol, with palmitic acid (claimed).    ADVANTAGE - The polymer-supported acidic ionic liquid catalyst has excellent catalytic activity.    DETAILED DESCRIPTION - A polymer supported-ionic liquid catalyst of formula (I) is new.    m=50-200;and    n=50-100.    An INDEPENDENT CLAIM is included for manufacture of polymer supported-ionic liquid catalyst.
NOVELTY - An ethanol-diesel fuel blend additive comprises 10-20 pts. wt. 4-7C alcohol, 50-70 pts. wt. ether, 10-20 pts. wt. high molecular polymer, and 10-20 pts. wt. cetane number improver.    USE - Ethanol-diesel fuel blend additive.    ADVANTAGE - The additive can improve stability, cold-start performance and ignition performance of ethanol-diesel fuel blend.
NOVELTY - Preparation of microbial agent for degrading domestic sewage, involves: inoculating Pseudomonas, Bacillus, nitrifying bacteria, Nitrosomonas bacteria and Bacillus megaterium in sterilized domestic sewage culture medium to culture and incubating; (2) mixing the bacterial liquid strains; (3) obtaining the domestic sewage degrading microbial agent.    USE - The method is useful for preparing microbial agent for degrading domestic sewage (claimed).    ADVANTAGE - The method efficiently prepares microbial agent with enhanced sewage treating capacity, sewage ammonia conversion rate can reach to 95%, total nitrogen conversion rate is 82%, COD conversion rate is 60%, and total phosphorus conversion rate can reach 75%.    DETAILED DESCRIPTION - Preparation of microbial agent for degrading domestic sewage, involves: inoculating Pseudomonas, Bacillus, bacillus, nitrifying bacteria, Nitrosomonas and Bacillus megaterium in sterilized domestic sewage culture medium to culture and incubating at a temperature of 15 degrees C, shaking at a speed of 130 rpm under the condition of culturing, the number of bacteria strain is 3.6x 108-9.3x 108 cells/ml, 2.5x 108-7.8x 108 cells/ml, 1.5x 108-6.6x 108 cells/ml, 5.0x 108-6.8x 108 cells/ml and 2.5x 108-8.6x 108 cells/ml; (2) mixing the bacterial liquid strains Bacillus and Pseudomonas to obtain chemical oxygen demand (COD) degradation complex bacteria, the nitrifying bacteria and Nitrosomonas liquid strain to obtain composite nitrification, and the B. megaterium bacterial liquid and phosphorus removing bacteria; (3) mixing the COD degradation complex bacteria, composite nitrification bacteria and phosphorus removing bacteria according to the volume ratio of 10:(0.25-4):0.5, obtaining the domestic sewage degrading microbial agent.
NOVELTY - The method involves separating gonads, flour meat offal and sand sea cucumbers. Size of a flour meat of the sand sea cucumber is shrinked when size of the flour meat of the sand sea cucumber reaches approximately 60 mesh. The flour meat of the sand sea cucumber is dried with a convection oven at a temperature of 40-55 degree Celsius for 24 hours, where the flour meat of the sea cucumber includes size of 60 mesh sand and the flour sea cucumber contains specific percent water content with protein, carbohydrates, crude fiber, fat and ash content.    USE - Method for preparing material i.e. sand sea cucumber meat meal (claimed), for hormone replacement therapy in treatment of menopause for middle-aged women.    ADVANTAGE - The method enables converting testosterone in a middle-aged vanilla body to estradiol to reduce menopause in a middle-aged women so as to provide body estradiol in the women, and to allow the body estradiol as a drug without side effects of menopause, so that sea cucumber powdery product can be an alternative TSH, and can add to repertoire of use of products in efficient, effective, safe and environmentally-friendly manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for preparing flour sea cucumbers.'(Drawing includes non-English language text)'
NOVELTY - A high molecular mesoporous silicon dioxide hybrid membrane comprises 60-98 wt.% poly (ethylene oxide)-poly-caprolactam embedded, 2-40 wt.% block copolymer functionalized mesoporous silicon dioxide and optionally functionalized mesoporous silica functionalized polyethyleneimine reagent, where the hybrid film thickness is 60-100 microns, polyoxyethylene segments of the block copolymer is 55-60 wt.%, polycaprolactone segments represent the mass fraction of the block copolymer of 40-45 wt.%.    USE - High molecular mesoporous silicon dioxide hybrid membrane for seperating carbon dioxide/methane mixture (claimed).    ADVANTAGE - The membrane has good separating property, and can be prepared in simple and cost effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing high molecular mesoporous silicon dioxide hybrid membrane, which involves taking O-functionalized mesoporous silica prepared in methanol as solvent, preparing 10% polyethyleneimine solution, stirring for 0.5 hours, at ratio of mesoporous silica and polyethylene imine solution of 1:1, adding mesoporous silica and poly-ethyleneimine solution, stirring for 8 hours, placing in a vacuum oven and drying for 48 hours, to give the functionalized mesoporous silica, adding polyoxyethylene-polycaprolactam block copolymer in ethanol at a temperature of 75-80 degrees C, heating under reflux, stirring for 0.5-4 hours, and completely dissolving to obtain 2-7 wt.% poly-polyoxyethylene-polycaprolactone block copolymer solution, adding the resultant functionalized mesoporous silica in poly-polyoxyethylene-polycaprolactone block copolymer solution, stirring at room temperature for 5-10 hours, casting the resulting solution onto a clean glass plate, drying at room temperature and placing in a vacuum oven to remove residual solvent to obtain finished product.
NOVELTY - Synthesizing methanol from methane comprises pressurized gasification of carbon containing raw material including methane, hydrogen, carbon monoxide and carbon dioxide, where a part of carbon monoxide is converted to hydrogen and carbon dioxide, removing sulfide and most carbon dioxide to improve hydrogen-carbon ratio to obtain fresh air, using a part of all of the fresh air in methanol synthesis by methanation reaction to obtain synthetic natural gas, by adjusting the carbon monoxide conversion rate and synthesis gas amount to adjust the yield of synthetic natural gas.    USE - The method is useful for synthesizing methanol from methane (claimed).    ADVANTAGE - The method recycles gas without any recycling device; and has low production cost and investment, thus improving economic efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for synthesizing methanol from methane, comprising a methane gasification device, carbon monoxide conversion device, a purification device, a compression cycle machine, methanol synthesis device and methanation device, where the methane gasification device, carbon monoxide conversion device, purification device, methanol synthesis device and methanation device are sequentially connected. The conversion device is parallely connected with the methanol synthesis device. The methanol synthesis device comprises a compression cycle machine, a methanol synthesis reactor and alcohol divider, which are sequentially connected in series. The compression circulating machine is connected with a constant-pressure bypass. A circulating gas outlet of the alcohol divider is provided with a circulating pipeline connected to the inlet of the compression cycle machine. The outlet of the alcohol divider is connected with the methanation device.
NOVELTY - Biomass comprises biomass carbon powder and additives to form composite biomass carbon powder, where biomass carbon powder is less than 10% and grain diameter is less than 0.5 mm. The additives are ferric oxide (0.5%) and urea (2.5%).    USE - Biomass used for coal burning power station boiler (claimed).    ADVANTAGE - The biomass is prepared in a simple and cost effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biomass, which involves:    (A) selecting, drying, cutting, crushing, sieving and molding agricultural and forest biomass to obtain grain material;    (B) prolysing biomass by using fixed or movable low temperature pyrolysis device at 200-300 degrees C for 10-30 minutes and then cooling to room temperature to obtain biomass carbon;    (C) crushing obtained biomass carbon to obtain biomass carbon powder;    (D) spraying biomass carbon powder with alkali solution(1-5%) at 60-90 degrees C for 0.5-2 hours to obtain mixture;    (E) drying and grinding obtained mixture to obtain biomass carbon powder, where powder grain diameter is less than 0.5mm; and    (F) mixing biomass carbon powder with grain diameter is less than 0.5mm and additive obtain the biomass.
NOVELTY - A Pseudomonas otitidis (CCTCC NO: M2013458), is new.    USE - The P.otitidis is useful in microbial additive in the form of powder for purifying water, preferably water in aquaculture or domestic sewage (all claimed).    ADVANTAGE - The P.otitidis provides nutrients to water, and obviously reduces nitrogen and ammonia in water.
NOVELTY - Microorganism composition comprises bacteria, actinomycete, yeast and mold, chosen from Bacillus subtilis, B.licheniformis, Zymomonas mobilis, Streptomyces, Lactobacillus plantarum, L.acidophilus, Saccharomyces cerevisiae, Pichia pastoris, fragrance producing yeast, Rhizopus, R.oryzae, and Mucor indicus.    USE - The microorganism composition is useful for processing kitchen waste (claimed).    ADVANTAGE - The microorganism composition is isolated from nature or fermented foods and hence it is nontoxic and has good processing effect and stable heredity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparing the composition involves mixing several strains of bacteria, actinomycete, yeast and mold, culturing the mixed microorganisms in different liquid culture medium, adding sterilized wheat bran to the medium, and mixing the mixture uniformly; and    (2) applying the above-mentioned microorganism for processing kitchen waste, involves (a) culturing the above-mentioned strains in the culture medium, allowing the culture to stand and agitating the culture, (b) sterilizing wheat bran, mixing the obtained culture with sterilized wheat bran, brown sugar and yeast extract, and drying the mixture, and (c) mixing the mixture with kitchen waste, fermenting and degrading waste for 24-72 hours.
NOVELTY - The utility model claims one high fermentation bed type pigsty pad material automatic turning system, comprising at least two turning lane, automatic turning vehicle, rail and rail replacing vehicle lane, each turning lane are laid up on the cement ground pig's column below the fermenting area along the longitudinal direction's pigsty, automatic turning vehicle to move back and forth on the upper turning lane and taking turning work, changing the vertical is paved on the terminal's each turning lane, the rail is installed on the rail replacing vehicle moving lane up, automatic vehicle turning after turning the work's one of turning traffic lane by the rail vehicle and the other corresponding's turning lane. The utility model's working efficiency, reducing the labour intensity, automatically turning the pig manure and the padding, fully stirring and mixing in the turning pad material process, by the rail roadway and rail replacing vehicle realizes the automatic turning vehicle's free conversion between each turning rail, reduces the number of arranged automatic turning vehicle's, which effectively reduces the cost of the device.
NOVELTY - Low energy consumption denitrification biological filter device comprises regulation pool (1), dosers (2,3), water distributor (4), zeolite filler layer (5), backwash water outlet (6), buffer layer (7), sand filter layer (8), supporting layer (9), backwash pump (10), water inlet pump (11), packing support plate (12), reactor body (13), storage tank (14) and fan (15).    USE - Low energy consumption denitrification biological filter device.    ADVANTAGE - The device ensures total nitrogen (TN) of less than 3 mg/L, and requires small floor area.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the application of low energy consumption denitrification biological filter device comprising feeding wastewater in regulation pool, opening first doser, adding ammonium chloride solution, adjusting ammonia concentration to 1.6 plus minus 0.0.3 mg/L, starting water inlet pump, water flowing through water distributor to zeolite filler layer, zeolite adsorbing ammonium-nitrogen in water, adding nitrifying bacteria, converting ammonium-nitrogen to nitrate/nitrite-nitrogen, water flowing to packing support plate into buffer layer and into sand filter layer, starting second doser, adding sodium acetate into buffer layer, water flowing to supporting layer and into storage tank, opening backwash pump, backwashing sand filter layer and discharging.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of low energy consumption denitrification biological filter device.    Regulation pool (1)    Dosers (2,3)    Water distributor (4)    Zeolite filler layer (5)    Backwash water outlet (6)    Buffer layer (7)    Sand filter layer (8)    Supporting layer (9)    Backwash pump (10)    Water inlet pump (11)    Packing support plate (12)    Reactor body (13)    Storage tank (14)    Fan (15)
NOVELTY - Fluorenone derivatives (I) are new.    USE - (I) are useful in fields of medicine, pesticide, polymer material, photosensitive material and dye.    ADVANTAGE - The method: is simple and non-toxic; and produces high-purity product, which has unique optical and electrical properties, and biological activity.    DETAILED DESCRIPTION - Fluorenone derivatives of formula (I) are new.    R1, R2 = H, benzyl, methyl or methoxymethyl.    An INDEPENDENT CLAIM is also included for preparation of (I).
NOVELTY - Sphingomonas paucimobilis strain (I) having a preservation number of CCTCC N0: M2013456, is new.    USE - (I) is useful in water purification such as aquaculture water or domestic sewage (all claimed).    ADVANTAGE - (I) can: be prepared with aerobic denitrification ability and simple nutrient requirement; obviously reduce the nitrate nitrogen in water; effectively reduce the ammonia nitrogen content in the domestic sewage; and be developed into aquatic micro-ecological preparation and sewage processing agent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a microbial additive comprising the Sphingomonas paucimobilis strain.
NOVELTY - A Tetraselmis sp. (KCTC 12236BP), is new. The Tetraselmis sp. (KCTC 12236BP) is grown at culture condition of 0-37 degrees C.    USE - The Tetraselmis sp. (KCTC 12236BP) is useful in composition for producing biodiesel (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) composition for producing biodiesel, comprising the above-mentioned strain, as an active ingredient; and    (2) method for producing biodiesel, involves culturing the above-mentioned strain in culture medium (light irradiation), collecting the culture, and adding catalyst to the culture (converts glycerol esters of fatty acids existing in the strain to fatty acid ester).
NOVELTY - The apparatus has first solid-liquid separator (20) to separate organic waste ejected from an acid formation tank (10) into liquid waste (22) and solid industrial waste (21). An organic acid extractor (30) extracts organic acid from separated liquid waste. A methane reaction bath (40) disassembles the liquid waste. A mixed tide (60) mixes solid industrial waste with microorganism and provides mixture to a dry anaerobic tank (70). The dry anaerobic tank performs dry anaerobic treatment to the mixture.    USE - Organic acid and biogas formation apparatus using organic waste such as food waste and sewage sludge.    ADVANTAGE - The generation yield of the biogas degraded with the acid fermentation microorganism can be prevented. The generation yield of the biogas and organic acid can be increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the organic acid and bio gas generator. (Drawing includes non-English language text)    Acid formation tank (10)    Solid-liquid separators (20,90)    Solid industrial waste (21)    Liquid waste (22)    Organic acid extractor (30)    Methane reaction bath (40)    Mixed tide (60)    Dry anaerobic tank (70)
NOVELTY - An Aspergillus glaucus has accession number of CGMCC6025.    USE - An Aspergillus glaucus for saline transformation and environmental pollution treatment (all claimed).    ADVANTAGE - Strain has high salinity environment degradation of straw.
NOVELTY - A Chlamydomonas moewusii strain KNUA 013 (KCTC 12065BP), is capable of producing heptadecane, hexadecenol, and 16-18C fatty acid, is new.    USE - The C.moewusii strain KNUA 013, is useful for producing heptadecane, hexadecenol, and 16-18C fatty acid (claimed) for producing biodiesel.
NOVELTY - A kiln-type biogas dry fermentation method involves crushing straw, adding manure such that weight ratio of straw and manure is 2:1, uniformly mixing in a mixer, filling the filling material before closing out the door of fermentation device to thickness of 30 cm, arranging adjacent horizontal plate, connecting with oblique manifold with elbow or T-joint, arranging gas collecting pipe, paving, completing fermentation in 3 or more stages, opening feeding port, and storing fermentation gas in air bag.    USE - Kiln-type biogas dry fermentation method (claimed).    ADVANTAGE - The biogas is efficiently produced by fermentation by effectively utilizing agricultural waste.    DETAILED DESCRIPTION - A kiln-type biogas dry fermentation method involves crushing straw, adding manure such that weight ratio of straw and manure is 2:1, uniformly mixing in a mixer, filling the filling material before closing out the door of fermentation device to thickness of 30 cm, arranging adjacent horizontal plate, connecting with oblique manifold with elbow or T-joint, arranging gas collecting pipe, paving, completing fermentation in 3 or more stages, opening feeding port, and storing fermentation gas in air bag. The fermentation device has inter-circular kiln-type fermentation chamber having dome with diameter of 600 cm and height of 200-300 cm, (2), airbags for storing biogas, reservoir supporting the installation of pipes and valves, vent, unidirectional fermentation control valve or gate, elastic sealing membrane on the exterior of each kiln fermentation chamber, fermentation deposits manifold, and circular peripheral fermentation outlet.
NOVELTY - A livestock and poultry breeding waste water for resource utilization and circulation use device, comprising an anaerobic tank, a grid tank, an adjusting pool, a removing device. the aeration biological filter tank (BAF), a disinfection tank, a sludge tank, a sludge filter press, a gas collecting device, wherein the device can be ammonia nitrogen struvite precipitation method of removing ammonia nitrogen and removing method for removing ammonia nitrogen; This utility model based on anaerobic technology, technology, BAF technique and sterilizing technology to livestock and poultry breeding waste water source, it is processed by anaerobic fermentation for producing biogas production waste water and marsh gas and separating solid from liquid, solid slag and producing organic fertilizer is used as raw material to produce organic fertilizer, waste water by recycling and discharging and BAF technique and sterilizing, the processing effect is good, the energy consumption is low, use of the resource at the same time is provided with economic benefit.
NOVELTY - The device comprises a methane detector connected to the methane conversion unit (40). The methane conversion unit is connected to the carbon dioxide separating device (30). The respiration outcome transfer device is interposed between the carbon dioxide separating device that separates the carbon dioxide among multi-flow passage control unit (10) outlet baffle and port and soil microbes respiration outcome. The multi-flow passage control unit is connected to sample containers containing soil samples. The transfer device is controlled to supply the carbon dioxide to separating device.    USE - Device for measuring soil microbes breathing quantity.    ADVANTAGE - The respiration outcome transfer device is interposed between the carbon dioxide separating device that separates the carbon dioxide among multi-flow passage control unit outlet baffle and port and soil microbes respiration outcome, thus provides a convenient and automated way of measurement of soil microbes breathing quantity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for measuring soil microbes breathing quantity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for measuring soil microbes breathing quantity. (Drawing includes non-English language text).    Multi-flow passage control unit (10)    Carbon dioxide separating device (30)    Methane conversion unit (40)
NOVELTY - Spherical methane gas generating tank comprises an upper half casing (110) exposed to solar heat and installed on ground, a lower half casing (120) formed airtight and combined with the upper half casing, an inlet (130) for introducing organic waste, connected to the upper half casing or lower half casing, a residue outlet (140) for discharging residue, after anaerobic digestion of the organic waste, connected to the upper half casing or the lower half casing, and a gas delivery unit (150) for externally transferring generated methane gas during anaerobic digestion of the organic waste.    USE - Used as spherical methane gas generating tank.    ADVANTAGE - The tank prevents rapid lowering of temperature, is simple and compact, can be easily operated.    DETAILED DESCRIPTION - Spherical methane gas generating tank comprises an upper half casing (110) exposed to solar heat and installed on ground, having hollow hemispherical shape, a lower half casing (120) formed airtight and combined with the upper half casing, having hollow hemispherical shape, an inlet (130) for introducing organic waste, connected to the upper half casing or lower half casing, a residue outlet (140) for discharging residue, after anaerobic digestion of the organic waste, connected to the upper half casing or the lower half casing, and a gas delivery unit (150) for externally transferring generated methane gas during anaerobic digestion of the organic waste, connected to upper half casing or the lower half casing. An INDEPENDENT CLAIM is also included for methane gas generator comprising the spherical methane gas generating tank, and solar air heater for circulating air heated by solar heat into the spherical methane gas generating tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the spherical methane gas generating tank.    Upper half casing (110)    Lower half casing (120)    Inlet (130)    Residue outlet (140)    Gas delivery unit (150)
NOVELTY - The method involves providing ground terminal, battery terminal, ignition switch, main hydrogen reactor unit, fly back arrestor unit, gas filter and air intake manifold. The ground terminal, battery terminal and ignition switch are connected with the hydrogen reactor uni. The hydrogen gas output from fly back arrestor unit is passed to gas filter to absorb moisture and output portion is connected to the intake manifold.    USE - Controlled method for generating hydrogen gas with zero sludge by highly efficient electrolysis and develop electronic control module.    ADVANTAGE - The need for washing the plate of electrolyzer can be prevented effectively. The leakage of the engine oil can be prevented effectively, so that pollution to the environment can be reduced efficiently. The structure of the electrolyzer is simple, so that manufacturing cost of the electrolyzer can be reduced. The electrolyzer can be maintained efficiently. The service life of the battery can be prolonged, as the generation of noise and deterioration in the battery can be prevented effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen reactor.
NOVELTY - Preparation of solid catalyst comprises adding 0.01-0.02 mol potassium ferrocyanide (K4Fe(CN)6.3H2O) in 40-80 mL water to obtain solution A, adding 0.1-0.2 mol zinc chloride (ZnCl2) into 10-20 mL water and 10-20 mL t-butyl alcohol to obtain solution B, and dissolving 30 g polyethylene glycol in 50 mL alcohol to obtain solution C; magnetically stirring solution C in slowly dropping solution A, gradually adding solution B, stirring, filtering, and vacuum drying; and esterifying, adding methanol and waste oil, adding catalyst, condensing, refluxing, and separating catalyst.    USE - Method for preparing solid catalyst used for biodiesel (claimed).    DETAILED DESCRIPTION - Preparation of solid catalyst comprises adding 0.01-0.02 mol K4Fe(CN)6.3H2O in 40-80 mL water to obtain solution A, adding 0.1-0.2 mol ZnCl2 into 10-20 mL water and 10-20 mL t-butyl alcohol to obtain solution B, and dissolving 30 g polyethylene glycol in 50 mL alcohol to obtain solution C; at 45-50 degrees C, magnetically stirring solution C in slowly dropping solution A, gradually adding solution B to generate precipitate, continuously stirring for 1-1.5 hours, filtering, and vacuum drying at 50-60 degrees C for 6-8 hours; and esterifying, adding methanol and waste oil in reaction kettle, adding catalyst, circulating, condensing, refluxing, stirring, and separating catalyst.
NOVELTY - A multifunctional hydrogen-oxygen generator and drinking water machine comprises base module (1), hydrogen and oxygen separating module (2), shell module (3), water dispenser module (4) and storage module (5).    USE - Multifunctional hydrogen-oxygen generator and drinking water machine for supplying oxygen and conditioning air.    ADVANTAGE - The machine is convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of multifunctional hydrogen-oxygen generator and drinking water machine.    Base module (1)    Hydrogen and oxygen separating module (2)    Shell module (3)    Water dispenser module (4)    Storage module (5)
NOVELTY - The method involves combining LNG and oxygen-enriched gas combustion in a gas turbine engine circulating device for generating carbon dioxide and water from high temperature flue gas. The flue gas is provided for heat recovery by a steam power circulation device. A high temperature high pressure steam is provided for improving power generation efficiency of natural gas. LNG cold energy is provided in an air separation device to reduce carbon dioxide energy consumption.    USE - Liquefied natural gas collecting joint power circulating method.    ADVANTAGE - The method enables achieving high power generation efficiency with high carbon dioxide trap and cold energy of liquefied natural gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a combined power circulating system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic circuit diagram of a combined power circulating system. '(Drawing includes non-English language text)'
NOVELTY - This utility new type relates to a marsh gas membrane separation one decarburization device, comprising a compressor, a drying and dehydrating system, first-stage membrane system, second level film system, CO2 percent of recovery device and methane storage device by using the gas component in the high molecular polymer dissolve diffusion rate of different gas permeation through the membrane according to the rate of speed of the gas into " and " ". Each gas component under the effect of pressure difference between the two sides of the membrane side caused by the permeation rate of the fibre film wall is separated, so as to separate the carbon dioxide of the biogas purifying of decarburization. Process flow is simple, the energy consumption is low, the device is simple to maintain.
NOVELTY - The device comprises a condenser to absorb light energy, and a solar absorber to provide heat to a copper chloride circulating system. The condenser comprises a first condenser and a second condenser, and a photovoltaic cell for providing electrical energy to the copper chloride circulating system. The solar energy absorber is connected between the first condenser and the second condenser for absorbing heat. The first condenser is a first parabolic groove condenser arranged face to face to the second condenser.    USE - Hydrogen production device.    ADVANTAGE - The hydrogen producing device requires low reaction temperature and less energy.    DETAILED DESCRIPTION - The device comprises a condenser to absorb light energy, and a solar absorber to provide heat to a copper chloride circulating system. The condenser comprises a first condenser and a second condenser, and a photovoltaic cell for providing electrical energy to the copper chloride circulating system. The solar energy absorber is connected between the first condenser and the second condenser for absorbing heat. The first condenser is a first parabolic groove condenser arranged face to face to the second condenser. Focal point of the first parabolic groove condenser is located between the solar energy absorber and the second condenser. A surface of the photovoltaic cell comprises a filter coating having a transmittance value of 0.85-0.95 and a light wavelength of 400-100 nm. The solar energy absorber is equipped with a heat exchanger for increasing the efficiency of heat transfer. The heat exchanger is provided with a thermoelectric module to supply electric energy to the copper chloride circulating system. The device further comprises a heater for providing heat to the copper chloride circulating system when there is a shortage of heat provided by the solar absorber.
NOVELTY - Fertilizer preparation involves mixing manure, sawdust, animal offal powder, plant ash, humic acid, rock phosphate powder, rice hull, seaweed meal, shell powder, perlite and corrosion accelerating agent. The obtained mixture is fermented for 2-3 days in a fertilizer tank, where water content of obtained product is 38-42wt.%. The obtained product is mixed with bentonite for 40-50 minutes. Broom cypress fruit, pine needle, thunder god vine, radix stemonae, cinnamon and clove are extracted thrice using water for 2-4 hours.    USE - Method for preparing fertilizer (claimed).    ADVANTAGE - The method enables preparation of fertilizer in simple and convenient manner. The fertilizer is nutritionally balanced and has antibacterial ability, strong absorption rate and high organic matter.    DETAILED DESCRIPTION - Fertilizer preparation involves mixing manure, sawdust, animal offal powder, plant ash, humic acid, rock phosphate powder, rice hull, seaweed meal, shell powder, perlite and corrosion accelerating agent. The obtained mixture is fermented for 2-3 days in a fertilizer tank, where water content of obtained product is 38-42wt.%. The obtained product is mixed with bentonite for 40-50 minutes. Broom cypress fruit, pine needle, thunder god vine, radix stemonae, cinnamon and clove are extracted thrice using water for 2-4 hours. The obtained extract is heated and concentrated to obtain concentrated juice. Ethanol (95vol.%) is added to concentrated juice to precipitate water-soluble impurity. The obtained solution is filtered and then filtrate is centrifuged. The obtain product is filtered and then sterilized using ultraviolet light to obtain herbal liquid. The obtained liquid is mixed with obtained powder and garlic powder in weight ratio of 40:1:1 for 20-25 minutes using a granulator. The obtained product is cooled naturally for 1-2 hours and then packaged to obtain finished product.
NOVELTY - Fertilizer preparation involves mixing pig manure (50-95%) and agricultural waste (5-50%), wher moisture content of materials is adjusted. The obtained mixture is mixed with humic acid (0.1-10%) with continuous stirring to obtain mixture. The obtained mixture is fermented under aerobic conditions to obtain desired product.    USE - Method for preparing fertilizer (claimed).    ADVANTAGE - The method enables to prepare fertilizer in simple and cost-effective manner.
NOVELTY - Bio-organic fertilizer comprises sawdust, cow manure, chicken manure, household garbage, Bacillus stearothermophilus additive, Lactobacillus plantarum additive, traditional Chinese medicinal additive and kelp.    USE - The bio-organic fertilizer is useful for improving quality and yield of crop, and protecting soil.    ADVANTAGE - The bio-organic fertilizer is contamination-free and reduces usage of chemical fertilizer and pesticide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the fertilizer which involves (a) stirring sawdust, cow manure, chicken manure, household garbage, traditional Chinese medicinal additive and kelp uniformly in a stirrer and adjusting moisture content to 55-60%, (b) adding above mixture to fermentation tank with B.stearothermophilus and L.plantarum additives, mechanical turning for loosening material and increasing oxygen content, fermenting at 60-70 degrees C for 10-15 days and performing secondary fermentation at 48-52 degrees C for 5-7 days, and (c) drying fermented material at 80 degrees C in fluidized bed drier until the moisture content is reduced to 10-15%, crushing and sieving through 60-80 mesh sieve to obtain product.
NOVELTY - Preparation of sugar alcohol fermented fertilizer, involves inoculating the yeast into medium after sterilization, and adding sugar alcohols, sodium, potassium and phosphorus, surfactant, amine hexanoate into the yeast.    USE - The method is useful for preparation of the sugar alcohol fermented fertilizer (claimed).    ADVANTAGE - The sugar alcohol fermented fertilizer has good water-solubility and spreadability, and promotes growth of crops, improves crop yield and quality, and improves selenium content of agricultural product.
NOVELTY - Solid fertilizer comprises 20-30 %mass protein fermentation, 5-20 %mass water-retention agent, 40-50 %mass chemical fertilizer, 5-10 %mass water and 0.5-1 %mass trichlorphon raw powder. The fertilizer is prepared by mixing the above-mentioned raw materials and drying to obtain the product.    USE - As solid fertilizer.    ADVANTAGE - The fertilizer is cost-effective and has long lasting effect.
NOVELTY - Microbial soil activating agent, comprises 5-10 pts. wt. microbial culture, 10-25 pts. wt. potato, 15-35 pts. wt. straw, 50-70 pts. wt. organic fermentation, 3-7 pts. wt. xanthan gum, 5-15 pts. wt. humic acid, 0.05-0.2 pts. wt. ammonium dihydrogen phosphate, and 0.1-0.5 pts. wt. soil disinfector.    USE - As microbial soil activating agent.    ADVANTAGE - The microbial soil activating agent promotes forming of soil granule, improves soil structure, and improves crop yield.
NOVELTY - Method for obtaining active ingredient of agent, involves crushing Rabdosia rubescens, adding ethanol as solvent to crushed product, recycling solvent to obtain ethanol total extract, mixing the ethanol total extract with silicon glue, adding petroleum ether, ethyl acetate and methanol to the mixture, recycling petroleum ether, ethyl acetate and methanol, purifying obtained product by column chromatography using Sephadex (RTM: Crosslinked dextran gel) LH-20 column, and re-crystallizing purified product to obtain product.    USE - The method is useful for obtaining active ingredient of an agent which is useful for promoting blood coagulation, where the active ingredient is oridonin, rosmarinic acid, salicylic acid, or ferulic acid, preferably oridonin (all claimed).
NOVELTY - Preparation of bromo-methyl naltrexone involves mixing naltrexone hydrochloric acid, methylene dichloride, triethylamine and tertiary butyl dimethyl chlorosilane, reacting in dipolar aprotic solvent, extracting, recycling solvent and obtaining 3-O-tertiary butyl dimethyl silicon ether naltrexone, adding product to methyl bromide, sealing in a container, decompressing, distilling and obtaining 3-O-tertiary butyl dimethyl silicon ether-bromomethyl naltrexone, and adding product in hydrobromic acid solution and 1-3C alcohol.    USE - Preparation of bromo-methyl naltrexone (claimed).    ADVANTAGE - The method efficiently and economically provides bromo-methyl naltrexone with high purity using simple process in short period of time.    DETAILED DESCRIPTION - Preparation of bromo-methyl naltrexone involves mixing naltrexone hydrochloric acid, methylene dichloride, triethylamine and tertiary butyl dimethyl chlorosilane, reacting in dipolar aprotic solvent, extracting, recycling solvent and obtaining 3-O-tertiary butyl dimethyl silicon ether naltrexone, adding product to methyl bromide, sealing in a container, decompressing, distilling and obtaining 3-O-tertiary butyl dimethyl silicon ether-bromomethyl naltrexone, adding product in hydrobromic acid solution and 1-3C alcohol, de-protecting, reducing the temperature to crystallize, filtering and obtaining bromo methyl naltrexone crude product and refining crude product using mixed solvent.
NOVELTY - This utility new type claims a one STAIC high-efficient anaerobic reactor, comprising upper and lower two overlapping of UASB anaerobic reaction tank and a feeding tube, a cloth tube, discharging, sludge reflux tube, spherical three-phase separator and inclined connecting tube, return tube, an adjustable-speed circulating pump, a gas-liquid separating room, a methane tube, two reaction pool height and diameter of superposition are different TAIC anaerobic reactor, the diameter ratio of upper and lower tank is 5: 4, the height ratio of two upper tank is 1: 4, the whole reactor of height is 12-30, ratio is 3-6, adjustable-speed circulating pump is set on the sludge reflux tube upper is provided with an automatic traction backflow circulating device up the feed tube is provided with a protective cover, biogas slurry and biogas residue overflow tube reflowing tube high than the feeding pipe feeding tube is provided with reverse washing switch. This utility new type has high volume of production rate can be higher than the TAIC reactor of the fermentation rate reaches 1, and floor area is less than TAIC reactor, investment is greatly reduced, augmented can automatic trailer in the reflux tank material liquid, and prevent the material liquid in the pipeline in the block, improves the benefit, the most important is that it improves the resistance of tank body of punching.
NOVELTY - Preparation of biodiesel oil involves drying branches, straw, sawdust or mulberry yellow residue biomass waste at 250-600 degrees C for 8-12 hours under nitrogen gas supply in a muffle furnace, naturally-cooling to room temperature, adding product in 95-98% wt.% concentrated sulfuric acid, filtering, processing at 100-300 degrees C in muffle furnace for 10-15 hours, cooling, adding distilled water, drying in an oven at 60 degrees C and obtaining solid acid catalyst, mixing alcohol, methanol and silkworm pupae oil in molar ratio of 6:1-12:1, adding 1-5% w solid acid catalyst, and heating.    USE - Preparation of biodiesel oil (claimed).    ADVANTAGE - The method efficiently and economically provides biodiesel oil using simple process.    DETAILED DESCRIPTION - Preparation of biodiesel oil involves drying branches, straw, sawdust or mulberry yellow residue biomass waste at 250-600 degrees C for 8-12 hours under nitrogen gas supply in a muffle furnace, naturally-cooling to room temperature, adding product in 95-98% wt.% concentrated sulfuric acid, filtering, processing at 100-300 degrees C in muffle furnace for 10-15 hours, cooling, adding distilled water, drying in an oven at 60 degrees C and obtaining solid acid catalyst, mixing alcohol, methanol and silkworm pupae oil in molar ratio of 6:1-12:1, adding 1-5% w solid acid catalyst, heating to 50-90 degrees C, stirring for 5-60 minutes, stratificating and obtaining fatty acid methyl ester, mixing obtained ester, methanol and silkworm pupae oil in molar ratio of 4:1-8:1, then adding 1-5 wt.% solid hydroxide, heating to 30-70 degrees C for 5-30 minutes, standing layer and obtaining biodiesel as upper layer.
NOVELTY - A 2-substituted benzimidazole ring derivative is synthesized by reacting o-phenylenediamine and aldehyde of formula R-CHO (II) in organic solvent with action of enzyme i.e. pig pancreatic alpha -amylase, Aspergillus oryzae amylase, peak alpha -amylase, Lipase AT30 (RTM: Triacylglycerol lipase), or Lipase AY30 (RTM: Butyrinase).    USE - Synthesis of 2-substituted benzimidazole ring derivative (claimed).    ADVANTAGE - The synthesis of 2-substituted benzimidazole ring derivative is mild, environment-friendly, suitable for recrystallization, and has high yield, shorter reaction time, and easy removal of catalyst.    DETAILED DESCRIPTION - A 2-substituted benzimidazole ring derivative of formula (I) is synthesized by reacting o-phenylenediamine and aldehyde (II) in organic solvent with action of enzyme i.e. pig pancreatic alpha -amylase, A. oryzae amylase, peak alpha -amylase, Lipase AT30, Lipase AY30, or pig pancreatic trypsin.    R=heterocyclic aryl, or aryl optionally substituted with 1-3C alkyl, 1-3C alkoxy, NO2, halo, or Ph.
NOVELTY - A biologically active peptide is prepared using walnut meal by adding water to walnut meal until concentration is 10-15 wt.%, heating for 30-45 minutes at 100-121 degrees C, passing in colloid mill to obtain walnut meal slurry, heating to 45-55 degrees C, adding 0.6-1.2% alkaline protease and 1-1.5% cellulase based on mass of walnut meal raw material, inactivating enzyme when degree of hydrolysis reaches 10-15%, centrifuging, collecting supernatant as walnut meal enzymolysis liquid, passing enzymolysis liquid in ultrafiltration membrane with 10000 Da membrane flux, and collecting permeate.    USE - Preparation of biologically active peptide using walnut meal used for preparing uric acid-lowering medicine (claimed).    ADVANTAGE - Preparation method is simple, low in cost, environment-friendly, and accurate in vitro screening indicators, and biologically active peptide has strong uric acid lowering activity, and protects kidney and significantly reduces serum creatinine levels when tested in rats.    DETAILED DESCRIPTION - A biologically active peptide is prepared using walnut meal by adding water to walnut meal until concentration is 10-15 wt.%, heating for 30-45 minutes at 100-121 degrees C, passing in colloid mill to obtain walnut meal slurry, heating to 45-55 degrees C, adding 0.6-1.2% alkaline protease and 1-1.5% cellulase based on mass of walnut meal raw material, inactivating enzyme when degree of hydrolysis reaches 10-15%, centrifuging, collecting supernatant as walnut meal enzymolysis liquid, passing enzymolysis liquid in ultrafiltration membrane with 10000 Da membrane flux, collecting permeate, subjecting to strong acid gel type cation exchange resin with acidic water as eluent, collecting eluate, vacuum concentrating, and spray drying.    DESCRIPTION OF DRAWING(S) - The drawing shows a uric acid peak chromatogram of uric acid peptide and commercial soy peptide. (Drawing includes non-English language text).
NOVELTY - A culture substrate comprises vegetable residual strain compost, biogas residue, and ground slag, where ratio is 3-5:5-8:2-3. The residual strain is plant or plant tissue of tomato, cucumber, and Chinese cabbage abandoned in fields at ratio of 6:2:3. The biogas is anaerobic fermentation of crushed semi-solid corn stalk powder and chicken manure at ratio of 4:1.    USE - Culture substrate used for cultivating Capsicum seedling.    ADVANTAGE - The culture substrate reduces production cost and environment pollution and has economic, social, and ecological benefits.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of vegetable stump comprising pulverizing vegetable, where carbon/nitrogen ratio is 24-26 and moisture content is 58-60%, adding 0.5% viable cells 2x 109 cfu/g compost inoculant, and fermenting;    (2) preparation of biogas residue comprising adding water to crushed corn straw and chicken manure, stirring, adding 0.1% anaerobic strain, stirring, and fermenting at 28 degrees C; and    (3) preparation of culture substrate comprising preparing vegetable stump; rotting for 6 days, turning, stacking, and reducing temperature to 30 degrees C; preparing biogas residue; and uniformly mixing vegetable residual strain compost, biogas residue, and ground slag at ratio of 4:6:3 and adjusting pH to 6.1-6.3.
NOVELTY - A culture substrate comprises vegetable residual strain compost, ground slag, and bentonite, where ratio is 4-6:2-3:6-8. The residual strain is plant or plant tissue of sweet potato, cucumber, and Chinese cabbage abandoned in fields at ratio of 5:2:2. The biogas is anaerobic fermentation of crushed semi-solid corn stalk powder and chicken manure at ratio of 4:1.    USE - Culture substrate used for cultivating cabbage seedling.    ADVANTAGE - The culture substrate reduces production cost and environment pollution and has economic, social, and ecological benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of vegetable stump comprising pulverizing vegetable, where carbon/nitrogen ratio is 24-26 and moisture content is 59-61%, adding 0.5% viable cells 2x 109 cfu/g compost inoculant, and fermenting.
NOVELTY - Soil modifying agent comprises more than 25 %mass silicon powder, 0.1-0.8 %mass petrochemical powder, 6.6-8.2 %mass amino acid powder, 10.2-16.2 %mass phosphoric acid salt, 12.7-14.8 %mass potassium dihydrogen phosphate, 12.8-18.9 %mass ammonium sulfate, 12.8-17.4 %mass peat, 11.4-20.8 %mass shell powder, 9.7-14.6 %mass calcium carbonate and and 3.8-8.2 %mass serpentine powder.    USE - The soil modifying agent is useful for high fat green paddy (claimed).    ADVANTAGE - The soil modifying agent can be decomposed by microorganisms, can be completely restored to the original agricultural land softly, and enables to produce high-quality agricultural products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the soil modifying agent, which involves (a) fermenting silicon powder, petrochemical powder and amino acid powder at 10 degrees C for 3 days, (b) mixing the semi-finished product with phosphoric acid salt and potassium dihydrogen phosphate, and (c) fermenting the mixture with ammonium sulfate, peat, shell powder, calcium carbonate and and serpentine powder at more than 10 degrees C for 15 days.
NOVELTY - Cultivation material for Agaricus, comprises 58-68 %mass wild rice stem and leaf sheath, 20-30 %mass cow dung, 8 %mass rapeseed, 2 %mass lime powder, 1 %mass superphosphate, 1 %mass gypsum powder, and 100 %mass dry matter.    USE - As cultivation material for Agaricus (claimed).    ADVANTAGE - The cultivation material is high in yield of Agaricus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the cultivation material, which involves (a) mixing wild rice stockpiles and leaf sheath with 2% lime, mixing mixture with water, accumulating the mixture for 2 days, at the same time stacking the mixture before 2 days, spray-drying the cow dung, mashing the mixture, evenly mixing the mixture, and pre-compacting heap, (b) covering concrete floor with 15-20 cm thick water bamboo leaf sheath, covering with a layer of cow dung, stacking layer of leaf sheath and cow dung, sealing the top cover real cow dung, where piling to a height of 1.5-1.8 m and width of 2.3-2.5 m, completing accumulation, adding suitable amount of water, inserting a stick to every 1-15 cm, interlinking to form a channel up and down, increasing amount of gas exchange stockpile inside and outside, and obtaining secondary fermentation product, and (c) turning the mixture for interval of 5, 4, 3, 2, and 1 days and totally turning for 4 times, plunging leaf sheath material into the pile next to the center, adding gypsum powder into the mixture, adding crushed superphosphate powder to the mixture, adding rapeseed and water to the mixture, fermenting the mixture, and obtaining product with 63-65% moisture content.
NOVELTY - Preparation of water hyacinth organic fertilizer comprises drying fresh water hyacinth sample, crushing, adding mineral fertilizer, composting at height of 0.5-1 m, covering, attaching mercury thermometer in middle and bottom, sprinkling bacteria, fermenting, monitoring temperature, maintaining water content at 50-70% for 3-4 days, stabilizing at 35-45 degrees C, stacking for 7 days, drying, crushing, sieving, screening and packaging.    USE - Method for preparing water hyacinth organic fertilizer (claimed).
NOVELTY - A tobacco seedling matrix comprises 60-75 wt.% decomposed sawdust and 40-25 wt.% tobacco seedling floating culture medium.    USE - Tobacco seedling matrix.    ADVANTAGE - The matrix meets YC/T310-2009, satisfies normal tobacco growth, reduces cost of tobacco seedlings and production cost, increases economic benefits, and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of tobacco seedling matrix comprising uniformly mixing decomposed sawdust and tobacco floating seedling substrate, where the decomposed sawdust is prepared by sieving sawdust, adjusting water content to 50-60%, adding fertilizer and organic material, uniformly mixing, stacking, piling, fermenting at 60-75 degrees C for 15-30 days, where fertilizer is 1.4 kg nitrogen and 0.8 kg phosphorus in 100 kg saw dust and mass of organic matter in 100 kg saw dust is 200-500 g.
NOVELTY - A water hyacinth organic fertilizer comprises 30-70 wt.% dry water hyacinth, 0.01-0.5 wt.% biological bacteria, 20-40 wt.% peat, and 1-5 wt.% mineral fertilizer.    USE - Water hyacinth organic fertilizer.    ADVANTAGE - The fertilizer greatly shortens production time, reduces costs, and has fast and good fermentation process both at high and low temperatures.
NOVELTY - A fruit trees fertilizer comprises 62-70 wt.% fresh chicken manure, 5-7 wt.% alpha -naphthalene sodium acetate, 4-7 wt.% humic acid, 6-10 wt.% nitrogen fertilizer, 8-15 wt.% phosphorus pentoxide, 8-15 wt.% potassium hydroxide, 2-5 wt.% calcium phosphate, and 3-5 wt.% fermentation strains.    USE - Fruit trees fertilizer.    ADVANTAGE - The fertilizer has low price and simple fertilization method, promotes growth of roots, branches, and flowering of fruit trees, and enhances drought tolerance effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer by adding water to fresh chicken manure until moisture content is 60-70%, mixing fermentation strains, and stirring in fermentation tank; fermenting to 85-95 degrees C, dispersing, naturally drying until water content is 30-40%, and adding into second fermentation tank; fermenting to 85-95 degrees C, dispersing, naturally drying until water content is 20-30%, and adding into third fermentation tank; fermenting to 60-75 degrees C, dispersing, continue fermenting for 3-5 days to obtain crude fertilizer; adding alpha -naphthalene sodium acetate, nitrogen fertilizer, phosphorus pentoxide, potassium hydroxide, calcium phosphate and humic acid, and continuously fermenting for 1-2 days; slightly drying until moisture content is less than 15%, screening, and removing impurities; and drying to room temperature, adding water until water content is less than 5%, pulverizing, granulating, and packaging.
NOVELTY - An Agaricus blazei cultivation material comprises 45-55 wt.% sugarcane leaves, 25-35 wt.% cow dung, 15 wt.% wheat bran, 2 wt.% lime powder, 1 wt.% superphosphate, 1 wt.% urea, and 1 wt.% gypsum powder.    USE - Agaricus blazei cultivation material.    ADVANTAGE - The material has reasonable ratio, balanced nutrition, high yield of up to 7.8-9.2 kg/m2, and harmless treatment of sugarcane leaves, allows mycelium to absorb simpler substances, and promotes growth.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (A) preparation of material by (i) cutting sugarcane leaves into 30-40 cm long, adding lime powder, irrigating for 2 days while spraying with cow dung, crushing, and uniformly mixing; (ii) placing bamboo sticks on concrete floor, stacking with layer by layer of 15-20 cm sugarcane leaves and cow dung, dissolving urea in water, pouring into stacked pile, covering with cow dung to obtain 1.5-1.8 m long, 2.3-1.8 m wide, and less than 5 m length heap, inserting 15 cm sticks, removing bamboo sticks forming vertical and horizontal channels, increasing amount of gas exchange inside and outside for microbial activity, and fermenting; and (iii) turning heap at intervals of 7,6,5,4, and 3 days for a total turning of 4 times for 23-25 days, adding gypsum powder/first turning, superphosphate/second turning, and wheat bran/third turning, adding water depending on water content of heap, and stopping fermentation when moisture content is 63-65%; and (B) cultivation of Agaricus blazei by spreading cultivation material into bed frame, cooling, sowing seedlings, sprouting, and fruiting.
NOVELTY - A rabbit manure fermentation fertilizer comprises 5-15 pts. wt. rabbit dung, 0.1-0.4 pts. wt. zinc sulfate, 0.01-0.05 pts. wt. effective microorganism bacteria liquid, and 50-90 pts. wt. water.    USE - Rabbit manure fermentation fertilizer used for increasing zinc content of crops, particularly millet, rice, or wheat (all claimed).    ADVANTAGE - The fertilizer is environment-friendly, can increase zinc, lysine, and soluble protein and sugar contents of crops, improves quality of crops, removes plant insects and pests, saves production costs, and has variety of fertilization effects.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer by anaerobically fermenting rabbit manure compost for 5-20 days, and turning once every 3-5 days while keeping temperature to 50-70 degrees C; diluting with water, dropping effective microorganism bacteria liquid, fermenting for 2-4 days, filtering to obtain solid residue and mixed fertilizer liquor; and adding liquor with zinc sulfate and stirring to dissolve.
NOVELTY - Preparation of oxibendazole comprises carrying out concentrated sulfuric acid-catalyzed nitration of m-dichlorobenzene, alkali neutralizing, and washing organic layer with water to obtain 2,4-dichloronitrobenzene; adding an amination reagent to obtain 2-nitro-5-chloroaniline; carrying out alkali metal salt condensation of 2-nitro-5-chloroaniline and n-propanol to obtain 2-nitro-5-propoxyaniline; carrying out catalytic hydrogenation or formaldehyde-hydrazine reduction to obtain 4-propoxy-1,2-phenylenediamine; and carrying out cyclization.    USE - Method for the preparation of oxibendazole (claimed).    ADVANTAGE - The method is simple, and is environment-friendly.
NOVELTY - Preparation of (S)-4-benzyl-3-propionyl-2-oxazolidinone (I) comprises dissolving (2S)-2-amino-3-phenylpropanoic acid in an organic solvent I, adding a reducing agent to carboxyl group, reacting at 30-70 degrees C for 3-8 hours, filtering, removing solvent, and re-crystallizing; mixing with an organic solvent II and diethyl carbonate, and reacting at 60-120 degrees C for 1-5 hours; and reacting with an organic solvent III at - 10-0 degrees C, mixing, reacting for 20-60 minutes, dripping acid chloride at - 10-0 degrees C, reacting at 15-50 degrees C for 3-8 hours, filtering, removing solvent, and re-crystallizing.    USE - Method for the preparation of (S)-4-benzyl-3-propionyl-2-oxazolidinone (I) (claimed).    ADVANTAGE - The method is environment-friendly, has a process yield more than 90%, and has a total yield is more than 70%.    DETAILED DESCRIPTION - Preparation of (S)-4-benzyl-3-propionyl-2-oxazolidinone of formula (I) comprises:    (A) dissolving (2S)-2-amino-3-phenylpropanoic acid in an organic solvent I, stirring and isolating oxygen, adding a reducing agent to the carboxyl group, reacting at 30-70 degrees C for 3-8 hours, stopping reaction, filtering, removing solvent, and re-crystallizing to obtain (2S)-2-amino-3-phenyl-1-propanol;    (B) mixing (2S)-2-amino-3-phenyl-1-propanol, an organic solvent II, and diethyl carbonate, microwave heating, reacting at 60-120 degrees C for 1-5 hours, filtering the reaction liquid, removing the solvent, and passing through a chromatographic column; and    (C) reacting with an organic solvent III at - 10-0 degrees C, mixing in the absence of oxygen, adding strong base, reacting for 20-60 minutes, dripping acid chloride at - 10-0 degrees C, reacting at 15-50 degrees C for 3-8 hours, filtering, removing solvent, and re-crystallizing.
NOVELTY - A nitrogen-containing 1-benzothiophene derivative (I) is new.    USE - Nitrogen-containing 1-benzothiophene derivative in the form of foliar or soil pesticide used for preventing and treating plant disease, particularly powdery mildew, rice blast, corn rust, cucumber and grape downy mildew, and cucumber anthracnose (claimed).    ADVANTAGE - The biodegradable fungicidal composition has high efficiency, broad spectrum, and low toxicity.    DETAILED DESCRIPTION - A nitrogen-containing 1-benzothiophene derivative of formula (I) is new.    R1-R4=H, halo, trihalomethyl, 1-4C alkyl, 1-4C alkoxy, 1-4C alkylthio, nitro or cyano;    R5=H, 1-4C alkyl, 3-6C cycloalkyl or optionally substituted phenyl; and    Q=benzene derivative of formula (a)-(e).    INDEPENDENT CLAIMS are included for:    (1) preparation of compound (I); and    (2) fungicidal composition comprising 1-99 wt.% compound (I) and carrier.
NOVELTY - Preparation of amikacin comprises using kanamycin A and hexamethyl disilazane as raw materials, silylation reacting while protecting the hydroxy and amino groups of kanamycin A to obtain methyl silyl kanamycin A, taking gamma -phthalimido-imino- alpha -hydroxybutanoic acid and N-hydroxyphthalimide as raw materials, dehydration reacting in N,N-dicyclohexylcarbodiimide to obtain active ester, and subjecting active ester and methyl silyl kanamycin A to acylation, hydrolysis, and hydrazinolysis to obtain the product.    USE - Preparation of amikacin (claimed).    ADVANTAGE - The method shortens the reaction time to 2 hours, is easy to operate and environment-friendly, shortens the siliconizing reaction to 1 hour, while improving subsequent acylation reaction selectivity, and improves the yield.    DETAILED DESCRIPTION - Preparation of amikacin comprises using kanamycin A and hexamethyl disilazane as raw materials, silylation reacting while protecting the hydroxy and amino groups of kanamycin A to obtain methyl silyl kanamycin A, taking gamma -phthalimido-imino- alpha -hydroxybutanoic acid and N-hydroxyphthalimide as raw materials, dehydration reacting in N,N-dicyclohexylcarbodiimide to obtain active ester, and subjecting active ester and methyl silyl kanamycin A to acylation, hydrolysis, and hydrazinolysis to obtain the product. The first step comprises micronizing ammonium sulfate to a granularity d0.1 of less than or equal to 1 mu m, d0.9 of less than or equal to 10 mu m, taking kanamycin A, adding hexamethyl disilazane and micronized ammonium sulfate, silylation reacting at 40-100 degrees C, and evaporating to dryness to obtain methyl silyl kanamycin A.
NOVELTY - A composite extraction agent comprises potassium pyrophosphate solution and potassium hydroxide solution. The composite extraction agent is prepared by mixing 300 ml of 0.25 mol/L potassium pyrophosphate solution and 700 ml of 1 mol/L potassium hydroxide solution.    USE - Composite extraction agent used in extraction of humic acid from sewage sludge (claimed) used in liquid fertilizer for landscaping and gardening.    ADVANTAGE - The composite extraction agent allows simple and fast extraction of humic acid with easy operation at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for extraction of humic acid from sewage sludge, comprising:    (A) dehydrating sludge from municipal sewage treatment plant at 100-105 degrees C for 8-10 hours, then naturally cooling to room temperature, and crushing to 0.25 mm mesh to obtain dry sludge sample having water content of less than 5%;    (B) adding dry sludge with composite extraction agent at room temperature, oscillating and extracting for 1 hour, standing for 8-12 hours, and separating supernatant to obtain humus slurry; and    (C) adding humus slurry with 1.2-1.4 mol/L nitric acid solution and uniformly mixing, standing and depositing, separating to obtain supernatant, adding supernatant with 1 mol/L potassium hydroxide solution until the sediment is completely dissolved to obtain brown humic acid solution.
NOVELTY - A nitromethane (II) is reacted with formaldehyde, to obtain nitro ethanol (III). The obtained substituted nitro ethanol is reacted with bisulfite in the presence of base, to obtain nitro ethanesulfonate (IV). The obtained compound is reduced and acidified, to obtain taurine (I).    USE - Preparation of taurine used in pharmaceutical field.    ADVANTAGE - The taurine is efficiently and easily prepared.    DETAILED DESCRIPTION - A nitromethane of formula: CH3NO2 (II) is reacted with formaldehyde, to obtain nitro ethanol compound of formula (III). The obtained substituted nitro ethanol is reacted with bisulfite in the presence of base, to obtain nitro ethanesulfonate of formula (IV). The obtained compound is reduced and acidified, to obtain taurine of formula (I).    M=alkali metal or ammonium ion.
NOVELTY - Method for preparing androstenedione by biotransformation, circulation and recycling of edible oil, involves settling and separating biotransformation reaction liquid of androstenedione to obtain oil phase containing cells and product of liquid-solid-solid three-phase reaction liquid, adding organic solvent A to the liquid-solid-solid three-phase reaction liquid, performing centrifugal separation, processing, adding organic solvent B to the obtained liquid-solid two-phase system B, processing and performing biotransformation of obtained oil phase B.    USE - The method is useful for preparing androstenedione by biotransformation, circulation and recycling of edible oil (claimed).    ADVANTAGE - The method is cost-effective and environmentally-friendly, and reduces edible oil waste discharge by 75%.    DETAILED DESCRIPTION - Method for preparing androstenedione by biotransformation, circulation and recycling of edible oil, involves obtaining biotransformation reaction liquid of androstenedione as raw material, extracting androstenedione and recycling edible oil, by (a) settling and separating biotransformation reaction liquid of androstenedione to obtain oil phase containing cells and product of liquid-solid-solid three-phase reaction liquid, adding organic solvent A to the liquid-solid-solid three-phase reaction liquid, and converting the three-phase reaction liquid into liquid-solid two-phase reaction solution, (b) performing centrifugal separation of the liquid-solid two-phase reaction liquid to obtain the androstenedione, and removing the oil phase A, (c) forcibly evaporating the oil phase A to remove solvent A, forming liquid-solid two-phase system B, and adding organic solvent B to the liquid-solid two-phase system B to obtain oil phase B containing extract of androstenedione, and (d) forcibly evaporating the oil phase B to remove organic solvent B, and performing biotransformation of oil phase B to obtain product.
NOVELTY - Method for producing vermicompost organic fertilizer using biological bacteria involves processing microorganism treatment stage and biological treatment stage, where the microorganism processing stage is breeding microbial in sludge and performing fermentation process and biological treatment stage is subjecting fermented product to earthworm bed, where the earthworm utilizes organic matter and heavy metal, and earthworm manure is collected.    USE - The method is useful for producing vermicompost organic fertilizer using biological bacteria. The biological organic fertilizer is used for processing animal dung into organic manure, feed, food, medicine and daily chemical raw material (all claimed).    ADVANTAGE - The biological organic fertilizer comprises antagonistic microorganisms, and can restrain soil-borne disease.
NOVELTY - Method for preparing organic fertilizer, involves mixing mushroom waste, yellow whey and essential microorganism bacteria in a weight ratio of 100:50-80:1-2, inoculating essential microorganism in the raw materials, sealing the mixture, anaerobically fermenting the mixture at 20-50 degrees C for 15-20 days, and drying the fermented mixture to moisture content of below 15%.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The method consumes minimal energy, recycles wastewater, exhibits edible fungi material degradation rate, is environmentally-friendly, simple and rapid, and requires minimal floor space.
NOVELTY - The deodorant has an inclined plane stored in a row of sulfur oxide thiobacillus. A spherical bud holding bacillus strain is inoculated corresponding to a liquid culture medium, where temperature of a triangular bottle ranges from 28-30 degrees Celsius. Plant extraction liquid is provided with biological deodorizing liquid.    USE - High temperature composting deodorant for use in bio-filtering tower.    ADVANTAGE - The deodorant is simple and convenient, and has better effect, and avoids pollution.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a high temperature composting deodorant application    (2) a high temperature deodorant composting method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a high temperature composting deodorant.'(Drawing includes non-English language text)'
NOVELTY - This utility new type claims a one containing sulphide waste water catalytic oxidation reactor, belonging to the sewage treatment device technology field, aiming at solving the problems of processing waste water containing sulphide complex structure device, sewage processing effect of. Using of it is filled up reactor is provided with catalyst packed bed, a catalyst filling bed is filled with height as the catalyst of 0.8 to 1.2 m of catalytic oxidation reactor, the waste water collecting tank of waste water lifting pump of the coupled waste water conveying tube connecting to catalytic oxidation reactor top, a catalytic oxidation reactor in the catalyst filler bed lower part is set with a fan connecting pipe of aeration, catalytic oxidation reactor is further connected with a hydrogen peroxide dosing mechanism of oxidant transporting tube, overflow port and flow up the reactor top is connected with processing water discharge tube, processing water discharge tube connecting with the processing water collecting pool connected with. The structure is simple and practical, which is suitable for treatment of petroleum chemical industry, dye, pesticide, medicine and so on containing sulphide waste water.
NOVELTY - Residual dimethylformamide and sewage are collected, and additive is added to residual dimethylformamide, and toxic element is removed. Composite microbial flora is added to sewage mixture, mixture is placed in anaerobic reactor, and fermented. The residual toxic elements are removed, and chemical oxygen demand of initial feed sewage is controlled. The resulting mixture is incubated, fermented, and methane and biogas are separated. Biogas is introduced into storage tank, desulfurized and combusted. The obtained slurry is oxidized, obtained biogas residue is filtered, and dried.    USE - Utilization method of distillation residue of synthetic leather (claimed).    ADVANTAGE - The method economically utilizes distillation residue of synthetic leather, by a simple process.    DETAILED DESCRIPTION - Residual dimethylformamide and slaughter sewage are collected using specific container, and additive is added to the residual dimethylformamide and slaughter sewage, toxic element is removed, and pH is adjusted to 7-9. Composite microbial flora is added to sewage mixture, stirred, the resulting mixture is placed in anaerobic reactor, and fermentation is carried out. The residual toxic elements are removed, and the chemical oxygen demand of initial feed sewage is controlled to 5000-10000. The resulting mixture is incubated in anaerobic reactor, fermented, and methane and biogas are separated. Biogas is introduced into the storage tank, desulfurized, and combusted. The obtained slurry is introduced into contact oxidation tank, and aerobic-facultative treatment is carried out. The biogas residue is entered into pressure filter, and biomass is dried. The weight ratio of residual dimethylformamide and slaughter sewage to additive is 1:10-100:0.001.
NOVELTY - A fertilizer is prepared by mixing compost, crushed seaweed, chicken manure and water, and stirring at 28 degrees C.    USE - Method for preparing fertilizer used for Chinese cabbage seedling (claimed).    ADVANTAGE - The method is cost-efficient and environment-friendly.
NOVELTY - Biofertilizer used for straw comprises organic material and composite nutrient solution at weight ratio of 2-4:1, prepared by mixing organic material and composite nutrient solution, fermenting at 40-50 degrees C for 15-20 days, deodorizing, detoxifying, granulating at 40-60 degrees C, and packing.    USE - Biofertilizer used for straw (claimed).    ADVANTAGE - The biofertilizer has drought resistance rate of 10-15%, straw maturity for 5-7 days and yield of not less than 10%. It has stable structure, low cost, high input-output ratio, and easy preparation and application.
NOVELTY - Biofertilizer comprises 20-26 wt.% tobacco stems, 19.5-25.5 wt.% feather, 14-26.3 wt.% meat and bone powdered mixture, 15-20.1 wt.% scrap wood, 13-20.3 wt.% rice straw and 0.1-0.2 wt.% composite bacteria.    USE - Biofertilizer used for rice farming (claimed).    ADVANTAGE - The biofertilizer has high organic matter content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biofertilizer comprising mixing raw materials except for composite bacteria, fermenting, stirring, stacking for 1-3 days, decaying for 28-32 days at room temperature, drying at 28-40 degrees C, crushing, fermenting at room temperature, adding composite bacteria, composting for 8-10 days, mixing, granulating, and stirring.
NOVELTY - Fertilizer comprises 10-20 pts. wt. peanut cake, 100-200 pts. wt. excrement and 5-7 pts. wt. calcium superphosphate. The fertilizer is prepared by performing fermentation. The weight ratio of the excrement and peanut cake is 10:1. The fertilizer has not less than 16% phosphorus pentoxide of calcium superphosphate.    USE - The fertilizer is useful for mustard plant (claimed), and promoting growth of mustard plant.    ADVANTAGE - The fertilizer provides semitransparent and bright mustard with favorable taste and crispiness as compared with existing fertilizer, is cost-effective, and improves economic benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) uniformly mixing loess and sand in a weight ratio of 60-70:30-40, (b) uniformly mixing the above-mentioned components to obtain mixed material, and adding the mixed material in fermentation tank, and (c) adding the mixture obtained in the step (a) to the tank, covering the tank with thin film, sealing the tank, performing fermentation for 30-35 days, and turning the mixture for 2-3 times during fermentation to obtain product.
NOVELTY - Method for preparing Chinese cabbage seedlings substrate, by (a) crushing vegetable after adjusting the carbon and nitrogen content and water content, (b) inoculating viable bacteria and fermenting to obtain vegetable compost, (c) crushing corn straw, (d) mixing crushed corn straw and chicken manure, adding water and stirring uniformly to obtain paste, and adding anaerobic species, stirring uniformly, and heating the mixture and fermenting the mixture, and (e) mixing stone powder, vegetable compost, residue and vermiculite, mixing uniformly, and adjusting the pH.    USE - The method is useful for preparing Chinese cabbage seedlings substrate (claimed).    ADVANTAGE - The substrate improve physical and chemical properties of cabbage seedlings, is cost-effective and reduce environmental pollution.    DETAILED DESCRIPTION - Method for preparing Chinese cabbage seedlings substrate, involves (a) crushing vegetable after adjusting the carbon and nitrogen content and water content to 58-62%, (b) inoculating 0.5 %mass 2x 109 colony forming unit/g or more viable bacteria and fermenting to obtain vegetable compost, (c) crushing corn straw to 1-2 cm, (d) mixing crushed corn straw and chicken manure, adding water and stirring uniformly to obtain paste, and adding 0.1 %mass anaerobic species, stirring uniformly, and heating the mixture at 28 degrees C and fermenting the mixture, and (e) mixing stone powder, vegetable compost, residue and vermiculite in a ratio of 3:4;3, mixing uniformly, and adjusting the pH to 6.6-6.8.
NOVELTY - 1-Phenyl-3-methyl-5-pyrazolone and dimethyl sulfate are methylated at high temperature, and hydrolyzed, to obtain hydrolysis solution. 1-Phenyl-3-methyl-5-pyrazolone and dimethyl sulfate are subjected to methylation reaction at high temperature, hydrolyzed, and subjected to alkali treatment, to obtain antipyrine oil. The hydrolysis solution and antipyrine oil are mixed with water, to obtain antipyrine quaternary ammonium sulfate solution comprising 33-37% antipyrine and 9-12% sulfuric acid. Product is subjected to nitrosation and reduction, and cooled, to obtain 4-aminoantipyrine.    USE - Preparation of 4-aminoantipyrine (claimed).    ADVANTAGE - The 4-aminoantipyrine is prepared with high yield by simple and environmentally-friendly method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for 4-aminoantipyrine production device, which consists of primary pyrazolone storage hopper, primary dimethyl sulfate metering tank, primary methylation tank, primary hydrolysis tank, alkali treatment tank, primary antipyrine oil storage tank, secondary pyrazolone storage hopper, secondary dimethyl sulfate metering tank, secondary methylation tank, secondary hydrolysis tank, secondary antipyrine oil storage tank, tertiary water metering tank, antipyrine quaternary ammonium sulfate configuration tank, nitrosation reaction tank, sodium nitrite metering tank, nitrosation tank, reduction reaction tank, hydrolysis neutralization tank and caustic metering tank.
NOVELTY - Methyl benzaldehyde is subjected to radical reaction with 1,3-dibromo-5,5-dimethylhydantoin 40-90 degrees C in an organic solvent and initiator, to obtain 4-(bromomethyl)benzaldehyde. The obtained product is reacted with imidazole in dipolar aprotic solvent under the action of accelerator at room temperature. To obtain 4-(1-imidazolyl)benzaldehyde. The resulted product is reacted with acetic anhydride in eutectic solvent at 20-50 degrees C, to obtain ozagrel.    USE - Preparation of ozagrel (claimed).    ADVANTAGE - The ozagrel is prepared by economical, simple and environmentally-friendly method without using column chromatography.
NOVELTY - For inhibiting rice false smut, fusaric acid is used. The indoor experiment includes use hypha growth rate method and spore germination inhibiting method to determine the inhibitory strain of fusaric acid and spore germination of concentration EC5tl value.    USE - For inhibiting rice false smut; for preventing and treating of smut which is chemical bactericide, useful in the production of medicine.    ADVANTAGE - The fusarium acid is agricultural antibiotics, has strong inhibiting effect, good preventing and treating effect, and has no harm to human and livestock and does not kill natural enemy, and safety and environment friendly, long lasting time, which is good for ecological balance and stable.
NOVELTY - Treating a digestate extracted from a methanization plant digestion tank, comprises (a) mixing at least one liquid fraction of the digestate with an essential inorganic material containing a substantial amount of clay, zeolite and/or diatomaceous earth for a duration sufficient to allow the material to at least partially trap ionized ammonia nitrogen contained in the digestate, and (b) separating the solid fraction from the mixture.    USE - The method is useful for treating a digestate extracted from a methanization plant digestion tank in the production of a fertilizer composition (all claimed).    ADVANTAGE - The method is capable of simply, reliably and economically treating the digestate extracted from the methanization plant digestion tank without any environmental risk, and avoids the disturbance of enzymatic, microbial and/or bacterial action within the digester.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a unit for treating a digestate extracted from the methanization plant digestion tank comprising a unit for mixing the liquid fraction of the digestate with the essential inorganic material containing a substantial amount of clay, zeolite and/or diatomaceous earth for a duration sufficient to allow the material to at least partially trap ionized ammonia nitrogen contained in the digestate, and a unit for separating the solid fraction from the mixture.    DESCRIPTION OF DRAWING(S) - The diagram shows a flow chart of a method for treating a digestate from a methanization plant digestion tank.    Separating the liquid fraction of the digestate from the solid fraction by filtration (11)    Discharging 1000 l of liquid fraction into a mixing tank containing clinoptilolite type zeolite (12)    Separating the solid fraction of the mixture from the liquid fraction of the mixture (13)    Mixing solid fraction of digestate with the solid fraction of the mixture. (14)
NOVELTY - Biofuel oil contains 40-60 wt.% used edible oil refined oil, 40-60 wt.% petroleum-based kerosene products, and 0.05-2 wt.% additives.    USE - Biofuel oil composition for diesel engines, boiler, thermal power generation, cogeneration, and heating (all claimed).    ADVANTAGE - Oxidation and deterioration of biofuel oil products are prevented. The cleaning agent cleans deposit adhering to the spark plug of a diesel engine, an injector, an injection plug, or an air-intake valve using biofuel oil products as fuel of diesel engine. An engine upgrade, reduction of exhaust gas, and improvement of fuel consumption are achieved. Dispersing agent adsorbs moisture to improve the stability of mixed used edible oil refined oil and kerosene products. Abrasion resistance is excellent. The biofuel oil is equivalent to petroleum-based light oil products in physical property, and emitted-heat amount. Generation amount of global warming gas carbon dioxide (CO2) is half of the CO2 generation amount of petroleum.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biofuel oil composition obtained by removing free fatty acids and free glycerol in used edible oil by adsorption separation using activated clay consisting of 75-85% silica (SiO2), 9-13% alumina (Al2O3), 1-2% iron(III) oxide (Fe2O3), and 1-3% magnesium oxide (MgO) having a particles size of 100-200 mesh or 200-300 mesh, activating by heating and drying at 150 degrees C for 3 hours, adding 3 wt.% used edible oil, stirring at 50-60 degrees C for time 30- 40 minutes, and separating refined oil and waste clay using a filter.
NOVELTY - Degrading biomass or pretreated biomass to sugars comprises using an enzyme.    USE - The method is used for degrading biomass or pretreated biomass to sugars (claimed).    ADVANTAGE - Improved enzymes for feed and food processing applications are provided.    DETAILED DESCRIPTION - Degrading biomass or pretreated biomass to sugars comprises using an enzyme is used comprising a polypeptide having (i) a polypeptide sequence as set forth in any one of SEQ ID NOs: 3, 6, 9, 12, 15, 18, 21, 23, 25 and 27; (ii) a polypeptide that is at least 60%, preferably at least 70-99% homologous to the any one of SEQ ID Nos: 3, 6, 9, 12, 15, 18, 21, 23, 25 and 27; (iii) a polypeptide sequence encoded by nucleic acids sequence of SEQ ID NOs: 1, 2, 4, 5, 7, 8, 10, 11, 13, 14, 16, 17, 19, 20, 22, 24 and 26 or nucleic acids that are at least 60%, preferably at least 70-99% homologous to any one of SEQ ID NOs: 1, 2, 4, 5, 7, 8, 10, 11, 13, 14, 16, 17, 19, 20, 22, 24 and 26; (iv) a polypeptide sequence encoded by a nucleic acids sequence hybridizing under stringent conditions to the polynucleotide of SEQ ID NOs: 1, 2, 4, 5, 7, 8, 10, 11, 13, 14, 16, 17, 19, 20, 22, 24 and 26; or (v) a polypeptide sequence encoded by a nucleic acids sequence hybridizing under stringent conditions to the reverse complement of a polynucleotide of SEQ ID NOs: 1, 2, 4, 5, 7, 8, 10, 11, 13, 14, 16, 17, 19, 20, 22, 24 and 26. Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication.
NOVELTY - Fuel composition comprises a grain component comprising a non-petroleum plant based fuel, an oxidizer reactant operable to remove electrons from the grain component during combustion for oxidizing the grain component, and a fuel adhesive component configured to bond molecules from the fuel composition. The grain component is operable to release a vapor during combustion. The vapor is operable to enhance a combustion.    USE - The fuel composition such as biofuel is useful in a combustive assembly including laquer vehicle generation system engine, a combustion engine, a diesel engine, and a burner.    ADVANTAGE - The fuel composition provides a renewable biofuel energy source for reducing dependence on fossil fuels, enhances the air quality by reducing carbon monoxide emission during combustion, and has high stability and long shelf life.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composition comprising means for combusting the fuel composition, means for adding the grain component to the fuel composition, means for adding the oxidizer reactant to the fuel composition for oxidation, means for adding a fuel adhesive to the fuel composition for enhancing stability of the fuel composition, means for premodifying the grain component through saturation, means for adding a ball fuel formula to the fuel composition for enhancing fuel life, means for combusting the fuel composition in a chamber modulator, means for releasing a vapor, means for enhancing the combustion, and means for powering a vehicle.
NOVELTY - Apparatus (I) comprises: feeding trough set; piston feeding device, connected to the feeding trough set; horizontal high temperature high pressure reactor set, connected to the piston feeding device; high temperature pressure difference flash discharge device, connected to the horizontal high temperature high pressure reactor set; flash trough set, connected to the high temperature pressure difference discharge device; flashed steam heat-recycling system connected to the flash trough set; and a solid-liquid separation device, connected to the flash trough set.    USE - The apparatus is useful for continuously processing lignocellulosic material (claimed), and plant applications such as rice straw, sugarcane residue, Japanese silver grass, bamboo, Napier grass, and wheat straw.    ADVANTAGE - The apparatus is simultaneously and continuously operated, thus providing xylose hydrolysate by hydrolyzing hemicellulose, destroying the structure of the biomass material, and increasing surface area and porosity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus (II) comprising: feeding trough set; feeding device, connected to the feeding trough set; horizontal low temperature low pressure acid mixing pre-heating set connected to the feeding device; vertical high temperature high pressure reactor set, connected to the piston feeding device; high temperature pressure difference flash discharge device, connected to the horizontal low temperature low pressure acid mixing pre-heating set; high temperature pressure difference flash discharge device the vertical high temperature high pressure reactor set; flash trough set, connected to the high temperature pressure difference discharge device; flashed steam heat-recycling system connected to the flash trough set; and solid-liquid separation device, connected to the flash trough set.
NOVELTY - Formulation comprises prasugrel free base.    USE - The formulation is useful for preventing or treating thrombosis and cardiovascular diseases.    ADVANTAGE - The formulation can be simply and economically prepared with improved production yield and storage stability and high bioavailability and in a time-consuming and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the formulation, comprising (a) mixing a part of all excipients except for the active agent in a container to form mixture A and the remaining part in a separate container to form a mixture B, (b) mixing prasugrel free base with mixture A and then mixing the resulting mixture with mixture B, and (c) converting the mixture into a suitable dosage form and then packaging.
NOVELTY - Biogas reactor comprises: container with an encircling cylindrical wall; and two reel agitators, where the shafts of the two reel agitators are oriented parallel to each other. A cylinder axis is present that is perpendicular to the shafts and surrounded by the cylindrical wall. The container comprises a first container for preservation of beer extending from one shaft to the other shaft, and a second container for preservation of beer extending up to inner side of the wall.    USE - Used as a biogas reactor.    ADVANTAGE - The biogas reactor: is efficient in mixing and fermenting; can be produced in a simple and inexpensive manner; and exhibits enhanced agitating efficiency.    DETAILED DESCRIPTION - Biogas reactor comprises: container with an encircling cylindrical wall; and two reel agitators, where the shafts of the two reel agitators are oriented parallel to each other. A cylinder axis is present that is perpendicular to the shafts and surrounded by the cylindrical wall. The container comprises a first container for preservation of beer extending from one shaft to the other shaft, and a second container for preservation of beer extending up to inner side of the wall. The arrangement of the shafts in the container is in a manner so that A/2 is Kx B, where K is a factor having a value of greater than 1.    DESCRIPTION OF DRAWING(S) - The figure shows a plan view of the biogas reactor.    Container (1)    Wall (2)    Support (5)    First reel agitator (6)    Second reel agitator (7)
NOVELTY - The method involves burning char i.e. fixed carbon, with air such that a thermal medium is heated. The char is transduced into a fluidized-bed-combustion tower (120) with the thermal medium. The thermal medium is returned to a fluidized-bed-tar reforming tower (130) and a fluidized-bed-gasification tower (110) through cyclone such that temperature of the tar reforming tower and the gasification tower are maintained. Volatile matter, gasifying gas and water vapor are transduced into the tar reforming tower.    USE - Method for gasifying coal/biomass by a three-tower type circulating fluidized bed.    ADVANTAGE - The method enables decomposing coal tar such that the tar does not precipitate into pipes, so that prolonged continuous operation can be attained, thus operating the combustion tower and the tar reforming tower for long time in an efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a three tower type circulating fluidized bed gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a three-tower type gasifier.'(Drawing includes non-English language text)'    Fluidized-bed-gasification tower (110)    Fluidized-bed-combustion tower (120)    Fluidized-bed-tar reforming tower (130)    Heat exchanger (140)    Dust collector (150)
NOVELTY - An ethanol is manufactured by dissolving a cellulose raw material to cellulose solvent containing amine and obtaining dissolution regenerated cellulose, decomposing dissolution regenerated cellulose using cellulose decomposition agent and obtaining glucose, and making glucose react and obtaining ethanol.    USE - Manufacture of ethanol for supplying energy in production business or processing industry.    ADVANTAGE - Ethanol is efficiently manufactured from cellulose contained in a biomass.
NOVELTY - Method is carried out by converting bioethanol at a first step on a zeolite catalyst containing iron, at temperature of 300-350 degrees C and volume rate of 2 h-1 on liquid starting ethanol, then at a second step by hydrogenating the obtained product of converting ethanol on an industrial 3% or 5% platinum-containing catalyst at temperature of 250-300 degrees C for 1.5-3 hours in an autoclave with periodic supply of hydrogen, followed by distillation of the hydrogenation product and separating the end product, which boils off at temperature higher than 135 degrees C, with density of not less than 790 kg/m3 at 20 degrees C and containing naphthenic products.    USE - Chemistry.    ADVANTAGE - Method enables to obtain reactive biofuel for aircraft gas-turbine engines, which is more environmentally friendly compared to traditional fuels.1 dwg, 2 tbl
NOVELTY - The apparatus has a first chamber (1A) containing water and potassium hydroxide catalyst, where current is applied to electrolysis plates in presence of the water and potassium hydroxide catalyst to cause chemical reaction. A second chamber (2A) catches hydrogen released from the chemical reaction. A return tube allows water to drain back into the first chamber, where successive epoxy electrodes are provided from center diminish in size, and outer edges of the electrodes are covered with electrically resistive material. A circulation pump (9) causes water and hydrogen to rise.    USE - Apparatus for producing cleaner/dryer hydrogen gas used during fuel augmentation support system operation for a vehicle.    ADVANTAGE - The apparatus ensures complete ignition of fuel to improve fuel efficiencies such that improved/decreased fuel consumption makes a fuel augmentation support system to be useful for long-distance vehicles or stationary engines running constantly and water consumption can be reduced, thus providing prolonged functional life span to the electrolysis plates and minimizing maintenance requirements of the apparatus, while eliminating a requirement for operator interventions during the fuel augmentation support system operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view a fuel augmentation support system.    Chambers (1A-1C, 2A-2C)    Circulation pump (9)    Moisture collection chamber (25)    Distilled water reservoir (31)    Filler pump (38)
NOVELTY - Compact fire log having a longitudinal extent from end-to-end, a midsection, a lower part, an upper surface, a side surface and a lower surface, comprises one or more longitudinally extending, end-to-end incisions to it, where the incisions intersect in the log's midsection and fail to extend to the log's side surface; and an air duct, in the lower part of the log that extends from the log's side surface to the midsection of the log.    USE - The compact fire log is useful in fireplace or at campsite; and for making grill coal.    ADVANTAGE - The fire log burns from the inside out and the flame exits the log from the upper end similarly to a candle, preserving the log's decorative outer surface for nearly the entire burning period. During burning, a flaming star shape is formed in the middle of the log. The fire log is comfortable to use, easy to take along and requires no additional procedures prior to use. In the open air, the log does not require any additional support for using a pot or a pan. The fire log burns significantly longer and gives more warmth than a Lapland candle.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of forming a compact fire log involving cutting a wood log from a tree trunk, where the wood log has a longitudinal extent from end-to-end, a midsection, a lower part, an upper surface, a side surface and a lower surface; forming one or more longitudinally extending end-to-end incisions in the wood log, where the incisions intersect in the wood log's midsection and do not extend to the wood log's side surface; and forming an air duct in the lower part of the wood log, where the air duct extends from the wood log's side surface to the midsection of the wood log.
NOVELTY - The water purification apparatus comprises a condensed waste water reservoir, an oil separator, a wastewater discharging unit, a water storage tank, an anaerobic digester to generate methane gas, and a purification unit. The methane gas is fed to a heating device for generating steam or a heating medium for heating the organic waste.    USE - The apparatus is useful for purifying water contaminated with food waste, livestock waste and sewage sludge.    ADVANTAGE - The apparatus provides high purity water without the contamination of microorganism.
NOVELTY - Manufacture of solid fuel involves baking paper sludge at 170-350 degrees C where obtained solid fuel has concentration 10% or less.    USE - Manufacture of solid fuel used for powdered coal boiler.    ADVANTAGE - The method enables manufacture of solid fuel having high yield and excellent grindability.
NOVELTY - The system has a control unit triggering a direct current (DC)/DC converter. Electricity of a battery is supplied to an external load through the DC / AC converter. A fuel cell unit generates the electricity in a stack that includes the external load. Power offset value of the stack is greater than consumption power value of the external load, where the consumption power value is generated from the stack. Power supply of the stack to the external load is blocked when power offset of the battery is lesser than power offset of the stack.    USE - Fuel cell system for use with a high-capacity electrical machinery.    ADVANTAGE - The system is convenient to use, and independently drives the external load due to electricity of the battery based on discharge electricity and stack electricity of the battery.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for driving a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel cell system.'(Drawing includes non-English language text)'
NOVELTY - The apparatus has a reboiler that supplies thermal energy to gas-liquid separator that separates condensed water supplied to regenerator (27). A flash drum (33) evaporates the ejected lean amine in lower portion of regenerator, and generates vapor. A compressor (28) compresses the vapor generated from flash drum into the vapor of high pressure and high temperature. A heat exchanger lowers the regeneration absorbent in which carbon dioxide supplied from regenerator with a pump (25) at the temperature of absorptive tower level is removed, supplied to an absorptive tower (23).    USE - Apparatus for treating acidic gas such as carbon dioxide, methane, hydrogen sulfide and carbonyl sulfide in coal fired power plant.    ADVANTAGE - The generation of high temperature blazing fire and corrosion in flash drum can be prevented by heat-exchanging. The gas-liquid separation efficiency under the identical decompression condition can be enhanced by enhancing the driving temperature of the flash drum and by increasing the premise steam generation. The steam of high temperature is not immediately injected by the regenerator so that the stream amount used at the regenerator is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for treating acidic gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for treating acidic gas.    Absorptive tower (23)    Pump (25)    Regenerator (27)    Compressor (28)    Flash drum (33)
NOVELTY - Producing a treated biomass material, comprises irradiating a biomass material by passing an electron beam through multiple windows into the biomass material.    USE - The method is useful for producing treated biomass material (claimed), which is used as fuel.    ADVANTAGE - The method: reduces the recalcitrance of the biomass material; is safer, facilitates more robust processing while providing the treated biomass material with high yields, and incurs less down time from failure of foil windows; utilizes the multiple window systems that greatly reduce the likelihood of primary window failure/implosion, which can destroy expensive accelerator parts; reduces the production of toxic by-products, when compared to conventional processes; and enables the cooling of foil windows with a high flow rate of cooling gas without disturbing the material targeted for irradiation. The gap between window foils allows for the beam stop to be removable placed between the windows.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a system for cooling multiple single-type window foils of an electron beam accelerator, comprising a first flow path for providing a first cooling gas across a primary single-type window foil (510) and second flow path for providing a second cooling gas across a secondary single-type window foil, where the primary and secondary single-type window foils (530) are positioned with a gap of less than 9 cm between them; and    (2) cooling multiple single-type window foils of an electron beam accelerator, comprising passing a first cooling gas across the primary single-type window foil and passing a second cooling gas across the secondary single-type window foil.    DESCRIPTION OF DRAWING(S) - The figure shows a cross-sectional view of two foils window extraction system for scanning electron beam.    Biomass (444)    Primary single-type window foil (510)    Outlet (514)    Inlet (516)    Secondary single-type window foil (530)
NOVELTY - The system has a stack equipped with a fuel anode and an air electrode, and a purge valve arranged in a purge line. A drain valve is arranged in a drain line, and a water trap collects condensed water generated in the fuel anode. An air supplying part supplies air of the air blower to an air electrode through an air supply line. The purge valve purges reaction less hydrogen to an inlet of the air electrode. The drain valve ejects the condensed water and reaction less hydrogen to the humidifier.    USE - Fuel cell system.    ADVANTAGE - The system recycles the thrown away reactionless hydrogen, and improves OCV reduction speed and the durability capacity of the fuel cell stack. The system can reduce the operation end time and indirectly improve the continued ratio.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel cell system purging method.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic circuit diagram of a fuel cell system.
NOVELTY - Sintered refractory product comprises a granulate bound by a matrix comprising: greater than 40 wt.% of chromium oxide (Cr2O3); less than 50 wt.% of aluminum oxide (Al2O3); greater than or equal to 1 wt.% of zirconium oxide (ZrO2), where 20 wt.% of ZrO2 is stabilized in cubic and/or quadratic form; greater than or equal to 0.1 wt.% of yttrium oxide (Y2O3) acting as a stabilizer of ZrO2; and less than 1.9 wt.% of hafnium oxide HfO2. A total content of oxides of chromium, aluminum and zirconium is greater than 70 wt.%.    USE - The sintered refractory product is useful for coating an inner wall of a reactor of a gasifier (claimed) that is useful to gasify coal, petroleum coke, biomass, wood, charcoal, and heavy oils.    ADVANTAGE - The sintered refractory product has corrosion resistance and thermal shock resistance thus improving the lifetime of the inner wall of the reactor of the gasifier.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a gasifier including a reactor having an inner wall partially coated by a refractory coating comprising the sintered refractory product; and    (2) manufacturing the sintered refractory product, comprising preparing a load comprising the matrix, casting the load in a working mold by vibration and/or pressing and/or ramming of the load inside the mold so as to form a preform, releasing the preform from the mold, drying the preform under air or atmosphere controlled moisture so that the residual moisture of the preform is 0-0.5%, and firing the preform under an oxidizing atmosphere at a temperature of 1300-1600 degrees C so as to form the sintered refractory product.
NOVELTY - The method involves providing a sludge drawing-out portion (L4) which draws out precipitation sludge, and stirs inside of a methane fermentation tank (2). The process target waste water introduced into the methane fermentation tank is stirred, after the methane fermentation process is carried out in one predetermined time. A stirring apparatus (22) is stopped and the stirring stop process is performed in another predetermined time. The sludge drawing-out process of drawing out sludge from the sludge drawing-out portion is performed after the stirring stop process.    USE - Operating method of methane fermentation apparatus for use in waste water treatment.    ADVANTAGE - The sludge concentration in the tank is highly maintained, when drawing out precipitation sludge from the methane fermentation apparatus. Hence methane fermentation process can be performed efficiently. Since energy can be collected from the waste water, the environmental load of the waste water can be reduced efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a methane fermentation apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane fermentation apparatus.    Methane fermentation tank (2)    Processing tank (20)    Stirring apparatus (22)    Stirring blade (22a)    Sludge drawing-out portion (L4)
NOVELTY - A polymer electrolyte membrane (10) comprises a porous laminated film (20) and polymer electrolyte with which the laminated film is filled. The polymer electrolyte contains the acidic group, the laminated film contains a porous contact bonding layer arranged between a porous first film membrane (11), a porous second film membrane (12), the contact bonding layer (13) comprises PTFE, the elongation rate of film membrane differs by a direction.    USE - Polymer electrolyte membrane for manufacturing fuel cell (claimed).    ADVANTAGE - The polymer electrolyte membrane has high heat resistance, durability    DETAILED DESCRIPTION - A polymer electrolyte membrane comprises a porous laminated film and polymer electrolyte with which the laminated film is filled. The polymer electrolyte contains the acidic group chosen from disulfonyl compound (-SO2NHSO2-), sulfonyl-carbonyl compound (-SO2NHCO-) and dicarbonyl compound (-CONHCO-), the laminated film contains a porous contact bonding layer arranged between a porous first film membrane, a porous second film membrane, the contact bonding layer comprises PTFE, the elongation rate of film membrane differs by a direction, and the angle which direction from which elongation rate of a second film membrane becomes direction from which elongation rate of a first film membrane becomes the minimum with the minimum forms may exist in the range of 45-90 degrees . An INDEPENDENT CLAIM is also included for a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a polymer electrolyte membrane.    Electrolytic membrane (10)    First film membrane (11)    Second film membrane (12)    Contact bonding layer (13)    Laminated film (20)
NOVELTY - Gene recombinant yeast comprises acetyl xylan esterase gene, xylose reductase gene, xylitol dehydrogenase gene, xylulokinase gene, beta -xylosidase gene, endoxylanase gene, and arabinofuranosidase gene in which genes contained in gene recombinant yeast are introduced by chromosomal integration. Gene recombinant yeast can produce ethanol from xylo-oligosaccharide.    USE - Gene recombinant yeast for manufacture of ethanol (claimed).    ADVANTAGE - The gene recombinant yeast is not easily influenced by fermentation inhibitor and enables production of ethanol with high efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) classification method of gene recombinant yeast which involves introducing beta -xylosidase gene, endoxylanase gene, arabinofuranosidase gene, acetyl xylan esterase gene, xylose reductase gene, xylitol dehydrogenase gene, and xylulokinase gene into yeast by chromosomal integration, producing gene recombinant yeast, irradiating ion beam to gene recombinant yeast, and subculturing gene recombinant yeast in culture medium containing fermentation inhibitor to classify strain that can produce ethanol from xylo-oligosaccharide with high efficiency; and    (2) manufacture of ethanol which involves saccharifying hemicellulose contained in cellulose biomass by hydrothermally processing cellulose biomass to 5 carbon saccharide, saccharifying cellulose contained in cellulose biomass by hydrothermally processing cellulose biomass to 6 carbon saccharide, concentrating 5 carbon saccharide liquid and 6 carbon saccharide liquid, fermenting concentrated 5 carbon saccharide liquid and 6 carbon saccharide liquid by gene recombinant yeast, and producing ethanol.    DESCRIPTION OF DRAWING(S) - The drawing shows a conceptual diagram of the function of gene recombinant yeast MN8140/XXAAII. (Drawing includes non-English language text).
NOVELTY - Method for preparing sugar liquid from cellulose-comprising biomass, involves (a) fermenting 0.1-50 wt.% cellulose-comprising biomass comprising starch raw material, and (b) subjecting the fermented mixture to solid-liquid separation and hydrolysis, filtering the mixture using ultrafiltration membrane, collecting filamentous fungus-derived cellulase as non-permeate and obtaining sugar liquid from the filamentous fungus-derived cellulase.    USE - The method is useful for preparing sugar liquid from cellulose-comprising biomass which is useful for preparing chemical substance (claimed), and as sugar materials for various fermentation product.    ADVANTAGE - The method improves reusability of filamentous fungi origin cellulase, and reduces amount of usage of filamentous fungi.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing chemical substance, which involves fermenting the obtained sugar solution by culturing the microorganisms having capability to produce chemical substance from the sugar liquid.
NOVELTY - Device for mounting and maintaining stirrers (5) for biogas fermenter (1), is claimed. The device is designed as a crane basket for mounting a hook of a mobile crane. The crane basket is designed such that it can take at least one person. A winch is provided on the crane basket.    USE - The device is useful for mounting and maintaining stirrers for biogas fermenter.    ADVANTAGE - The device: is easy to use; and is produced and maintained in a cost efficient manner; and comprises locking means for agitators, thus it prevents sinking down of the device during repair work.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the arrangement of the stirrers in the fermenter.    Fermenter (1)    Wall (2)    Supporting structure (3)    Stirrers (5)    Stand (6)
NOVELTY - Aerosol composition comprises (a) a cosmetic preparation comprising at least one solidifying agent, and (b) a blowing agent mixture comprising 1,1-difluoroethane, and at least one second blowing agent comprising propane, propylene, n-butane, isobutane, isobutene, n-pentane, pentene, isopentane or isopentene. The 1,1-difluoroethane is present at 0.5-10 wt.%. The second blowing agent is present at 3-6 wt.%.    USE - The aerosol composition is useful for temporarily remodeling keratin fibers (claimed).    ADVANTAGE - The aerosol composition exhibits improved humidity resistance, low stickiness and high conditioning effect.
NOVELTY - Producing biogas in a solid fermenter (20, 22), comprises stream flowing the stackable biomass from a percolate for producing biogas in a fermentable process, and controlling the fermentable process based on the quality of the produced biogas, or supplying stackable biomass with percolate for producing biogas in the fermentable process, and regulating the supply of the biomass with the percolate based on the quality of the produced biogas.    USE - The method is useful for producing biogas in solid fermenter.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device (1) for producing biogas, comprising at least one solid fermenter for receiving stackable biomass.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device for producing biogas.    Device (1)    Solid fermenter (20, 22)    Percolate nozzles (44, 46)    Sensor (80, 82)    Controller (84)
NOVELTY - Device for torrefying biomass, comprises a feeding device (1) for feeding the biomass to the device, a hollow shaft (3) having a conveying device for conveying the biomass to an upper part of the device, torrefaction floors #(7, 7', 7'') which are present outside the hollow shaft, and are suitable for downwards sinking of the biomass from the upper part, and a flue gas supply pipe (11) for supplying flue gas such that the biomass is torrefied by the flue gas during conveying to the upper part of the device and/or during sinking through the torrefaction floors.    USE - The device is useful for torrefying biomass (claimed).    ADVANTAGE - The device requires less energy, conveys the produced exhaust gas to the combustion chamber of a power plant, and thus it reduces environmental pollution, is simple, and can be easily inertized, operated and monitored.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for torrefying the biomass, comprising feeding the biomass into the device for torrefaction, supplying flue gas into the device, conveying the biomass in the hollow shaft, into the upper part of the device for torrefaction, by the conveying device, carrying out floor-wise sinking of the biomass downwards from the upper part of the device outside the hollow shaft, through several torrefaction floors, and torrefying the biomass by the flue gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device and the method for torrefying biomass.    Feeding device (1)    Hollow shaft (3)    Bucket conveyor (5)    Torrefaction floors (7, 7', 7'')    Flue gas supply pipe (11)
NOVELTY - Controlling a torrefaction plant for biomass, comprises: continuously measuring at least one auxiliary parameter; indirectly determining current degree of torrefaction of the biomass from the auxiliary parameters; comparing the current degree of torrefaction of the biomass with a predetermined set value of the degree of torrefaction; and controlling the torrefaction plant so that the current degree of torrefaction of the biomass coincide with the predetermined set value of the degree of torrefaction.    USE - The method is useful for controlling a torrefaction plant for biomass (claimed).    ADVANTAGE - The method controls the torrefaction plant for biomass with less consumption of energy and less effort in a simple and environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for controlling the torrefaction plant for biomass, comprising at least one measuring device for the continuous measurement of the auxiliary parameters of the biomass and/or smoke- and/or exhaust gas, a device for indirect determination of the current degree of torrefaction of the biomass from the auxiliary parameters, a device for comparing the current degree of torrefaction of the biomass with the predetermined target value of the degree of torrefaction, and a control device (8) of the torrefaction plant so that the current degree of torrefaction of the biomass coincide with the predetermined target value of the degree of torrefaction.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a device for torrefaction of biomass.    Torrefaction tower (2)    Hollow shaft (3)    Bucket conveyor (5)    Floors (7)    Core. (14)
NOVELTY - Torrefying biomass, comprises pretorrefaction of biomass in a first device (10) to a first degree of torrefaction to the pretorrefied biomass, and comminution, final torrefaction and homogenization to a second degree of torrefaction in a second device (20) to a finished torrefied biomass.    USE - The method is useful for torrefying biomass (claimed).    ADVANTAGE - The method is capable of easily, effectively and economically torrefying the biomass with less consumption of energy in an environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for torrefying the biomass, comprising the first device for the pretorrefaction of biomass to a biomass of the first degree of torrefaction, and the second device for comminution, final torrefaction and homogenization of the biomass to a biomass of the second degree of torrefaction.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a device for the torrefaction of biomass.    First device (10)    Second device (20)    Rotor (22)    Outdoor screens (23)    Discharge port. (24)
NOVELTY - Generating a natural gas substitute containing methane from a feed gas containing carbon dioxide, comprises: subjecting the feed gas to a methanization reaction; dividing the product from the methanization reaction by a gas separator into a retentate gas containing methane and a permeate gas containing hydrogen; recycling at least a portion of the permeate gas to the feed gas and mixing to form the educt gas for the methanization reaction. A hyper-stoichiometric hydrogen content is set in the educt gas for the methanization reaction.    USE - The method is useful for generating a natural gas substitute containing methane from a feed gas containing carbon dioxide (claimed).    ADVANTAGE - The method is simple and compensates the catalyst aging phenomena in an improved manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a device (3) for generating a natural gas substitute containing methane from a feed gas containing carbon dioxide, comprising a methanation reactor (4) for obtaining a product gas from a supplied feed gas, a gas separation device (6) for separating the product gas, a permeate gas recirculation to the inlet side of the methanization reactor and to the local blending of the permeate gas for feed gas to form the educt gas, and a control or regulating device for the controlled or regulated setting of hyper-stoichiometric hydrogen content; and    (2) an energy supply system with a hydrogen generation device (2) for generating hydrogen and a biomass conversion plant (1) a carbon dioxide/carbon monoxide source for supplying carbon monoxide-containing gas, and the above mentioned device    DESCRIPTION OF DRAWING(S) - The figure shows is a schematic block diagram of a power supply system with the device (Drawing includes non-English language text).    Biomass conversion plant (1)    Hydrogen generation device (2)    Device (3)    Methanation reactor (4)    Gas separation device (6)
NOVELTY - One of agriculture and forestry waste resources comprehensive utilization production system, relating to agriculture and forestry waste resource efficient comprehensive utilization technical field, comprising a first-stage separating device in turn connecting of separating hemicellulose, second level separating device, separating cellulose and three level separating device, separating lignin, a first-stage separating device further connecting with anaerobic fermentation device, anaerobic fermentation device connecting said marsh gas generating device. This utility new type of used raw material is agriculture and forestry waste, raw material resources, wide distribution, the cost is low, the agriculture and forestry waste resource to obtain the high-efficient comprehensive utilization. This utility new type can be prepared by biochemical lignin, cellulose, marsh gas power and biomass forming fuel such as product, high yield, environment-friendly benefit.
NOVELTY - This utility new type relates to for countryside of domestic sewage purifying device, especially one kind of can solve the rural sewage is directly discharged sewage purifying tank three-layer structure results in the problem of environmental pollution. For vast rural areas lacking simple and feasible, low in cost of sewage treatment device, the amount of domestic sewage discharging randomly around river and pond pollution environment, and it is harmful to human body health of technical problem, this utility new type provides one three-layer structure sewage purifying tank, comprising a tank body of one top surface opening, the side wall of the upper part is provided with a drain hole, wherein said of inner cavity of the bath is provided in the plant layer, an absorption layer and gravel layer, vegetable layer is composed of floating plant, biological floating band absorbing layer, gravel layer is paved crushed stone of the groove body bottom is piled up. This utility new type has simple structure, small investment, fast effect, and does not need power, operation is simple, it can completely change rural domestic sewage can not reach the standard of discharging.
NOVELTY - This new type utility claims one marsh ecological treatment system, comprising a water collecting device, a solid-liquid separating device, precipitation acidification regulating reservoir, mud soft anaerobic tank, liquid storage tank, a steam-water separator, a desulfurizing tower, mud soft storage bag, a pressurizing device, the stored-pressure jar and fire retardant cleaning distribution device is provided with a constant-pressure device between the soft mud anaerobic tank and steam-water separator is provided with a pressure relief device between the desulfurizing tower and red mud storage soft bag. This utility new type by using solid-liquid separation technology and anaerobic fermentation technology, firstly the excrement sewage into dry dung and fecal sewage, dung processed into organic fertilizer, organic fertilizer can be directly to the crop, fertilizing, fecal sewage the anaerobic ferment produce marsh gas and biogas, biogas can be used for power generation, cooking, can be used for irrigating crops and trees. This utility new type and general marsh gas system lies in the excrement sewage by fermenting produce the marsh gas, through the solid-liquid separation to produce organic fertilizer.
NOVELTY - Novel ecological environment-friendly device, its structure relation is: storage bin, storage bin and a crusher by conveyer belt connecting the crusher with the adjusting tank is composed of a transmission belt connecting, preparing tank is connected with the anaerobic tank by a conveying pipe connecting, at the same time, the dirt collection device with the adjusting tank is composed of a delivery pipe connecting, excrement device and the dirt drain device of feed delivery pipe connecting, anaerobic tank are respectively connecting the feed delivery pipe and the biogas tank, tank, the anaerobic tank by a gas pipe connected with the gas connecting device, an anaerobic tank is composed of hot water pipeline with the marsh gas hot water boiler connecting the gas storage device and the pressurizing pump is composed of a connecting gas pipe, a pressurizing pump is connected with the constant pressure tank is composed of gas pipe connecting, constant pressure tank is composed of gas pipe is respectively connected with the fuel gas device, marsh gas hot water boiler connecting the seal tank is connected with slurry tank, biogas device of feed delivery pipe connecting the domestic sewage discharging device and the water collection tank by connecting pipe, water tank and purifying device by the connecting pipe.
NOVELTY - Fuel ethanol is produced by pressing sweet sorghum to obtain juice, mixing alcohol yeast with 30 degrees C warm water, activating for 1-2 hours, adjusting total sugar concentration of juice to 17-20%, adding auxiliary agent and 0.1-0.2% active dry yeast, fermenting at 18-33 degrees C for 45-60 hours, distilling with simple ethanol distillation tower, and distilling with continuous multi-stage distillation tower.    USE - Production of fuel ethanol (claimed).    ADVANTAGE - Production of fuel ethanol is environment-friendly and reduces production cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart for the production of fuel ethanol. (Drawing includes non-English language text).
NOVELTY - Fuel ethanol is fermented by mixing 100 g/L glucose, 8-10 g/L yeast powder, and nutrients, shaking culturing at 30 degrees C and 100 rpm for 10-20 hours to obtain seed culture medium, mixing 100 g/L glucose, 3-5 g/L yeast powder, 3-5 g/L peptone, and nutrients, adjusting pH to 6, and performing high-pressure steam sterilizing at 115 degrees C for 15 minutes to obtain fermentation culture medium, and mixing 86 g/L inositol, 35 g/L vitamin B1, 0.5 g/L vitamin B2, 0.5 g/L niacin, 0.67 g/L paraaminobenzoic acid, 350 ml pantothenic acid, and 0.0024 g/L vitamin H to obtain mixed vitamin solution.    USE - Fermentation of fuel ethanol (claimed).    ADVANTAGE - Fermentation of fuel ethanol increases ethanol concentration productivity, and equipment utilization, reduces water, electricity, and gas consumption, and inhibits growth of bacteria.    DETAILED DESCRIPTION - Fuel ethanol is fermented by mixing 100 g/L glucose, 8-10 g/L yeast powder, and nutrients, shaking culturing at 30 degrees C and 100 rpm for 10-20 hours to obtain seed culture medium, mixing 100 g/L glucose, 3-5 g/L yeast powder, 3-5 g/L peptone, and nutrients, adjusting pH to 6, and performing high-pressure steam sterilizing at 115 degrees C for 15 minutes to obtain fermentation culture medium, mixing 86 g/L inositol, 35 g/L vitamin B1, 0.5 g/L vitamin B2, 0.5 g/L niacin, 0.67 g/L paraaminobenzoic acid, 350 ml pantothenic acid, and 0.0024 g/L vitamin H to obtain mixed vitamin solution, inoculating 5-15 ml seed culture medium and 1 ml filter-sterilized mixed vitamin solution, controlling fermentation shaking flask liquid volume at 110 ml, and fermenting in 38 degrees C water bath with shaking speed of 100-150 rpm.
NOVELTY - Tannin is removed from acorn kernel by washing acorn kernel, mixing with water with material:water ratio of 1:20-1:40, grinding to obtain slurry, mixing, performing ultrasonic treatment with ultrasonic frequency of 20-60 kHz, power of 300-600 W, and feed temperature of 20-40 degrees C for 30-60 minutes to extract, and measuring tannin content through spectrophotometer.    USE - Removal of tannins from acorn kernel for fuel ethanol production (claimed).    ADVANTAGE - Removal of tannins from acorn kernel improves alcohol conversion rate.
NOVELTY - Fuel ethanol is produced by forming slurry from corn flour, adding alpha -amylase, glucoamylase, and Saccharomyces cerevisiae high active dry yeast, fermenting in automatic fermenter, distilling, and dehydrating in which alcohol degree of fermented mash is determined using densitometer.    USE - Production of fuel ethanol (claimed).    ADVANTAGE - Production of fuel ethanol is simple, does not require stewing or cooling steps, and reduces consumption of steam and water, labor intensity, and production cost.
NOVELTY - Fuel ethanol is produced from molasses by adding auxiliary material to honey, sterilizing, adjusting pH to 6, sending saccharified material to multi-stage continuous flow fermentation tank, using semi-continuous fermentation process control, adding immobilized yeast in proliferation tank, maintaining mash temperature at 28-35 degrees C and yeast count at greater than or equal to 0.8 million/m3, adding to each segmentation tank, fermenting for 65-72 hours, and distilling with 3 linked working towers e.g. crude distillation tower, aldehyde distillation tower, and rectifying tower at 82-85 degrees C.    USE - Production of fuel ethanol from molasses (claimed).    ADVANTAGE - Production of fuel ethanol from molasses uses waste as raw material.    DETAILED DESCRIPTION - Fuel ethanol is produced from molasses by adding auxiliary material to honey, sterilizing, adjusting pH to 6, sending saccharified material to multi-stage continuous flow fermentation tank, using semi-continuous fermentation process control, adding immobilized yeast in proliferation tank, maintaining mash temperature at 28-35 degrees C and yeast count at greater than or equal to 0.8 million/m3, adding to each segmentation tank, fermenting for 65-72 hours, and distilling with 3 linked working towers e.g. crude distillation tower, aldehyde distillation tower, and rectifying tower at 82-85 degrees C in which crude distillation tower discharge has alcohol purity of 35%, aldehyde distillation tower discharge has alcohol purity of 80%, and rectifying tower discharge has alcohol purity of 95%.
NOVELTY - An acorn kernel starch raw material fermentation for producing fuel alcohol is processed by selecting acorn seeds, removing shell, grinding, removing tannins, forming acorn starch, performing enzyme treatment, inoculating, fermenting, distilling to obtain fuel ethanol, placing 100 ml solution in distillation flask, adding 100 ml distilled water, uniformly mixing, distilling, collecting 100 ml distillate, measuring alcoholic strength of alcohol at 20 degrees C using alcohol meter, and calculating conversion rate of alcohol.    USE - Acorn kernel starch raw material fermentation for producing fuel alcohol (claimed).    ADVANTAGE - The fuel alcohol product resolves energy crisis and has wide prospect.    DETAILED DESCRIPTION - An acorn kernel starch raw material fermentation for producing fuel alcohol is processed by selecting acorn seeds, removing shell, grinding, removing tannins, forming acorn starch, performing enzyme treatment, inoculating, fermenting, distilling to obtain fuel ethanol, placing 100 ml solution in distillation flask, adding 100 ml distilled water, uniformly mixing, distilling, collecting 100 ml distillate, measuring alcoholic strength of alcohol at 20 degrees C using alcohol meter, and calculating conversion rate of alcohol, i.e. dividing product of alcohol by volume and alcohol by starch and multiplying by 100 to get rate percentage.
NOVELTY - A lawn grass saccharifying and fermenting process is performed by removing impurity on lawn grass, drying, cutting to 3 cm, smashing, passing to 60 items sieve, collecting powder, pretreating with alkali to remove lignin in which solid-to-liquid ratio is 1:20-1:40, saccharifying grass, diluting cellulase and pectinase to obtain hydrolysis liquid, filtering hydrolysis liquid to obtain saccharified liquid with fermentable sugar, adding yeast to saccharified liquid, adding auxiliary agent, fermenting, filtering fermentation liquid, and rectifying obtained filtrate to obtain fuel ethanol.    USE - Lawn grass saccharifying and fermenting process for producing fuel ethanol (claimed).    ADVANTAGE - The process is simple, has low cost, fully makes use of lawn grass, and obtains fuel ethanol which is environment-friendly.    DETAILED DESCRIPTION - A lawn grass saccharifying and fermenting process is performed by removing impurity on lawn grass, drying, cutting to 3 cm, smashing, passing to 60 items sieve, collecting powder, pretreating with alkali to remove lignin, saccharifying grass in which solid-to-liquid ratio is 1:20-1:40, diluting cellulase and pectinase 80-100 times to obtain hydrolysis liquid, filtering hydrolysis liquid at 60 mesh nylon filter cloth, 50 degrees C and 120 rpm to obtain saccharified liquid with fermentable sugar, adding 0.2-0.4% yeast to saccharified liquid, adding auxiliary agent, fermenting at 28-35 degrees C in fermentation tank for 30-45 hours, filtering fermentation liquid, and continuously rectifying obtained filtrate in multi-stage rectifying tower to obtain fuel ethanol.
NOVELTY - A fermented straw is pretreated by crushing wheat straw using crusher to obtain slag with 1 cm length, soaking crushed slag in degrading solution for 24 hours, transferring degraded straw in boiler, heating to boil for 5-10 hours, filtering, and washing until neutral.    USE - Pretreatment process of fermented straw for producing ethanol (claimed).    ADVANTAGE - The process is simple and convenient to use, improves conversion efficiency, and has conventional reagent and instrument.
NOVELTY - A composite agent comprises 8-10 parts high-temperature-resistant alpha -amylase, 80-100 pts. wt. glucoamylase, 30-40 pts. wt. pullulanase, 15-20 pts. wt. cellulase, 8-15 pts. wt. acid protease, 15-25 pts. wt. pectinase, 15-20 pts. wt. inulinase, 5-10 pts. wt. beta -glucanase, 3-6 pts. wt. beta -mannase, 5-15 pts. wt. xylanase, 3-5 pts. wt. phytase, and 80-90 pts. wt. high-temperature-resistant dry yeast.    USE - A composite agent for fermenting Jerusalem artichoke into fuel ethanol (claimed).    ADVANTAGE - Fermentation using composite agent is simple, short and low-cost and has high conversion efficiency.
NOVELTY - The method involves entering return liquid into sewage anaerobic zone (1) from anoxic zone (2). Reflux liquid is entered into anoxic zone from aerobic zone (3). Degradation and absorption of nitration and phosphorus of ammonia of organic matter is removed from aerobic area. High sludge concentration of residual sludge is discharged to sludge concentrating tank. Flow pushing type diving stirrer is installed in anaerobic area and anoxic zone.    USE - Annular membrane biological reactor sewage treatment method.    ADVANTAGE - Biological reactor sewage treatment process can be easily ensured, engineering investment can be reduced and consumption of energy can be saved.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the annular membrane biological reactor sewage treatment process. (Drawing includes non-English language text)    Anaerobic zone (1)    Anoxic zone (2)    Aerobic zone (3)    Water passing hole (19)    Air lifting device (25)
NOVELTY - Ecological restoration of eutrophic water body, by performing sedimentation of sewage in secondary settling tank of sewage treatment plant, where the secondary settling tank comprises sewage and activated sludge, adding obtained anaerobic microorganisms to aquatic culture containing aquatic plants, performing culturing process, allowing formation of microbial film, performing pretreatment process of river water for removing large particles floating on the surface of the water, and allowing cultured aquatic plants to grow in pre-treated river water.    USE - Ecological restoration method of eutrophic water body (claimed).    ADVANTAGE - The method purifies and beautifies water body, improves self-purification ability of the water body, restores quality of water at a faster rate, does not causes secondary pollution, is cost-effective, and maintains stability of ecosystem of the water body for longer period of time.    DETAILED DESCRIPTION - Ecological restoration method of eutrophic water body, involves (a) performing sedimentation of sewage in secondary settling tank of sewage treatment plant, where the secondary settling tank comprises sewage and activated sludge to obtain anaerobic microorganisms, (b) adding the anaerobic microorganisms to aquatic culture containing aquatic plants, performing culturing process and allowing formation of microbial film, (c) performing pretreatment process of the river water for removing large particles floating on the surface of the water, and (d) allowing cultured aquatic plants to grow in pre-treated river water.
NOVELTY - Carrier comprises bacteria isolated from sewage waste, where the bacteria are attached to carrier.    USE - The carrier is useful for enriching microbe in domestic sewage waste (claimed).    ADVANTAGE - The carrier is capable of providing protease and lipase as it contains microbe, synergetically decomposes organic waste, and improves decomposition rate to 80%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for degrading sewage organic waste, which involves adding the above-mentioned carrier to the sewage.
NOVELTY - Treatment of municipal sewage using physical filtering process involves concentrating sewage to obtain nitrogen and phosphorus as useful component.    USE - Treatment of municipal sewage used as liquid fertilizer for agriculture.
NOVELTY - Producing biofuels, comprises adding oil-producing algae into a transparent solar cell, then adding urban sewage into domesticated medium, short-cycle training domesticating for 3-6 months, passing algae and natural auxiliary additives into domesticated municipal sewage, separation of proliferation of algae and water using hydrophilic microfiltration membrane under certain pressure, drying the filtrate, adding the starch and protein algae in residue, which is useful as animal feed. The natural auxiliary additive is a mixture of diatomaceous earth and struvite with a ratio of 1:1-3.    USE - The method is useful for producing biofuels (claimed).
NOVELTY - A resveratrol saponin is extracted by drying resveratrol glycoside of natural plant raw material, crushing, performing reflux extraction of raw material with organic solvent for 2-4 times and 2-4 hours per extraction time, filtering, combining filtrate, decompressing and concentrating filtrate at 40-80 degrees C to 1/8-1/12 times original volume and obtaining thick paste, mixing thick paste and silicon glue, uniformly mixing, drying , obtaining mixed silicon glue sample, subjecting to chromatography column, eluting, decompressing and concentrating at 40-80 degrees C, crystallizing, filtering, and drying.    USE - Extraction of resveratrol saponin (claimed).    ADVANTAGE - Extraction process is simple and environment-friendly and has low device requirement and production cost, short production period, and high product yield and purity.    DETAILED DESCRIPTION - A resveratrol saponin is extracted by drying resveratrol glycoside of natural plant raw material, crushing, performing reflux extraction of raw material with organic solvent for 2-4 times and 2-4 hours per extraction time, filtering, combining filtrate, decompressing and concentrating filtrate at 40-80 degrees C to 1/8-1/12 times original volume and obtaining thick paste, mixing thick paste and silicon glue, uniformly mixing, drying , obtaining mixed silicon glue sample, subjecting to chromatography column, eluting, collecting eluent, decompressing and concentrating at 40-80 degrees C to 1/18-1/22 of original volume, naturally cooling and crystallizing, filtering to obtain filter cake, and drying in which amount of organic solvent is 3-6 times raw material weight per extraction and amount of silicon glue is 1-1.5 times weight of thick paste.
NOVELTY - Preparing estra-4,9-diene-3,17-dione (III) comprises dissolving 19-hydroxy-4-androstene diketone (I) in an organic solvent, refluxing and dehydrating, adding acetate, refluxing till reaction is complete, and obtaining the biodegradable ester (II); and dissolving the biodegradable ester (II) in organic solvent, refluxing and dehydrating, then adding organic weak acid to the reaction to obtain estra-4,9-diene-3,17-dione (III).    USE - Method for preparing estra-4,9-diene-3,17-dione (claimed).    ADVANTAGE - The method has short synthesis route and high yield, and is environment-friendly.    DETAILED DESCRIPTION - Preparing estra-4,9-diene-3,17-dione of formula (III) comprises dissolving 19-hydroxy-4-androstene diketone of formula (I) in an organic solvent, refluxing and dehydrating, adding acetate, refluxing till reaction is complete, and obtaining the biodegradable ester of formula (II); and dissolving the biodegradable ester (II) in organic solvent, refluxing and dehydrating, then adding organic weak acid to the reaction to obtain estra-4,9-diene-3,17-dione (III).
NOVELTY - Device comprises biogas generator box body (1), temperature probe (2), heating device (3), thermostat (4), gas liquid container (5) and insulation layer.    USE - Device used for promoting fermentation.    ADVANTAGE - The device is simple in structure, convenient, economical and eco-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fermentation device.    Biogas generator box body (1)    Temperature probe (2)    Heating device (3)    Thermostat (4)    Gas liquid container (5)
NOVELTY - Botryococcus braunii ENN41 strain with the preservation number CGMCC N0.5149, is new.    USE - The strain is useful in producing biofuel including biohydrocarbon, biodiesel and biokerosene, producing pigment and animal feed, and in wastewater treatment, waste gas treatment and reducing carbon dioxide emission (all claimed).    ADVANTAGE - The strain produces large amount of hydrocarbon containing biomass, and has fast growth speed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for culturing Botryococcus braunii ENN41 strain, where the culture condition is as follows: the temperature is 20-35 degrees C, the illumination condition is 50-500 mu mol/m2x second, the pH is 7-9, and the carbon source is 0.5-10% carbon dioxide gas.
NOVELTY - Botryococcus braunii strain ENN42 having preservation number of CGMCC N0. 5509, is new.    USE - The Botryococcus braunii strain ENN42 is useful in the: production of bio-fuel, preferably biological hydrocarbons, biodiesel or bio-kerosene; and waste water treatment, waste gas treatment, and reduction of carbon-dioxide emission; and production of pigment, food or animal feed (all claimed).    ADVANTAGE - The Botryococcus braunii strain ENN42 has high biomass and hydrocarbon content, and rapid growth, and high culture density; and is suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for culturing Botryococcus braunii strain ENN42.
NOVELTY - Oil producing freshwater Chlorella sp. HQ with the preservation number CGMCC No.7601., is new. The Chlorella sp. HQ is obtained by isolating Botryococcus braunii, exposing to air, aging, and culturing in a culture medium.    USE - The freshwater Chlorella sp. HQ is useful for purifying water and producing oil (claimed).    ADVANTAGE - The Chlorella sp. HQ protects the environment, and is cultivated in large-scale under low cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) culturing Chlorella sp. HQ; and (2) use method of Chlorella sp. HQ for purifying water and producing oil, comprising providing secondary effluent of municipal sewage as culture medium, adding Chlorella sp. HQ, which continuously transforms the pollutants, and proliferating the single cells to accumulate oil, and simultaneously conducting deep water purification so as to protect the water resources.
NOVELTY - A long-chain polyhydroxyalkanoates (PHAmcl) is prepared by mixing polyhydroxyalkanoate (PHA) synthase gene phaC1 and recombinant engineered bacteria, fermenting by taking recombinant engineered bacteria as carbon source of fermentation medium, filtering, extracting using solvent 1, removing solvent, adding solvent 2, and recrystallizing.    USE - Preparation of long-chain polyhydroxyalkanoates for hydroxy fatty acid methyl esters long chain biofuel production (claimed).    ADVANTAGE - The method uses low cost cellulose as one of the raw materials, and PHA has high density, good combustion property, and is a good prospect to replace petroleum source.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of hydroxy fatty acid methyl esters (3HAME) long chain biofuel which involves mixing alcohol solvent, water, and long-chain polyhydroxyalkanoates (PHAmcl), adding catalyst, and reacting for 10-130 hours.
NOVELTY - A residual sludge production and dehydration is processed by preheating residual sludge at 35-60 degrees C, adding calcium oxide, stirring and mixing uniformly, naturally cooling to room temperature, adding polymeric ferric sulfate, stirring under anaerobic condition, anaerobically fermenting to obtain volatile fatty acid and dehydrated sludge, and anaerobically fermenting anaerobic sludge reflux as inoculum.    USE - Residual sludge production and dehydration process for removing nitrogen and phosphorus in sewage without carbon source and high-sludge sewage treatment plant.    ADVANTAGE - The process reduces sludge pretreating and medicine use cost and anaerobic methane production reaction, improves acid fermentation efficiency, reactor acid accumulation rate, and excess sludge dewatering performance, increases low-temperature heating sharply, sludge flocculation effect, and acid-producing bacteria, saves heat exchanger heating cost, and removes active phosphorus component.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a residual sludge production and dehydration device.
NOVELTY - This utility new type relates to one kind of hardly-degradable waste water processing device, specifically claims a Fenton treatment with plasma, microorganism of biological film-depositing iron and recycling hydrogen peroxide solution of the reaction device. This utility new type device comprises a contact glow multi-electrode plasma reactor, hydrogen peroxide content control system, depositing iron bio-film reaction tank. This utility new type is divided into three stages: the first stage is biological film forming stage, the second stage is hydrogen peroxide stage (primary treatment stage, the third stage is synergetic degradation pollutant. This utility new type recycling preliminary treatment of hydrogen peroxide produce and improve the economic benefit of the the hydrogen peroxide will pollute the environment, and it is harmful to human body health. In addition, plasma processing of rear surface of the carrier, produce polar functional group of, the surface of the carrier of the generally hydrophilic.
NOVELTY - Method for processing urban and rural waste, involves sorting urban and rural waste, adding waste into maggot cultivation room with fermentation tank, connecting heat supply system, adding fermenting agent, adding straw or sawdust, adjusting water content, stirring in the fermentation tank before anaerobic fermentation process, using prepared fermentation product as feed of earthworm maggot cultivation room cultivation process, and performing fly maggot cultivation of earthworm residue and fermenting the compost and drying product.    USE - The method is useful for processing urban and rural waste (claimed).    ADVANTAGE - The method is environmentally-friendly and harmless.    DETAILED DESCRIPTION - Method for processing urban and rural waste, involves (a) sorting urban and rural waste, recycling waste, combustible waste, organic waste, and other waste by sorting classifying process, where combustible and organic matter of waste are classified as combustible waste, and other waste and waste removing waste are recycled, (b) adding waste into maggot cultivation room with fermentation tank, and connecting heat supply system, (c) using smoke waste incinerator, (d) processing organic waste, crushing organic waste to obtain organic crushed product, adding fermenting agent, adding straw or sawdust, adjusting water content, and stirring in the fermentation tank before anaerobic fermentation process, (e) using prepared fermentation product as feed of earthworm maggot cultivation room cultivation process, and (f) performing fly maggot cultivation of earthworm residue and fermenting the compost by fermentation device and drying to obtain finished product.
NOVELTY - Method for preparing microorganism organic fertilizer, involves (a) culturing Trichoderma harzianum in culture medium, and performing fermentation using cultured strain to produce chlamydospore, where the T.harzianum is preserved under CGMCC NO: 5812, (b) inoculating the strain in fermentation medium comprising chicken manure, humic acid and water, performing fermentation, collecting fermented product, and granulating and drying collected product, and (c) mixing granules with chlamydospore.    USE - The method is useful for preparing microorganism organic fertilizer (claimed) used for preventing and/or treating plant disease or avoiding transfer of plant disease, preferably soil-borne plant diseases chosen from verticillium wilt and fusarium wilt in cotton, Rhizoctonia solani disease in rice, and vascular wilt in banana (all claimed).
NOVELTY - Composite fertilizer comprises 25-50 pts. wt. beer slag, 10-15 pts. wt. urea, 10-20 pts. wt. dipotassium hydrogen phosphate, 1-5 pts. wt. potassium sulfate, 8-15 pts. wt. nutrient element, 0.4-0.8 pts. wt. borax, 0.1-0.3 pts. wt. manganese sulfate, 0.2-0.4 pts. wt. ammonium citrate, and 15-20 pts. wt. composite strain.    USE - As composite fertilizer.    ADVANTAGE - The composite fertilizer exhibits rapid effect, is long-acting fertilizer, and has improved nutrient content and improved utilization rate.
NOVELTY - Preparation of water-soluble fertilizer comprises collecting neem leaf, storing, adding decomposing inoculant, fermenting; adding water, stirring for 1-2 hours, leaching, centrifuging, collecting filtrate; adding strong acid, hydrolyzing at 40-80 degrees C for 15-22 hours to obtain amino acid mother liquor; adding microelement and adjusting chelating agent, reacting in kettle; inspecting and packaging.    USE - Method for preparing water-soluble fertilizer (claimed).    ADVANTAGE - The fertilizer has insecticidal and fungicidal activity.
NOVELTY - An adamantane amine formate salt (I) salt is new.    USE - For manufacturing photosensitive material, electronic material, and lubricant.    ADVANTAGE - The adamantane amine formate salt can be prepared using simple method that provides the adamantane amine formate salt with high yield and high purity, raw material used is easy to obtain and can be recycled, is economical and environment-friendly.    DETAILED DESCRIPTION - An adamantane amine formate salt (I) is new. An INDEPENDENT CLAIM is included for preparation of the compound (I).
NOVELTY - An acetyl-substituted rocuronium bromide derivative (I) is prepared by reacting rocuronium bromide derivative (i), acetylation reagent and acid-binding agent in acetonitrile solvent at 55-85 degrees C, and purifying.    USE - Method for preparing acetyl-substituted rocuronium bromide derivative (claimed).    ADVANTAGE - The compound has greater than or equal to 99.9% purity. The method is environment-friendly, simple and convenient.    DETAILED DESCRIPTION - An acetyl-substituted rocuronium bromide derivative of formula (I) is prepared by reacting rocuronium bromide derivative of formula (i), acetylation reagent and acid binding agent in acetonitrile solvent at 55-85 degrees C, and purifying.
NOVELTY - Extracting nutrients from poultry bone involves cleaning poultry bone, where the cleaned bone is then pulverized to obtain fine bone particles. The obtained fine bone particles are then inoculated with microorganism culture, and then kept for fermentation at low temperature and pressure to extract organic acid from bone particles.    USE - Method for extracting nutrients from poultry bone (claimed).
NOVELTY - Method for crystallization and purification of orlistat involves performing primary process involving dissolving crude orlistat in mixed solvent containing water and polar solvent, cooling, filtering and drying, repeating primary process until the mass content of 98% and re-crystallizing. The mass ratio of crude orlistat and mixed solvent is 2-10:1.    USE - Method for crystallization and purification of orlistat (claimed).    ADVANTAGE - The method efficiently enables crystallization and purification of orlistat with high yield by economical and environmentally-friendly process.
NOVELTY - A biodiesel oil is prepared by dissolving 3 g lipase powder in glycine-sodium hydroxide buffer solution at 4-6 degrees C, filtering, adding macroporous adsorption resin, vacuum freezing, drying, and catalytically reacting with 5-10 g animal fat, 10-15 mL ethanol and 2-4 g immobilized enzyme at 40-50 degrees C for 8-10 hours at speed of 150-200 revolutions/minute.    USE - Method for preparing biodiesel oil (claimed).    ADVANTAGE - The method has low energy consumption, easy separation and environment-friendly process.
NOVELTY - Optical biosensor for detection of organophosphorus pesticides, comprises reaction vessel, circuit and detector.    USE - The optical biosensor is useful for detection of organophosphorus pesticides or determine methyl parathion pesticide.    ADVANTAGE - The optics biosensor: detects organophosphorus pesticides in simple, single step and direct Flavobacterium sp. NCIM 5107 microbial glass fiber disc; is disposable; is cost effective for methyl parathion detection; and is important tool by various environment pollution monitoring and screening agencies (pollution control board) that have to keep a check on the increasing pollution and take preventive measures to curb them.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for designing optics biosensor by designing reaction vessel, designing assembly of biosensor, circuit designing biosensor, machining and processing nylon bar to the specific dimensions of 55-60 mm length and 45-50 mm diameter, attaching convex lenses at the two terminals of the cylindrical bar by using screws, where focal length of convex lens is 30 mm for transmittance of light through the reaction vessel, and length of cylinder was to 60 mm, designing two entry ports of 8-10 mm diameter on cylindrical surface for the addition of sample solution and the immobilized cells discs, designing and pairing special knobs with hook for attachment of glass fiber filter discs on which cells were immobilized, and attaching O-ring at the convex surface of lenses to make the reaction vessel waterproof and air tight.
NOVELTY - Preparing Imidaclothiz involves condensing 2-chloro-5-chloromethylthiazole (CCMT) and 2-nitroaminoimidazoline (NIL) in the presence of an acidic binding agent, a solvent and a catalyst to form an impurity due to bis substitution of the NIL; optimizing the NIL to remove the impurity and excess of the NIL by crystallization of the material with the solvent at pH 9-10 in alkaline media; adding water to the material and agitating the material at 65-70 degrees C for 30 minutes; and filtering the material to remove unreacted NIL which increases with decrease in the impurity, to form a pure material.    USE - For preparing Imidaclothiz (claimed); where the Imidaclothiz is a broad spectrum insecticide available for a variety of crops for prevention and treatment of rice leafhoppers, plant hoppers, thrips, coleopteran, Diptera and Lepidoptera pests, also effective, especially for the rice step borer and yellow stem borer.    ADVANTAGE - The process produces Imidaclothiz with 82% yield and 97-98% purity; has low cost and low toxicity; and is independent of temperature. The Imidaclothiz has a strong insecticidal activity as compared to other insecticides such as Imidacloprid, Acetamiprid and Thiamethoxam.
NOVELTY - Liquid fuels production involves performing flash pyrolysis process with high efficiency through homogenization, heat exchanging, oxygen scavenging, and mixing catalysts (0.25-2%) and additives (0.5-10%). The thermal cracking is performed under controlled conditions at 220-450 degrees C and -1-2 atmospheric pressure. The formed reaction mixture is agitated at 50-600 revolutions per minute (rpm) in presence of oxygen and nitrogen gases.    USE - Method for producing liquid fuels from carbonaceous polymeric materials, such as waste plastic or biomass.    ADVANTAGE - The method produces liquid fuels in a simple, cost-effective and eco-friendly manner without affecting corrosion of equipment and environmental risk, and maximizes production of liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the liquid fuels production equipment.    Raw materials (1)    Heat exchangers (2)    Catalysts (4)    Additives tank (5)    Secondary mixer (8)
NOVELTY - Preparing ilaprazole (I) comprises (a) reacting a 2-((3-methyl-2-pyridyl)methylsulfanyl)-1H-benzimidazole compound (IV) with alkali oxy chlorites/bromites in the presence of a base in a solvent or a mixture of solvents, and (b) isolating the product by the extraction from aqueous layer using solvent(s) followed by removal of solvent by distillation and crystallization of the product using solvent(s).    USE - The process is useful for preparing (I) (claimed), which is useful for treating dyspepsia, peptic ulcer, gastroesophageal reflux and duodenal ulcer. No biological data given.    ADVANTAGE - The process safely and economically prepares (I) with high yield and purity in feasible and environmental friendly manner.    DETAILED DESCRIPTION - Preparing ilaprazole of formula (I) or its salts, comprises (a) reacting a 2-((3-methyl-2-pyridyl)methylsulfanyl)-1H-benzimidazole compound of formula (IV) with alkali oxy chlorites/bromites in the presence of a base in a solvent or a mixture of solvents, and (b) isolating the product by the extraction from aqueous layer using solvent(s) followed by removal of solvent by distillation and crystallization of the product using solvent(s). INDEPENDENT CLAIMS are included for:    (1) sodium salt of (I) having a X-ray powder diffractogram having peaks as given in the specification;    (2) potassium salt of (I) having a X-ray powder diffractogram having peaks as given in the specification;    (3) amorphous (I); and    (4) a process-I for preparing the amorphous form of (I) comprising dissolving (I) in a solvent, and crystallizing the amorphous (I) by adding antisolvent.
NOVELTY - Preparing an open metal carbonyl cluster, comprises chemically reacting a closed metal carbonyl cluster and an opening agent, with the opening agent reacting with a bound carbonyl group so as to unbind it from the cluster and leave behind a carbonyl-labile ligand on the cluster.    USE - The method is useful for preparing an open metal carbonyl cluster which is useful in a chemical catalytic reaction (all claimed).    ADVANTAGE - The method provides stable open metal carbonyl clusters having improved catalytic activity, in a simple manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) the open metal carbonyl cluster prepared by the method, which is supported on a catalyst support; and    (2) a chemical catalytic reaction comprising conducting a chemical reaction either in the presence of the open metal carbonyl cluster or in the presence of a supported and treated open metal carbonyl cluster.
NOVELTY - Manufacture of biomass fuel involves preparing a biomass raw material, providing the biomass raw material into a mold and processing, drying molded biomass until the water content is less than 2 wt.%, and heat-treating the dried material.    USE - Manufacture of heat-treated biomass fuel (claimed).
NOVELTY - Manufacturing biomass fuel comprises introducing biomass raw material pellets into a high-temperature molding device, forming into briquettes or block form by molding, transferring the molded product into a biomass emulsion water bath, emulsifying at a high temperature and carrying out heat-treatment.    USE - The method is useful for manufacturing biomass fuel (claimed).    ADVANTAGE - The method maintains the intensity and apparent density of the biomass being processed in the emulsion water bath (half biomass carbonization); increases the calorific value of the fuel; does not require the additional step including binder addition, thus simplifying the process and reducing production cost. The fuel has lower water absorption rate; and high storage and transportation properties.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for biomass fuel produced by the above mentioned method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the process flow for manufacturing biomass fuel (Drawing includes non-English language text).
NOVELTY - The oxygen generator has electrode plate that is set up in anode plate (1-2) and negative plate (1-1) of respective constant interval. Both electrode boards face the inner side. The oxygen sensor (1-6) detects the oxygen content of the indoor space. The oxygen density control unit (1-7) controls the oxygen content range within the indoor space based on oxygen content signal of the oxygen sensor. The hydrogen gas generated in the water electrolysis device is controlled.    USE - Automatic oxygen generator using water electrolysis and hydrogen fuel cell.    ADVANTAGE - The automatic oxygen generator is environment-friendly. The oxygen generating efficiency can be enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the oxygen generator.    Negative plate (1-1)    Anode plate (1-2)    Hydrogen gas exhaust pipe (1-3)    Oxygen sensor (1-6)    Oxygen density control unit (1-7)
NOVELTY - The oxygen generator has electrode plate that is set up in anode plate (1-2) and negative plate (1-1) of respective constant interval. The oxygen sensor (1-6) detects the oxygen content of the indoor space. The hydrogen gas exhaust pipe (1-3) obtains and ejects the oxygen content signal of the oxygen sensor. The oxygen density control unit (1-7) controls the oxygen content range within the indoor space and the hydrogen gas generated in the water electrolysis device based on the oxygen content signal of the oxygen sensor.    USE - Automatic oxygen generator using water electrolysis and hydrogen fuel cell.    ADVANTAGE - The automatic oxygen generator is environment-friendly. The oxygen generating efficiency can be enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the oxygen generator.    Negative plate (1-1)    Anode plate (1-2)    Hydrogen gas exhaust pipe (1-3)    Oxygen sensor (1-6)    Oxygen density control unit (1-7)
NOVELTY - A photoelectrolytic apparatus comprises housing which holds aqueous medium and permits UV and visible light to enter the interior of the housing, 1st electrode which contains substrate (38) having an undulating surface (40) and semiconductor film which is on and conforms to undulating surface to induce a stress of greater than or equal to 100 mPa in semiconductor film which alters bandgap of stressed part of semiconductor film, 2nd electrode (44) and unit which collects hydrogen gas generated at 2nd electrode substantially free from oxygen generated at the semiconductor film.    USE - Photoelectrolytic apparatus for production of hydrogen gas from aqueous medium, photovoltaics for production of electricity, and photocatalysis for detoxification and disinfection.    ADVANTAGE - Delamination of the film from substrate is prevented. Catalyst has efficient photocatalytic action. Absorption is increased and reflection is decreased. Heat dissipation is improved.    DETAILED DESCRIPTION - A photoelectrolytic apparatus comprises housing which holds aqueous medium and permits UV and visible light to enter the interior of the housing, 1st electrode which contains substrate having an undulating surface and semiconductor film which is on and conforms to undulating surface to induce a stress of greater than or equal to 100 mPa in semiconductor film which altersbandgap of the stressed part of the semiconductor film; a second electrode; and means for collecting hydrogen gas generated at the second electrode substantially free from oxygen generated at the semiconductor film.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of the photoelectrolysis apparatus.    Light (37)    Substrate (38)    Undulating surface (40)    2nd electrode (44)    Optional bias voltage source (45)    Reservoir (46, 47)
NOVELTY - This utility model claims one kind of sludge fermentation pool automatic balk cargo trolley, comprising a guide rail and can move along the guide rail of the trolley, and the other end is set with a bracket, fixing upper bracket fixing with a hopper, and the upper and lower end of the hopper are respectively provided with inlet and outlet, upper discharge hole is hinged with a discharging plate, a upper trolley rotatably equipped with a rotating shaft, the rotating shaft one end of the transmission connecting with a motor, the rotating shaft of the upper trolley is set on the fermenting tank opening two sides of fixing connecting with a swinging rod, a swinging rod with the unloading plate is hinged with a connecting rod. The structure of this utility model is simple, it can uniformly adding dehydrated sludge and aerobic microbial thalli to the fermenting tank to make the dehydrated sludge and aerobic microbial thalli in the fermentation tank can be flat paving, improves the fermentation efficiency and the dewatered sludge, conversion efficiency.
NOVELTY - A one hot can convert marsh gas generator for frigid zone, comprising a plurality of fermentation device, comprising a boiler steel plate to form a connecting main body, said each fermenting device through biogas outlet pipeline connecting storage tank, said storage tank by the gas pipeline connecting gas boiler, said gas storage tank by the civil fuel gas pipe connecting with the subsequent part upper gas device, hot water pipe and one end of the water return pipeline connecting said gas boiler, and the other end extends into said main body, said fermentation device is set, the bottom is provided with a slag pushing stirring propeller. Said fermentation device is corrosion resistant glass fibre reinforced plastic cylindrical fermenting device. Civil hot water pipe and civil water return pipe one end connecting said gas boiler, the other end connecting the subsequent device. Said propeller by the motor and gear driven by the joint process. Said fermentation device one sealed head is provided with propeller thruster port sealing cover, and the other one head is provided with the slag hole, the slag hole is sealed cover sealing said discharging hole. The utility model ensures the fermentation temperature, is suitable for frigid zone;
NOVELTY - This utility model claims one kind of marsh gas generator, comprising a tank body and a water pressure, said pool body is composed of section and in the bottom part tank body, the tank body upper section, which are respectively provided with a discharging pipe interface and inlet interface pipe on the tank body bottom part of the bottom and upper part of upper section of the tank body is provided with inlet and outlet and barrel-type storage chamber, said water pressure at the bottom is provided with a water pressure chamber interface pipeline, said tank body and water pressure chamber by discharging interface pipe and water pressure chamber interface pipeline between the discharging device are connected with each other, said discharging device of three-way pipe and a discharging output interface pipeline, wherein two inlets of the three-way pipe are respectively connected with the discharging interface pipe and water pressure chamber interface pipeline, one outlet and the discharging output interface pipeline of the three-way pipe is connected with a gate valve is set up on the discharging output interface pipeline. The structure of this utility model is simple, the use is convenient, can use crop straw raw material, using time of the residual slag tank in the tank bottom is not easy to block.
NOVELTY - This utility model claims one kind of solar energy and biogas combined heating of the waste heat recovery type marsh gas generating system, comprising a feeding connecting device, marsh gas and solar heat collector, wherein said marsh gas tank and connecting with the marsh gas boiler, said marsh gas and marsh gas boiler and solar heat collector in parallel connecting. Beneficial effects: using solar energy hot collecting technology and is suitable for rural area of allixiary hot source marsh gas boiler marsh gas fermentation to provide stable hot environment, waste heat recovery device recycling row material heated by the heat of the hot water in the heat storage water tank and part of the hot water to marsh gas feeding device in pre-heating biomass raw material. Combined use of solar energy and methane boiler in winter, can ensure the cloudy and rainy days, night time is system of solar heat. Suitable for the user in the marsh gas fermentation and farm house the hot water, heating and cooking, lighting and so on.
NOVELTY - The method involves entering domestic sewage into physical and chemical section. The macromolecule organic matter or inorganic small molecular substance is removed. The biochemical treatment of waste water in secondary sedimentation tank is performed. The remaining sludge is delivered to electric processing reactor, and the residual sludge extraction amount is 10%. The sludge is discharged to a sludge dewatering center, such that the sludge landfill or brick is dried.    USE - Sludge sewage treatment method.    ADVANTAGE - The high efficiency can be achieved and the energy consumption can be reduced, and the sludge yield can be reduced. The treatment ability of the sewage sludge can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the sludge sewage treatment process. (Drawing includes non-English language text)
NOVELTY - Preparation of levalbuterol involves performing asymmetric synthesis of levalbuterol using chiral amphiphilic block copolymer containing poly(ethylene oxide)-b-poly(glycidyl triazolyl-L-quinine) as catalyst.    USE - Preparation of levalbuterol (claimed).    ADVANTAGE - The levalbuterol is prepared with high yield and enantiomeric excess value by simple and environmentally-friendly method.
NOVELTY - Preparation of cellulose liquid fuel involves pretreating biomass, then mixing the pretreated biomass with ethanol aqueous solution at high temperature and pressure for 10-30 minutes, filtering, mixing the obtained solid with a catalyst and carrying out fermentation process in presence of bacteria.    USE - Preparation of cellulose liquid fuel (claimed).    ADVANTAGE - The method enables economical preparation of cellulose liquid fuel by environmentally-friendly and simple process, under reduced energy consumption.
NOVELTY - An external electrolysis device comprises shell (1) containing parallel iron electrodes (2) and carbon plate electrodes (3) staggeredly arranged from bottom to top in which iron electrode is connected to cathode of external power supply (4), carbon plate electrode is connected to anode of external power supply, outside of shell bottom contains feed tube (6) connected to feed pump (5), and outside of shell top contains discharge tube (8) connected to discharge pump (7).    USE - An external electrolysis device for producing methane (claimed).    ADVANTAGE - External electrolysis device is easy to install, has small volume, stable methane production ability, promotes anaerobic degradation of organic substrates, and improves methane yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the structure of external electrolysis device.    Shell (1)    Iron electrode (2)    Carbon plate electrode (3)    External power supply (4)    Feed pump (5)    Feed tube (6)    Discharge pump (7)    Discharge tube (8)
NOVELTY - A Mycobacterium gilvum strain CP13 (CGMCC 7963) is new.    USE - A Mycobacterium gilvum strain CP13 (CGMCC 7963) used for degrading polycyclic aromatic hydrocarbon component in petroleum (claimed). Can also be used for bioremediation of petroleum-contaminated water and soil and biological treatment of polycyclic aromatic hydrocarbon-containing industrial wastewater.    ADVANTAGE - Mycobacterium gilvum has high degradation rate and strong degradation ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of Mycobacterium gilvum for degrading polycyclic aromatic hydrocarbon component in petroleum.    DESCRIPTION OF DRAWING(S) - The drawing shows a scanning electron microscope image of a Mycobacterium gilvum strain CP13.
NOVELTY - A Serratia marcescens strain S2 (CGMCC 3654) is new.    USE - A Serratia marcescens strain S2 (CGMCC 3654) used for degrading dibenzothiophene in contaminants containing dibenzothiophene (claimed) such as petrochemicals, coke waste, and petroleum-contaminated soil and groundwater.    ADVANTAGE - Serratia marcescens strain S2 (CGMCC 3654) is efficient and easy to become dominant strain, has fast degradation speed, grows fast, and promotes environmental pollution control.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of Serratia marcescens strain S2 (CGMCC 3654) for degrading dibenzothiophene.
NOVELTY - An algae is pre-processed by drying algae, crushing, sieving, weighing, boiling with water to obtain algae solution, adding ferrous sulfate solution and hydrogen peroxide solution or drying algae, crushing, sieving, weighing, subjecting algae to water, orderly adding ferrous sulfate solution and hydrogen peroxide solution when heat treatment is finished in which water boiling or heating temperature is 60-100 degrees C, water boiling or heating time is 5-60 minutes, concentration of ferrous sulfate is 2.63-52.6 mM, and concentration of hydrogen peroxide solution is 0.004-0.08 mass%.    USE - Pre-processing of algae for fermenting fuel ethanol.    ADVANTAGE - Pre-processing time is short, energy consumption is low, and operation is simple and environment-friendly and has no inhibitor, low device requirement, and non-corrosive material.
NOVELTY - An algae biofuel is produced by soaking algae in aqueous alkaline solution for 20-40 minutes, washing with water at elevated temperature and pressure, adding acid solution, mixing for 20-30 minutes, filtering or centrifugating, separating liquid component by suction filtration or centrifugation, removing solid, adding acid catalyst, and mixed flora, and fermenting.    USE - Production of algae biofuel (claimed).    ADVANTAGE - The method uses high yield and fast-growing algae, is highly efficient, and low cost.
NOVELTY - The method comprises disposing agricultural and domestic wastes on a waste processing device and then processing the waste using a marsh gas. The device includes first and second layers arranged in a container, a water outlet, and a discharging pipe. The first layer is positioned at bottom end of the container. The second layer is positioned at top end of the container. A gas outlet is configured for providing exhaust gas in the waste. A top part of an air storage layer is connected at a top end of a water return pipe that is installed at a bottom end of the gas outlet.    USE - The method is useful for processing agricultural and domestic wastes (claimed).    DETAILED DESCRIPTION - The method comprises disposing agricultural and domestic wastes on a waste processing device and then processing the waste using a marsh gas. The device includes first and second layers arranged in a container, a water outlet, and a discharging pipe. The first layer is positioned at bottom end of the container. The second layer is positioned at top end of the container. A gas outlet is configured for providing exhaust gas in the waste. A top part of an air storage layer is connected at a top end of a water return pipe that is installed at a bottom end of the gas outlet. An arc maintains the pressure inside the waste processing device. A filtering layer is filled with a filtering material. An INDEPENDENT CLAIM is included for a device for processing agricultural and domestic wastes.
NOVELTY - Additive composition comprises terpene, limonene and pinene associated with one or multiple ingredients which improve properties and alter characteristics of the fuel.    USE - Additive composition used for preparing fuel composition or biofuel composition for reducing clogging in cold weathers (all claimed).    ADVANTAGE - The additive composition efficiently reduces formation of molecular clusters in the fuel system by reducing extent of clogging in cold filter of the engines, and reduces emission of air pollutants such as nitrogen oxide.
NOVELTY - The reactor has a strainer that is arranged in upper and lower portion of microorganism apparatus portion. A waste water outlet (120) is arranged to allow the waste water to effluent supply unit (110). The organic wastewater is supplied and the effluent which becomes with anaerobic digestion to discharge. The reactor main portion (100) is equipped with a biogas exhausting portion (130) to allow the biogas through anaerobic digestion portion. The microorganism apparatus portion is installed inside a reactor main portion.    USE - Anaerobic digestion reactor for producing biogas from liquid organic wastewater.    ADVANTAGE - The leakage of anaerobic microorganism can be prevented effectively, such that the removal of high concentration organic material through microorganism can be performed. The biogas production efficiency of anaerobic digestion reactor can be maximized reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic digestion reactor.    Reactor main portion (100)    Effluent supply unit (110)    Waste water outlet (120)    Biogas exhausting portion (130)
NOVELTY - Mixed germ liquid comprises Mucor circinelloides, Bacillus pumilus and Stenotrophomonas maltophilia in a ratio of 1:0.9-1.2:0.9-1.2.    USE - The mixed germ liquid is useful for reducing odor of excrements and producing organic fertilizer (all claimed).    ADVANTAGE - The mixed germ liquid can be prepared simply and cost-effectively. The fertilizer is easy to supply.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing organic fertilizer, which involves crushing livestock manure, mixing manure with bacteria in a weight ratio of 1:6 until the moisture content is 60-70%, and stacking the obtained mixture for 21-28 days.
NOVELTY - The utility model claims one for anaerobic reaction of the heating device, comprising a reaction container and heat exchanger, said reaction vessel from the feeding side to the discharging side is divided into at least three heating area, two groups of heat exchanger are set at the lower part of the reaction vessel, wherein the heat exchanger comprises at least three groups of , each group of heat-exchange pipe group from the feeding side passes through the reaction vessel and is set in the corresponding heating region. This utility model has reasonable structure and it can the reaction vessel section area of heat supply are greater than the reaction container after the end of the heat supply, which can ensure the consistency of the material heating temperature in the reaction vessel, which is good for fully organic garbage anaerobic fermentation, anaerobic processing efficiency can be improved.
NOVELTY - One for automatically controlling the biomass fermentation marsh gas test device, comprising a heating water tank, a bag, an air guide pipe, a fermentation bottle, a heater, a temperature sensor, a temperature control box, test bench. Said heating water tank is equipped with a fermentation bottle, a heater, a temperature sensor, a fermentation bottle through the gas-guide tube and the connecting bag, a temperature control box is set on the test bench up, a heater, a temperature sensor is connected with the temperature control box and connecting the heating water tank. The utility model has automatic control heating temperature, automatically collecting methane, can be applied to various ferment test, glass device is convenient to observe in fermentation, biogas parameter is convenient to detect, high heat transfer efficiency, simple structure, small volume, low cost, reliable use and so on, widely used in fermentation of various biomass raw material marsh gas.
NOVELTY - This utility model claims one kind of methane tank generating system, comprising a generator, a rotating shaft and marsh gas tank, upper rotating shaft is provided with a blade, an air blowing blade rotating shaft to rotate to drive the generator to generate electricity, taking the current input controller through the lead, taking the input inverter convert between the lower end of the alternating current input to the fermentation liquid in the fermentation chamber in the heating device, a rotating shaft is provided with a stirrer extends into the fermentation, using a fermenting liquid and fully contact methane bacteria, a rotating shaft by a rotating base fixing on the bottom surface. The utility model solves the problem that the marsh gas tank cannot work normally in winter electricity under the low temperature condition of the problem of system design layout is reasonable, using wind energy convert into electric energy, taking, the antibacterial activity is marsh gas tank, an air rotating shaft material of generator end capable of moving up and down is provided with a stirrer, the fermentation liquid and the methane bacteria using fully contact, the marsh gas power generation effect.
NOVELTY - Nitrosation processing domestic sewage, comprises inoculating municipal sewage reflux sludge into a reactor, (b) then starting, adding dissolved oxygen (OD), ammonia nitrogen and calcium carbonate under condition of nitration sludge domestication to obtain preliminary nitrite, controlling concentration of ammonia nitrogen and calcium carbonate, reducing concentration of ammonia nitrogen, calcium carbonate and DO, operating the reactor, and maintaining domestic sewage into nitrous accumulation at more than 95%.    USE - The method is useful for nitrosation processing of domestic sewage (claimed).    ADVANTAGE - The method is capable of nitrosation processing of domestic sewage in a stable manner.    DETAILED DESCRIPTION - Nitrosation processing domestic sewage, comprises (a) inoculating municipal sewage reflux sludge having concentration of 10-12 g/l into a reactor, (b) then starting at temperature of 20-25 degrees C and pH of 7.8-8, adding 0.2-0.5 mg/l of dissolved oxygen (OD), 200 plus minus 10 mg/l of ammonia nitrogen and 2000 plus minus 100 mg/l of calcium carbonate under condition of nitration sludge domestication with rate of more than 90% to obtain preliminary nitrite, (c) controlling concentration of ammonia nitrogen to 200 plus minus 10 mg/l, preferably 150 plus minus 10 mg/l and calcium carbonate to 2000 plus minus 100 mg/l, preferably 1500 plus minus 100 mg/l, reducing concentration of ammonia nitrogen to 100 plus minus 10 mg/l, calcium carbonate to 1000 plus minus 100 mg/l and DO, and operating the reactor at temperature 20-25 degrees C for 10 days, and (d) maintaining domestic sewage into nitrous accumulation at more than 95%.
NOVELTY - Manufacture of biomass carbon involves using bamboo charcoal, carbon or activated carbon as raw material, crushing the raw material using a crusher to obtain carbon powder, adding thermosetting adhesive to the carbon powder, stirring, supplying the obtained carbon powder into forming machine, cold-drying, supplying the carbon powder into high temperature furnace, passing hot air through the furnace, carbonizing (I) at 400-700 degrees C, molding the carbonized product (I) to obtain molded carbon product, carbonizing (II) the molded product to obtain a carbon product and cooling.    USE - Manufacture of biomass carbon (claimed).    ADVANTAGE - The method provides biomass carbon having excellent absorbing property, and improved quality and yield.    DETAILED DESCRIPTION - Manufacture of biomass carbon involves using bamboo charcoal, carbon or active carbon as raw material, crushing the raw material using a crusher to obtain carbon powder, adding thermosetting adhesive to the carbon powder, stirring uniformly, supplying the obtained carbon powder into forming machine, cold-drying, supplying the carbon powder into high-temperature furnace, passing hot air through the furnace, carbonizing (I) at 400-700 degrees C, molding the carbonized product (I) to obtain molded carbon product, carbonizing (II) the molded product to obtain a carbon product and cooling. The temperature of carbonization process (II) is higher than the temperature of carbonization process (I) by 1-500 degrees C.
NOVELTY - Producing acid component by directional control and anaerobic fermentation of cassava alcohol wastewater comprises mixing cassava alcohol wastewater and inoculation sludge (of volatile suspended solids concentration 10-13 g/l) of volume ratio 9:6:1, adjusting pH of the mixed solution to 8-9, low speed stirring and anaerobic fermenting at 30-40 degrees C, promoting directional conversion of organic substance into to butyric acid or acetic acid/propionic acid as volatile fatty acid as main component, and controlling the hydraulic retention time for 2.5-3.5 hours.    USE - The method is useful for producing acid component by directional control and anaerobic fermentation of cassava alcohol wastewater (claimed).    ADVANTAGE - The method utilizes high carbohydrate content and low nitrogen-phosphorus content cassava alcohol wastewater, ensures processing of carbon source or other chemical raw materials and realizes directional control by changing pH of fermentation system.
NOVELTY - The pneumatic test water cellar has a concrete pit body (16), a drainage (1), a water inlet (2), a water outlet (3), a PVC water pipe (4), a pit port cover (9), a neck (8), and an inverted V-shaped sealing air inlet (14) that is sealed with an air sealing basin (13). The air sealing basin is connected with a gas pot lifting chunk (11) and a fixing strip (12). The concrete pit body has a test air charging pipe (5) with an air door valve (6) and a pressure gauge (7) which detects a sludge leak at a concave pit (18) that is formed at a bottom portion of the pit body.    USE - Pneumatic test water cellar for marsh gas tanks and special inflator module (claimed).    ADVANTAGE - Prevents mortar buoyancy, ensures a safe cellar that is convenient in cleaning silt in a concave pit, and improves the accuracy of a small cellar in a closed state.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a pneumatic test water cellar construction method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a pneumatic test water cellar.    Drainage (1)    Water inlet (2)    Water outlet (3)    PVC water pipe (4)    Test air charging pipe (5)    Air door valve (6)    Pressure gauge (7)    Neck (8)    Pit port cover (9)    Gas pot lifting chunk (11)    Fixing strip (12)    Air sealing basin (13)    Sealing air inlet (14)    Concrete pit body (16)    Concave pit (18)
NOVELTY - The system (100) has an anaerobic digester (110) in which biogas producing microorganism digest the organic compound with anaerobic. An ultrasonic irradiation apparatus (130) irradiates low-strength ultrasound to biogas producing microorganisms. A control device controls a membrane separation device (150) which prevents the outflow of biogas producing microorganism from digestive fluid generated within anaerobic digester, by fire-extinguishing of organic compound.    USE - Anaerobic digestion system for digesting organic compound such as rice hull, chinese cabbage, onion, livestock excretion, food waste, sewage sludge, barley straw and wheat straw.    ADVANTAGE - The microorganism outflow within the anaerobic digestion tub can be maintained with high concentration. The digestion efficiency of the anaerobic digestion system can be increased. The biogas generation rate of the anaerobic digestion system can be maximized and the organic waste weight loss rate of the anaerobic digestion system can be maximized. The methane gas productivity and the organic treatment efficiency of the anaerobic digestion system can be increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the anaerobic digestion system. (Drawing includes non-English language text)    Anaerobic digestion system (100)    Anaerobic digester (110)    Biogas outlet (115)    Ultrasonic irradiation apparatus (130)    Membrane separation device (150)
NOVELTY - The method comprises preparing first and second molding compounds comprising a thermosetting resin, a conductive carbon material, a reinforcing material and a release agent, mixing the compounds to obtain a mixture, forming a plate-like preform, and forming a three-layered structure including a copolymer to obtain a fuel cell separator plate.    USE - The method is useful for manufacturing a fuel cell separator plate (claimed), where the fuel cell is a polymer electrolyte fuel cell.    ADVANTAGE - The method enables efficient and economic manufacture of the fuel cell separator plate with light weight, high flexural strength and quality and improved electrical and thermal conductivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell separator plate.
NOVELTY - The method involves mixing (S10) combustible waste to through-hole punched in a rotation trommel. The iron material mixed in combustible waste is selected (S20) in a magnetic separator. The soil mixed in combustible waste selected in magnetic separator is selected (S30). The selected combustible waste is crushed (S40) to 200~300mm. The crushed combustible waste is transferred (S50) to conveyer belt and put into inlet port of reduction selector. The combustible waste of high purity is obtained by pulverizing (S70) the crushed combustible waste.    USE - Fuel recycling screening method of combustible waste such as furniture waste, waste plastic film, waste synthetic resin and garbage.    ADVANTAGE - The fuel recycling of the high purity combustible waste can be obtained, while the foreign substance including earth and sand etc. is completely removed, by injecting heat generated in heating portion of kiln drier into the cylinder.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel recycling screening apparatus of combustible waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a block flow diagram of the fuel recycling screening equipment. (Drawing includes non-English language text)    Step for mixing combustible waste to through-hole punched in a rotation trommel (S10)    Step for selecting iron material mixed in combustible waste in magnetic separator (S20)    Step for selecting soil mixed in combustible waste selected in magnetic separator (S30)    Step for crushing selected combustible waste (S40)    Step for transferring crushed combustible waste to conveyer belt (S50)    Step for pulverizing the crushed combustible waste (S70)
NOVELTY - Tea tree fertilizer comprises 20-25 pts. wt. of dry chicken manure, 30-40 pts. wt. of plant ash, 10-12 pts. wt. of shell powder, 12-14 pts. wt. of straw, 10-15 pts. wt. of grass, 2-4 pts. wt. of rice bran, 4-6 pts. wt. of jade powder, 5-7 pts. wt. of phosphogypsum, 2.5-3.5 pts. wt. of ammonium bicarbonate, 3-5 pts. wt. of ammonium chloride, 4-6 pts. wt. of potassium chloride, 1-2 pts. wt. of zinc sulfate, 3-5 pts. wt. of Celastrus powder, 2-4 pts. wt. of cork powder, 4-6 pts. wt. of Aloe vera powder, and 3-4 pts. wt. of modified clay powder.    USE - Tea tree fertilizer.    ADVANTAGE - The tea tree fertilizer improves the quality of the soil in a rapid manner.
NOVELTY - A 17-oxo-7-hydroxymethylphenyl furan chalcone (I) is new.    USE - 17-Oxo-7-hydroxymethylphenyl furan chalcone used as foul controlling agent for marine organisms, particularly barnacle larvae and young mussel (all claimed).    ADVANTAGE - The foul controlling agent is safe, environment-friendly, effective and suitable for large-scale production.    DETAILED DESCRIPTION - A 17-oxo-7-hydroxymethylphenyl furan chalcone of formula (I) is new.
NOVELTY - An biological silicone hydrophobic organic waste treatment method, involves mixing broth with a silicone oil, to obtain absorbing liquid, adding absorbing liquid to the bioreactor, followed by mixing hydrophobic organic waste into the bioreactor through the handle at 25 degrees C.    USE - Biological silicone hydrophobic organic waste treatment method.    ADVANTAGE - The method enables increasing the scope of the biological treatment of organic waste, and promoting and improving the stability of the reaction apparatus, and ability of the device anti-transient shocks.
NOVELTY - An organic fertilizer comprises 30-40 pts. wt. chicken manure, 15-25 pts. wt. cow manure, 12-25 pts. wt. pig manure, 10-13 pts. wt. peat soil, 15-20 pts. wt. straw ash, 8-10 pts. wt. sawdust, 2-4 pts. wt. formic acid, 5-8 pts. wt. animal bone powder, 6-8 pts. wt. egg shell powder, 3-5 pts. wt. gypsum powder, 2-4 pts. wt. calcium hydrogen phosphate and 0.5-0.8 pt. wt. ectomycorrhizal inoculum.    USE - Organic fertilizer.    ADVANTAGE - The simple, economical and easy-to-operate method has short fermenting time, low cost and wide raw material sources, and it utilizes waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising mixing animal bone powder, egg shell powder, gypsum powder, calcium hydrogen phosphate, chicken manure, cow manure, pig manure, peat soil, straw ash, sawdust and formic acid, adding ectomycorrhizal inoculum and water, adjusting water content to 30-40%, placing in fermentation tank, covering plastic film, fermenting at 55-65 degrees C for 2-4 days to obtain fermentation product, sieving, screening, removing impurities, granulating, and drying.
NOVELTY - A fertilizer comprises 6-8 pts. wt. microbial agent, 25-35 pts. wt. potassium sulfate, 240-255 pts. wt. urea, 35-50 pts. wt. calcium superphosphate, 150-175 pts. wt. plant ash, 300-330 pts. wt. sawdust, 200-250 pts. wt. carbon, 100-115 pts. wt. maifanite powder, 120-125 pts. wt. zeolite powder and 7-9 pts. wt. soil conditioner.    USE - Fertilizer.    ADVANTAGE - The fertilizer improves micro-environment of soil and repairs soil pollution. It absorbs poisonous heavy metal element in soil and improves crop yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer comprising crushing microbial agent, potassium sulfate, urea, calcium superphosphate, plant ash, sawdust, carbon, maifanite powder and zeolite powder, granulating, drying, adding soil conditioner, and mixing uniformly.
NOVELTY - Separation and preparation of L-gossypol by high speed counter-current chromatography comprises (a) taking racemic gossypol compound crude product, where gossypol compound is gossypol acetate or gossypol formate, (b) preparing high speed counter current chromatography stationary phase and mobile phase, (c) purifying gossypol compound, and (d) preparing L-gossypol.    USE - The method is useful for separation and preparation of L-gossypol by high speed counter-current chromatography (claimed).    ADVANTAGE - The method has high separation efficiency, produces high purity product; maximizes the extraction rate due to the usage of the expansion solvent and ultrasonic-microwave combined extraction process; completely uses the raw materials; is economical; carries out separation after hydrolysis process, thus avoiding product oil and increasing pigment presence to improve product purity; can directly obtain optically-active substance; and is suitable for industrial usage.
NOVELTY - Preparing high color value of gardenia blue pigment involves enzyme hydrolysis of 5-15 mg/ml gardenia yellow waste liquid at 45-60 degrees C for 40-120 minutes, to obtain beta-glucosidase hydrolytic solution; adding 10-30 g amino acid to beta-glucosidase hydrolytic solution, to obtain gardenia blue pigment solution; carrying out gardenia blue pigment ultra-filtration separation using ultrafiltration membrane; extracting gardenia blue pigment purified product, and drying, to obtain gardenia blue pigment powder; adding the powder into methanol or ethanol, stirring, and extracting.    USE - For preparing high color value of gardenia blue pigment (claimed), used in food, medicine and cosmetic industry.    ADVANTAGE - The method obtains the gardenia blue pigment with high color value and good quality, and high purity; and is environmental friendly.    DETAILED DESCRIPTION - Preparing high color value of gardenia blue pigment involves enzyme hydrolysis of 5-15 mg/ml gardenia yellow waste liquid at 45-60 degrees C for 40-120 minutes, to obtain beta-glucosidase hydrolytic solution having pH value of 4-6; adding 10-30 g amino acid to beta-glucosidase hydrolytic solution at 60-100 degrees C for 10-30 minutes, to obtain gardenia blue pigment solution; carrying out gardenia blue pigment ultra-filtration separation using ultrafiltration membrane, at 15-45 degrees C, washing filtrate for 1-4 times, collecting trapped fluid and permeate liquid after separating; extracting gardenia blue pigment purified product, vacuum drying, spray drying or vacuum freeze-drying, to obtain gardenia blue pigment powder; adding the gardenia blue pigment powder continuously into 80-100% methanol or ethanol, stirring under magnetic force in water bath to extract for 0.5-4 hours, extracting at 30-70 degrees C for 1-3 times, to obtain the gardenia blue pigment.
NOVELTY - A blend membrane comprises poly(ether block amide) and glyceryl triacetate at fraction of 0.01-99%, and rest of poly(ether block amide).    USE - Blend membrane for use as gas separation membrane for separating gas mixture with different gas components such as carbon dioxide, hydrogen sulfide, or sulfur dioxide, and permeate gas such as non-priority nitrogen, oxygen, 1-4C hydrocarbon gas, and hydrogen (all claimed).    ADVANTAGE - The membrane has high separation performances.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing blend membrane, which involves preparing a casting solution by dissolving polyether-b-polyamide in n-butanol solvent to prepare a concentration of 0.1-20% solution of polyether-b-polyamide, adding glycerol triacetate, to prepare homogeneous casting solution, at dissolution temperature of 70-110 degrees C, degassing the casting solution, coating flow cast film in glass or PTFE film or plates to prepare composite membrane, and removing residual solvent in the membrane.
NOVELTY - A pure natural plant growth regulator comprises 60-90 pts. wt. molasses fermentation broth, 5-15 pts. wt. calcium ammonium nitrate, 1-5 pts. wt. boric acid, 5-15 pts. wt. water, and 1.51% alcohol milk powder.    USE - Pure natural plant growth regulator.    ADVANTAGE - The regulator is more conducive to effective absorption and utilization of crops, does not contain hormones, and has high content and purity of active ingredients and utilization rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of regulator by spraying 0.2-0.5 ppm 1.51% alcohol milk powder into reactor, adding molasses fermentation broth, calcium ammonium nitrate, boric acid, and water, dissolving, and heating to low temperature.
NOVELTY - Substituted 2-chloroquinoline-3-carbaldehyde phenyl hydrazone compounds (I) are new.    USE - (I) have antimicrobial, anticonvulsant, analgesic, antiinflammatory, antiplatelet and antitumoral activities. Tests details are described but no results given.    ADVANTAGE - (I) can be prepared with high yield and purity without using excess amount of organic solvent in a rapid, simple, economical and user friendly manner.    DETAILED DESCRIPTION - Substituted 2-chloroquinoline-3-carbaldehyde phenyl hydrazone compounds of formula (I) are new.    R1 = H, alkyl or alkoxy;    R2 = H, halo or nitro;    R3 = H or alkyl; and    R4 = H or halo.    An INDEPENDENT CLAIM is included for the preparation of (I).
NOVELTY - Extracting essence from buckwheat leaves, involves (a) cleaning buckwheat leaves and drying the cleaned buckwheat leaves, and grinding the dried leaves to obtain buckwheat powder, (b) extracting the obtained powder using ethanol, uniformly stirring the extract, and heating the extract in microwave oven, (c) extracting the obtained product using edible ethanol for 2-3 times, filtering the extracts, and combining the filtrate, (d) concentrating the filtrate, and (d) centrifuging or filtering the concentrate, drying the obtained product, and pulverizing the product.    USE - The method for extracting essence from buckwheat leaves, where the essence is rutin (natural flavone).    ADVANTAGE - The method extracts not less than 72% essence from buckwheat leaves, and is simple and rapid (extraction time is short), and suitable for industrialization, and consumes less energy. The essence has excellent antioxidant effect. In method, the solvent is nontoxic, cost-effective and environmentally-friendly.    DETAILED DESCRIPTION - Method for extracting essence from buckwheat leaves, involves (a) cleaning buckwheat leaves and drying the cleaned buckwheat leaves, and grinding the dried leaves to obtain buckwheat powder, (b) extracting the obtained powder using 65-85% ethanol (obtained powder:ethanol=1:40-60), uniformly stirring the extract, and heating the extract in microwave oven at 250-300 W for 3 minutes, (c) extracting the obtained product using 65-85% edible ethanol for 2-3 times, filtering the extracts, and combining the filtrate, (d) concentrating the filtrate (to volume), and (d) centrifuging or filtering the concentrate, drying the obtained product at 600 degrees C, and pulverizing the product.
NOVELTY - A spirulina is cultured by filtering livestock and poultry excrement, sterilizing filtrate to obtain culture solution, inoculating seed in fresh water or sea water, domestic culturing, inoculating domestic cultured seed in culture solution, culturing, collecting spirulina, filtering, washing, collecting spirulina, drying, and recovering ethanol from filtrate.    USE - Culture of spirulina (claimed).    ADVANTAGE - Culture process reduces culturing cost and pollution.
NOVELTY - Culturing Nannochloropsis salina comprises: carrying out two-stage culture on microalgae that is rich in nutrition after oligotrophic culture.    USE - The method is useful for culturing Nannochloropsis salina for improving biomass and oil production (claimed).    ADVANTAGE - The method is capable of culturing microalgae without additional nutrients, while reducing cost of the medium and promoting microalgae biomass yield and oil yield upto 65% and 133%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for oligotrophic f/2 medium culture medium comprising phosphate.
NOVELTY - Bacillus subtilis strain X3 (I) preserved under a number of CCTCC No. M2013261, at China Centre for Type Culture Collection, at 2013 year 06 months 16 days, and China. Wuhan China.    USE - (I) is useful for degrading hydrogen sulfide generated in cattle excrement (claimed).    ADVANTAGE - (I) degrades hydrogen sulfide (19.59-52.74%), has high efficiency, low requirement and simple operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of (I) for degrading hydrogen sulfide generated in cattle excrement.
NOVELTY - The biogas production system comprises a substitution bath tub (13) for performing the substitution reaction. The organic waste is provided to a fermenter (11) for fermenting the organic waste. The fermenter generates the biogas. An anaerobic fermentation tub (15) is connected to the substitution bath tub to supply the generated biogas to the substitution bath tub which has wastewater sludge, food waste and the livestock excretion. The biogas includes fifty to hundred percent of methane and ten to fifty percent of the carbon dioxide.    USE - System for producing biogas using substitution reaction in pretreatment process of anaerobic fermentation.    ADVANTAGE - The organic waste is provided to a fermenter for fermenting the organic waste, thus ensures economically production of the biogas. The disabling of the methane fermentation is prevented by injecting the organic waste in the anaerobic fermentation tub, thus ensures reduction of time delay in the gas generation and improves the yield of the biogas production with simple operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biogas manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a biogas production system. (Drawing includes non-English language text).    Fermenter (11)    Substitution bath tub (13)    Anaerobic fermentation tub (15)    Filtrate tub (17)    Energy converter (19)
NOVELTY - The apparatus has an inclined plate inclinedly arranged in an upper portion of a ptecticus tenebrifer line. A storage unit is formed with a head space and a down space. Organic waste is settled in the storage unit. A compost material is generated from the organic waste. A filter plate is connected to an external ptecticus tenebrifer collector of a cubical shaped main body. The main body is arranged in the inclined plate. The main body is connected with a right side edge part of a bottom plate. An inlet port is provided with an opening and closing part.    USE - Ptecticus tenebrifer breeding and organic waste treating apparatus.    ADVANTAGE - The apparatus efficiently proceeds composting of the organic waste by ptecticus tenebrifer larva. The apparatus avoids generation of dispersion smell during composting process of the organic waste by closing a vent and an inlet port of the main body.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a ptecticus tenebrifer breeding and organic waste treating apparatus.
NOVELTY - The water filter comprises a membrane including a proton pump for pumping water, where the membrane separates the protein inside the water. The membrane is a water impermeable membrane. The proton pump is pumped using solar energy. The membrane accommodates water by osmosis process. The proteins are passed through the membrane. A concentration of the pure water is higher than the concentration of the sewage water in the membrane. The pressure is generated inside the membrane by forward osmosis process according to the density difference of sewage water and pure water.    USE - The water filter is useful for purifying the water such as sewage water (claimed).    ADVANTAGE - The water filter is capable of economically, easily and eco-friendly purifying the sewage water in an energy efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for purifying a water using proton pump.
NOVELTY - Method of producing glucose by hydrolysis of microalgae Dunaliella tertiolecta biomass, involves obtaining amylose-like glucan from the microalgae D.tertiolecta and hydrolyzing amylose-like glucan to obtain product.    USE - The method is useful for producing glucose which is used in production of biofuel, preferably bioethanol (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing biofuel, which involves performing the above-mentioned steps to obtain glucose and fermenting the glucose to obtain product.
NOVELTY - Processing anthraquinone compound waste water by Ceriporiopsis subvermispora mediated degradation comprises taking C. subvermispora as a starting strain, culturing in a test tube, carrying out liquid shake flask culturing process, liquid amplification culture and liquid fermentation to remove anthraquinone compound in the waste water, where the anthraquinone compound removal rate is 60-100%.    USE - The method is useful for processing anthraquinone compound waste water by C. subvermispora mediated degradation (claimed).
NOVELTY - The method involves directly mixing material into the crushing system. The mixed material water content is processed to 25-30 % in rear crushing system. The water vapor is sprayed to the inside of furnace. The residue of rear cracked and unctuous material are mixed. The cracking of gas-liquid mixture is entered into spray air purifying processing device.    USE - Cracking method of mixture of straw and food waste.    ADVANTAGE - The water vapor can be sprayed to control the temperature of furnace to reduce energy loss.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the straw and food waste. (Drawing includes non-English language text)    Straw (1)    Kitchen garbage mixture (2)    Ash (3)    Gas-liquid mixture (4)    Clean water (7)
NOVELTY - The method involves crushing and drying house-hold rubbish waste. The crushed house-hold rubbish waste is sent to an industrial ethylene cracking furnace. Water vapor steam is evaporated from the ethylene cracking furnace during cracking process. Gas-liquid mixture is generated from the house-hold rubbish waste. A purifying device is connected with the ethylene cracking furnace.    USE - House-hold rubbish waste gasification method.    ADVANTAGE - The method enables generating high-level combustible gas from the rubbish waste, reducing energy consumption of the cracking furnace in an efficient manner and generating renewable energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a house-hold rubbish waste gasification method.'(Drawing includes non-English language text)'
NOVELTY - An auxiliary agent comprises 30-40 wt.% isopropyl alcohol, 1-7 wt.% n-butyl alcohol, 1-5 wt.% isobutyl alcohol, 1-5 wt.% dimethyl carbonate, 1-9 wt.% acetone, 5-15 wt.% methylal and 35-45 wt.% methyl tert-butyl ether.    USE - Auxiliary agent is used for vehicle gasoline (claimed).    ADVANTAGE - The auxiliary agent is environmentally-friendly, and has excellent workability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of auxiliary agent.
NOVELTY - A methanol fuel is obtained by mixing 5-85 wt.% methanol, 0.05-0.8 wt.% additive and remainder of gasoline or gasoline component oil, and uniformly stirring. The additive is n-octylamine.    USE - Methanol fuel is used for spark-ignition engine (claimed).    ADVANTAGE - The methanol fuel is manufactured efficiently and economically with excellent antiknock property, cold-starting property, corrosion resistance, swelling resistance and workability, and reduced energy consumption, by simple method.
NOVELTY - A biomass fuel comprises cow dung and straw. The mass ratio of cow dung and straw is 8-10.    USE - Biomass fuel (claimed).    ADVANTAGE - The biomass fuel is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass fuel, which involves pre-processing cow dung by crushing into block-shaped and dehydrating, drying, adding cow dung with straw into automatic drier, drying, feeding into a biomass briquetting equipment, packaging, and storing.
NOVELTY - A wine lees biomass fuel rod is prepared by performing acid-base neutralization by mixing with calcined lime, hot air drying fresh spent grain using discharged flue gas generated by spent grain boiler or high temperature steam generated by pent grain boiler heat exchanger, hot press forming at 140-180 degrees C temperature and 4-8 MPa pressure, packing, and storing.    USE - Preparation of wine lees biomass fuel rod (claimed).    ADVANTAGE - Wine lees biomass fuel rod is environment-friendly, energy-saving, and easy to be formed, has uniform particles, small diameter, and large amount of combustible components, and does not need crushing process.    DESCRIPTION OF DRAWING(S) - The drawing shows a work schematic diagram of preparing wine lees biomass fuel rod. (Drawing includes non-English language text).
NOVELTY - A biomass fuel contains 100 mass parts straw, 200 mass parts grain shell, 50 mass parts sawdust, 80 mass parts crushed wood, 120 mass parts wheat bran, and 30 mass parts wood leftover material.    USE - A biomass fuel (claimed).    ADVANTAGE - Biomass fuel is energy-saving, good clean energy source, convenient to use, environment-friendly, sanitary, and low in cost, has solid particles, high power density, small volume, high flash point, good combustion property, high burn-off rate, very low sulfur and nitrogen content, and low ash content, and utilizes agricultural and forestry waste, and preparation method is simple, has wide raw material source, and reduces production of black smoke.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of biomass fuel which involves placing components in crusher, crushing into powder, screening, drying, mixing in screw extruder, roll press forming into cylindrical particles, packing, and storing.
NOVELTY - A solid fossil fuel reaction device comprises reaction chamber (100) composed of feeding port (110) for input of solid fossil fuel to be reacted, discharge port (120) for discharge of reacted solid fossil fuel, and greater than or equal to 1 electromagnetic radiation entrance (200) which is composed of inlet end (210) embedded in reaction chamber for introducing electromagnetic radiation to react solid fossil fuel which has narrow inlet and widely structured outlet embedded in reaction chamber.    USE - A solid fossil fuel reaction device for coal, lignite, and/or semi-fumed coal (all claimed).    ADVANTAGE - Reaction device promotes complete reaction of electromagnetic radiation and solid fossil fuel, prevents electromagnetic radiation leakage, promotes safe and high efficiency electromagnetic radiation reaction process, and increases contact surface of electromagnetic radiation.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural schematic diagram of a solid fossil fuel reaction device.    Reaction chamber (100)    Feeding port (110)    Discharge port (120)    Electromagnetic radiation entrance (200)    Inlet end (210)
NOVELTY - A Jatropha curcas oil biodiesel is synthesized by heating J. curcas oil and silicotungstic acid in 250-ml 3-necked flask, adding methanol and latent solvent, mixing uniformity, carrying out reflux esterification at constant temperature, placing liquid in separatory funnel, and standing for layering in which upper layer is biodiesel and lower layer is glycerol, unreacted methanol, and catalyst.    USE - Synthesis of Jatropha curcas oil biodiesel (claimed).    ADVANTAGE - Process is simple and has easy separation, no emulsification, and no waste pollution.
NOVELTY - A crude castor oil biodiesel is synthesized by heating crude castor oil, discharging water until no bubbles, cooling, carrying out methanol pre-esterification, adding filtered oil, methanol, and catalyst into 3-necked flask with condenser, heating to predetermined temperature, cooling, transferring into separatory funnel, standing to divide into layers, discharging lower layer liquid in which supernatant liquid is crude biodiesel, adding acid and catalyst, repeatedly washing with distilled water, heating to remove water, and vacuum distilling to obtain yellow oil.    USE - Synthesis of crude castor oil biodiesel (claimed).    ADVANTAGE - Crude castor oil biodiesel saves energy and reduces pollution.
NOVELTY - A biodesel is prepared by heating at predetermined temperature refined cottonseed oil and potassium hydroxide and methanol from potassium alkoxide solution in 1000 ml 3-necked flask, stirring, stopping reaction at predetermined time, cooling to room temperature, transferring in 1000 ml separatory funnel, standing for layering, removing lower layer black liquid, collecting clear upper layer oil, vacuum distilling to remove excess methanol to obtain liquid oil which is cottonseed oil methyl ester, placing in 3-necked flask, and adding diethylene glycol monomethyl ether and potassium hydroxide.    USE - Preparation of biodesel (claimed).    ADVANTAGE - Process improves oxygen content, cetane number, and emission characteristics.    DETAILED DESCRIPTION - A biodesel is prepared by heating at predetermined temperature refined cottonseed oil and potassium hydroxide (KOH) and methanol from potassium alkoxide solution in 1000 ml 3-necked flask, stirring, stopping reaction at predetermined time, cooling to room temperature, transferring in 1000 ml separatory funnel, standing for layering, removing lower layer black liquid, collecting clear upper layer oil, vacuum distilling to remove excess methanol to obtain liquid oil which is cottonseed oil methyl ester, placing in 3-necked flask, adding diethylene glycol monomethyl ether and solid KOH powder, starting electric sets and stirrer, continuously distilling off methanol to ensure forward reaction, stopping reaction when no liquid drops from condenser, cooling, placing in separatory funnel, adding dilute hydrochloric acid solution, removing KOH, washing 2-3 times using saturated aqueous sodium chloride solution, and vacuum distilling to remove excess diethylene glycol monomethyl ether and water.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flowchart of preparing biodesel. (Drawing includes non-English language text).
NOVELTY - A biodiesel using cottonseed oil soap stock is prepared by placing 250 ml 3-necked flask in heating set with stirrer, condenser, and thermometer, adding fatty substance, methanol, and catalyst, stirring, refluxing, removing methanol, washing with water until neutral, heating, dehydrating, sampling, measuring acid value, adding deacidification agent according to measured amount of acid, filtering to obtain crude product, and vacuum distilling.    USE - Preparation of biodiesel using cottonseed oil soap stock (claimed).    ADVANTAGE - Process is simple and low cost, has high conversion rate, eliminates cottonseed oil soap-stock environmental pollution, and provides high quality environment-friendly combustion engine internal fuel.
NOVELTY - A non-drying compound fertilizer is granulated by mixing urea, monoammonium phosphate and potassium chloride, adding magnesium oxide powder and phosphoric acid solution binder, granulating, cooling, dedusting, classifying, coating, and packaging.    USE - Method for granulating non-drying compound fertilizer (claimed).    ADVANTAGE - The process has simple process flow, improved production efficiency, and reduced equipment cost, energy consumption and environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for compound fertilizer comprising 47 pts. wt. urea, 23 pts. wt. ammonium phosphate, 20 potassium chloride, 8-15 pts. wt. magnesium oxide and 3-6 pts. wt. phosphoric acid solution.
NOVELTY - Azadirachtin from neem seed and its derivative azadirachtinin are new.    USE - New azadirachtin and azadirachtinin compounds from neem seeds for preparing pesticide (claimed).    ADVANTAGE - The azadirachtin and azadirachtinin compounds are nontoxic and can be efficiently extracted from neem seeds using organic solvent.    DETAILED DESCRIPTION - Azadirachtin of formula (Ia) from neem seeds and its derivative azadirachtinin of formula (Ib) are new. INDEPENDENT CLAIMS are included for:    (1) preparation of azadirachtin and azadirachtinin; and    (2) pesticide comprising 20-80 wt.% azadirachtin and azadirachtinin, 2-20 wt.% dispersant, 3-5 wt.% disintegrating agent, 3-8 wt.% emulsifier, 0.2-2 wt.% adhesive, 0.5-10 wt.% surfactant and balance filler.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of preparation of azadirachtin and azadirachtinin. (Drawing includes non-English language text).
NOVELTY - A bacterial strain having improved organic solvent tolerance, is new. In the bacterial strain, fatty acid metabolism regulator protein (fadR) gene and multiple antibiotic-resistance repressor protein (marR) gene are inactivated.    USE - The bacterial strain, preferably Escherichia coli having improved organic solvent tolerance is useful for producing biofuel (all claimed).    ADVANTAGE - The bacterial strain mass produces biofuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing the above-mentioned strain; and #method for producing biofuel from biomass, involves culturing the above-mentioned strain.
NOVELTY - The method involves installing (S10) slurry feet at swinery. The large amount of air and raw water are injected (S20) into aeration tank of swine manure host processing field. The excrements of hog are fermented (S30). The decomposition of excrements is accomplished (S40) through fermentation process. The sludge in settling tank of swine manure host processing field is precipitated (S60). The sludge which is not completely disassembled through aeration/fermentation process is precipitated (S70).    USE - Method for processing manure from excrement of hog.    ADVANTAGE - The illness intrusiveness of hog is prevented by providing the sanitary swinery internal environment and the death percentage of hog is reduced effectively. The excrement handling cost and the chemical expense can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the process of processing manure from excrement of hog. (Drawing includes non-English language text)    Step for installing slurry feet at swinery (S10)    Step for injecting large amount of air and raw water into aeration tank (S20)    Step for fermenting excrements (S30)    Step for accomplishing decomposition of excrements through fermentation process (S40)    Step for precipitating sludge in settling tank of swine manure host processing field (S60)    Step for precipitating sludge which is not completely disassembled through aeration/fermentation process (S70)
NOVELTY - Method (M1) for increasing total fatty acid content and useful fatty acid ratio in microalgae, involves overexpressing FAB2 gene encoding stearoyl-acyl carrier protein desaturase protein in microalgae.    USE - The method (M1) is useful for increasing total fatty acid content and useful fatty acid ratio in microalgae. The transformed microalgae with increased total fatty acid content and useful fatty acid ratio is useful for producing biodiesel, where the fatty acid is oleic acid or linoleic acid (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) of producing transformed microalgae, involves introducing gene encoding stearoyl-acyl carrier protein desaturase protein FAB 2 in a wild-type microalgae;    (2) transformed microalgae with an increased total fatty acid content and availability fatty acid rate;    (3) composition comprising gene encoding stearoyl-acyl carrier protein desaturase protein FAB 2; and    (4) method (M3) of producing biodiesel, involves culturing microalgae capable of producing fatty acid and converting fatty acid into biodiesel.
NOVELTY - The energy neutral system has a carbon dioxide reservoir (31) to filter the carbon dioxide that is separated by a gas separation apparatus (27). A gas preservation apparatus (25) collects a biogas that is generated from a fermenting apparatus (17), which uses the excrements of the domestic animals. A livestock excretion reservoir (15) collects the excrements of the domestic animals. A livestock shed (13) is reclaimed to a lower portion of underground of a house (11) that breeds the domestic animal. An anaerobic fermentation tub (21) disassembles the carbonic acid gas and the methane gas.    USE - Energy neutral system for a greenhouse integrated with an underground swine house.    ADVANTAGE - The livestock shed is reclaimed to the lower portion of underground of a house that breeds the domestic animal, and thus maintains the inside temperature and humidity of the shed of the cattle, and hence improves the residential environment of the domestic animals and provides an environment-friendly nature. The fermenting apparatus uses the excrements of the domestic animals, and thus protects the global warming and protects the environment from getting contaminated, and hence promotes the photosynthesis of the plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an energy neutral system. (Drawing includes non-English language text).    House (11)    Livestock shed (13)    Livestock excretion reservoir (15)    Fermenting apparatus (17)    Anaerobic fermentation tub (21)    Gas preservation apparatus (25)    Gas separation apparatus (27)    Carbon dioxide reservoir (31)
NOVELTY - O-tert-butyl p-cresol and dicyclopentadiene in mass ratio of 1:1-5 are added to a catalyst and polymerized, to obtain phenolic petroleum resin. The phenolic petroleum resin, phosphoric acid and nickel oxide are subjected to alkylation reaction at 60-90 degrees C for 60-180 minutes in presence of catalyst and 1-3C saturated alcohol and unreacted raw materials are distilled under reduced pressure, to obtain asymmetric polymeric hindered phenolic antioxidant resin.    USE - Preparation of asymmetric polymeric hindered phenolic antioxidant resin (claimed).    ADVANTAGE - The method enables efficient and economical preparation of asymmetric polymeric hindered phenolic antioxidant resin with yield of 80% and having high antioxidant activity, thermal stability and compatibility. The resin is non-toxic and environmentally-friendly.    DETAILED DESCRIPTION - O-tert-butyl p-cresol and dicyclopentadiene in mass ratio of 1:1-5 are added to a catalyst and polymerized at 80-100 degrees C for 60-120 minutes and further reacted at 100-150 degrees C for 120-300 minutes, to obtain phenolic petroleum resin. The mass ratio of o-tert-butyl p-cresol and catalyst is 1:0.01-0.5. The ratio of o-tert-butyl p-cresol and solvent is 1:2-10. The phenolic petroleum resin, phosphoric acid and nickel oxide are subjected to alkylation reaction at 60-90 degrees C for 60-180 minutes in presence of catalyst and 1-3C saturated alcohol and unreacted raw materials are distilled under reduced pressure, to obtain asymmetric polymeric hindered phenolic antioxidant resin having brown appearance, average molecular weight of 600-1000 and softening point of 80-115 degrees C, and is soluble in acetone and aromatic solution, and insoluble in water and aliphatic hydrocarbon solvents. The ratio of o-tert-butyl p-cresol and alkylation catalyst is 1:0.01-0.2. The mass ratio of o-tert-butyl p-cresol and 1-3C saturated alcohol is 1:0.05-0.5.    n=1-4.
NOVELTY - Enhancing lignin degradation in solid fermentation, involves collecting Aspergillus oryzae, inoculating into expanding culture medium, performing shake flask cultivation in liquid medium, obtaining seed culture and inoculating on solid fermentation bed and fermenting to obtain product containing manganese peroxidase.    USE - The method is useful for enhancing lignin degradation in solid fermentation (claimed). The method is also useful for preparing bioethanol and biobutanol and feed using straw as raw material.    ADVANTAGE - The method is simple and doesn't cause pollution.
NOVELTY - A kind of liquid high temperature water processing straw device, especially the straw and device for fermenting to generate marsh gas and a liquid high temperature water treatment process. It is provided with baffle plate in the device, one side of the clapboard is on the upper part of the pre-processing device, a pre-processing device is a feeding port, a lower part is liquid high temperature steam generating device, wherein the lower device part is a discharging port, the other side is fermentation device, the inner part is a stirring device, the stirring device is on the rotating shaft device is connected with the lower end of the rotating shaft is set with a stirring paddle, the middle part is set with separating plate, rotating shaft of the stirring device passes through the separating plate. The time for fermentation of straw enter into pre-treating device by liquid high temperature water processing device for high temperature liquid water treatment, and carrying out pre-processing step, the stirring device can stir for fermentation, fermentation is separating plate at the lower part to prevent fermenting steam exploded wood fibre straw is not completely, improving the fermenting steam exploded wood fibre straw.
NOVELTY - Production of steam or hot water involves treating boiler wastewater and mixing with sludge substances and biomass.    USE - Production of steam or hot water (claimed).    ADVANTAGE - The method is carried out efficiently and economically by reducing discharge amount of chemical oxygen demand without causing pollution to environment.
NOVELTY - A hydrogen storage electrode alloy (I) is new.    USE - Hydrogen storage electrode alloy used for nickel-metal hydride secondary battery (claimed).    ADVANTAGE - The alloy has greatly improved service life, and stable electrochemical capacity. Its preparation process is easy to control.    DETAILED DESCRIPTION - A hydrogen storage electrode alloy of formula RE1-xMgxZryNizAlmBn is new.    x=0.2-0.3;    y=0.01-0.05;    z=3.0-3.5;    m=0.05-0.15;    n=0.0005-0.002; and    RE=La, Ce, Sm, Y, Nd or Gd.    An INDEPENDENT CLAIM is included for preparation of hydrogen storage electrode alloy.
NOVELTY - A solid acid catalyst used as additive for preparing biological diesel oil, contains sulfonated acid carbide and glycerol.    USE - Solid acid catalyst is used for esterification of oleic acid with ethanol for preparing biodiesel oil (all claimed).    ADVANTAGE - The solid acid catalyst has high catalytic activity, and produces biodiesel by esterifying oleic acid and ethanol at high esterification rate of 92.5%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of solid acid catalyst, which involves adding glycerol in a beaker, adding preset amount of sulfuric acid, mixing uniformly, placing on hot plate, heating gradually to preset temperature for 20-40 minutes, carbonating sulfonated glycerol, heating, cooling to room temperature, washing under stirring condition, and placing in an oven for drying.
NOVELTY - Decolorization method of resin biodiesel byproduct glycerine involves soaking ethanol macroporous resin, washing using deionized water, passing hydrochloric acid through resin, soaking, washing using deionized water into neutral, passing sodium hydroxide through resin column, soaking, adding crude biodiesel byproduct glycerol and deionized water, adjusting pH value of sulfuric acid solution, centrifuging, standing layers, adding macroporous resin and glycerine using static adsorption, measuring pigment absorption wavelength and calculating decolorization rate.    USE - Decolorization method of resin biodiesel byproduct glycerine (claimed).    ADVANTAGE - The method economically enables the decolorization method of resin biodiesel byproduct glycerine having high adsorption efficiency and durability.    DETAILED DESCRIPTION - Decolorization method of resin biodiesel byproduct glycerine involves soaking 95% ethanol macroporous resin for 24 hours, washing using deionized water until there is no alcohol taste, passing 5% hydrochloric acid through resin, soaking for 2-4 hours, washing using deionized water into neutral, passing 2% sodium hydroxide through resin column, soaking for 2-4 hours, washing using deionized water into neutral, adding crude biodiesel byproduct glycerol and deionized water in the volume ratio of 6:1, adjusting pH value of 50% sulfuric acid solution to 4.5-5.5, centrifuging for 15-20 minutes at speed of 3000-4000 rpm, standing layers, adding liquid in the container in the ratio of 0.25-2, adding macroporous resin and glycerine using static adsorption for 15-30 minutes, measuring pigment absorption wavelength and calculating decolorization rate. The lower layer is glycerin layer.
NOVELTY - Mesophilic anaerobic method for fermenting wheat straw, involves (a) naturally drying wheat and rice, and crushing to 2 cm, (b) adding 5-10% biogas residue with respect to wheat straw, adding mixture to fermentation bottle and fermenting at 30-35 degrees C, and (c) collecting gas using discharging method.    USE - The mesophilic anaerobic method is useful for fermenting wheat straw (claimed) which is used as fertilizer.    ADVANTAGE - The method provides high yield and can be taken for long period of time, requires less energy consumption, and does not need dehydrating residues.
NOVELTY - This new type utility claims one using a solid elastic stuffing of marsh gas biological desulphurization device, comprising a desulphurization tower, a filler layer is set in the said of biological desulphurization tower, gas inlet of the lower part of a biological desulfurizing tower, gas outlet of said biological desulphurization tower top part, spraying liquid inlet is set on the top part of said of biological desulfurizing tower, spraying liquid outlet is a biological desulfurizing tower of the lower part of said filling layer using solid elastic stuffing layer, elastic padding layer comprising a filler and shell filler is set on the shell of solid elastic stuffing. The marsh gas biological desulphurization device using solid elastic filling layer, an elastic padding large specific surface area of filler layer structure can be enriched and microorganism and an external sphere, elliptical and polygonal body blocking and short structure can maintain of gap between the filler, the filler layer of. The solid elastic stuffing biogas bio-desulfurization device of long service life, good desulphurization effect.
NOVELTY - This utility new type relates to one and a biomass forming, the crusher one end connecting with a conveying belt A of raw material, and the other end of it through a conveying belt B is connected with the crusher, the crusher and the bag-type dust remover is connected with the bag-type dust remover is connected with the dusting machine A is connected, dust remover by A conveying belt C and the auger for material machine of biomass particle, the biomass granulator other end through a conveying belt with product particles storage bin. Rear raw material entering into crusher chord up taking the crusher crushing, crushing the raw material in rear with possible under the roller wheel with the effect of upper conveying belt B of iron process, after removing the crushing of raw materials in a crusher process crushing, entering into process and collected by the dust remover, and then sent to the biomass particle machine in process and by the hinge, and finally for particle process dust-removing processing rear stored product particles in process storage system is simple, each link.
NOVELTY - This utility new type claims a one algae slag harmless resource processing system, comprising a water body one side bank of nano-bubble generating device is set on the upper of dragging device set on the scum storage mechanism and dehydration device, nano-bubble generating device of nano-bubble generating device one side one side is further provided with a rear for fermentation and scum of rotating fermentation device, dehydrating device comprises a self-sucking water pump and is provided with an opening of tube, self-sucking water pump of opening of input end and tightly connecting tube, upper tube is provided with a small hole and is coated with at least one layer of filter film, tube is set on the slag storage mechanism, the utility model is new type nano-bubble generating device produce the nano-bubble of the water body of the algae in water body floating on the water surface floating up, taking rear floating process dehydration treatment, then fermenting organic fertilizer for water will not cause second pollution, it can reach completely of algae floating in water, and the can be used as the regeneration of resource utilization.
NOVELTY - This utility new type relates to sludge treatment technology, especially relates to a sludge treatment of one special device. Special device of a sludge processing one of claims, comprising a original sludge metering hopper (1), original sludge feeding belt machine (2), a solid additive metering hopper (3), a sludge stirring device (15), a sludge feeding material distributing system (4), a sludge of rear measuring and feeding device (6) of the feeding belt machine rear sludge dehydrator (7), auxiliary storage metering and conveying system, a main station (10), stirring and mixing main machine (11) and a finished product fuel discharging belt machine (13) and control system (14). This utility new type small floor area, processing abiligy, using control system control, saves labour and operation intervention, the product property and combustion and so on each index can reach the national standard, sludge harmless and resource processing treatment of ideal device.
NOVELTY - A fermenting device of liquid fertilizer one stirring device with at least one power connecting device for stirring to biological and at the same time heating the fertilizer can accelerate the fermentation, comprising: at least one stirring groove, and form one containing space with one space fill the groove wall, and is provided with at least one the first input hole and at least one first output hole, at least one heating device is set on one side of the stirring tank of, and with the fill space connecting to the one hot source input with the leading-out, and form circulation, at least one stirring device is set in the stirring groove, and to drive the bio-fertilizer by the stirring power device. Hot source of the maintain circulation of temperature in the stirring tank, accelerating biological fermenting device of liquid fertilizer and the effect and to shorten the processing time of all kinds of fertilizer and improve yield and reduce the manufacturing cost.
NOVELTY - A portable one fermenting steam exploded wood fibre straw bag, belonging to the fermenting steam exploded wood fibre straw device technology field. The inner frame comprises supporting body of the plastic bag, the plastic bag. The upper end is opening structure, the plastic bag is set in the water supply tube and oxygen supply tube, water supply tube and upper oxygen supplying tube are provided with a round hole, the rear upper end of the water supply tube extends out the plastic bag with the water supply connecting device, rear oxygen supply tube lower end extends out the plastic bag with the air connecting device. Said one of a portable fermenting steam exploded wood fibre straw bag is one a fool, portable compost operation device, it can realize straw compost field in the field, with the operation is convenient, process is simple, saves manpower and material resources, reduces the large area open compost, protects environment, improves of compost efficiency.
NOVELTY - This utility new type claims a one organic fertilizer rod, comprising a film bag and rear clamping device, film charging bag is cylindrical, one a bio-degradable film, fill organic fertilizer powder, one end is an opening, the opening end by the clamping device clamping. This utility new type has simple structure, convenient use, suitable for the organic fertilizer production forming. Using the technical production of organic fertilizer product according to the dosage of a certain proportion directly on the field, time it not only solves the problem that the existing organic fertilizer powder using dust is large, the phenomenon of polluting the environment, but also solves the problem that the time and organic fertilizer in the field distribution uniformity of.
NOVELTY - This new type utility claims one using a mixing tower of biological oil preparation device, comprising a reactor, reaction furnace, a pressure gauge, a collecting tube, mixing tower cooler, a pressure cylinder, a pressure regulating valve, a vacuum pump, a gas collecting bag, a stop valve, a nitrogen bottle, the reactor is set on the reaction furnace, upper reactor by the pipeline through the pressure gauge connecting rear tower cooler of the mixed gas inlet connecting, mixing tower cooler of air outlet connecting a pressure cylinder, a pressure cylinder is provided with two outlets, one outlet by pipeline through valve connecting to the vacuum pump, and the other one outlet pipeline through the check valve connecting the nitrogen bottle, a vacuum pump outlet connecting set. This utility new type of reaction device, simple and reliable structure, using the integrated design of the mixed column to ice water mixture cooler as cooling medium, the preparation is convenient, it is easy to realize, which is good for pushing vacuum pyrolysis technology of wide application.
NOVELTY - This utility new type provide a one for separating catalytic cracking dry gas of device, relating to petroleum and chemical industry technology field, concretely, it is a one using membrane separation and cryogenic separation coupling technology, multi-target at the same time recycling catalytic cracking dry gas of method and device, comprising a buffer tank, a compressor, a gas-liquid separator, a filter, a heater I, a heater II, a heater III, IV heater, hydrogen membrane system, a refrigeration compressor, a cold box, an organic steam film, demethanizer, deethanizer tower and a fuel gas tube network. The device replaces the pure of cryogenic separation process, small floor area, low investment, simple structure, high recovery rate of hydrogen and light hydrocarbon is more than 99%, and it has good economic benefit and social benefit of environment benefit, can the petroleum and chemical industry.
NOVELTY - This utility new type claims a multifunctional combination-type one biomass semi-gasification device, comprising a shell, an igniter, a combustion-supporting material room and semi-gasification chamber, an igniter, a combustion-supporting material room and semi-gasification chamber are set in the shell, said material seal room is set up material room is provided with a feeding port, upper port is provided with a seal cover, the upper shell is provided with an exhaust port, a flame lighter and combustion-supporting connecting, combustion room connecting with the material, the material room and the half gasification chamber connect, semi-gasification chamber connect with the air outlet. The multifunctional combined type biomass semi-gasification device of biomass gasification device each are combined into one integrated device, save device resource, which greatly reduces cost, using lighter and combustion-supporting the biomass raw material of flame combustion, and semi-gasification room for mixed gas taking futher gasification, obtain the combustible gas, suitable for a combustible gas is not high cleanliness of field.
NOVELTY - This utility new type claims a multifunctional combination-type one biomass full-gasification device, comprising a shell, a combustion storehouse, a gasification room and cleaning room, combustion-supporting material storehouse, gasification room and cleaning room are set in the shell, a combustion-supporting is set at the bottom of shell, bin is set on the combustion-supporting upper surface of the gasification room is set on the top of material bin, a purifying room is set on the gasification room of the top part, a material storehouse seal, side surface of material bin is provided with a feeding port, the feeding port is provided with a seal cover, upper side surface of the shell is provided with an air outlet, said air outlet in purifying room of. This utility new type biomass gasification device each are combined into one integrated device, save device resource and greatly reduce the cost by the first-stage gasification room, second level gasification room and cleaning room for the smoldering rear obtain of biomass gas purifying process, obtain clean combustible gas is suitable for a combustible gas for high cleanliness.
NOVELTY - One upper absorbing type pressurizing a biomass straw gasification furnace, belonging to the biomass energy can be recycled to the technical field. Wherein the gasification furnace is a steel material, is provided with an annular water groove and embedded hydraulic seal is covered on the upper port in the furnace is set pressing stirring device, feeding time seal inner cover and furnace pressure material device is separating status, the operation time in the seal cover and the furnace pressure mixing device is linked status of gasification furnace is set in upper area and lower room, the upper room is gasification room area and the preparatory material, the lower area room is high temperature oxidation room, the outdoor measuring region diffusion around the pre-heating room of the annular cavity structure of the oxidation area. Gasification agent by the pressure is not less than 35 Pa of pressure air pump provide, pressure air pump pumping the diffusion gasification agent pre-heating room, the pre-heating room, heating by necking oxidation zone room at the bottom center 20, the diameter of the throttle hole of 5 entering into gasification furnace in gasification of raw material, and connecting the pre-heating room out hot air with the stove head air distribution valve.
NOVELTY - This utility new type relates to a one of air distribution device comprises a biomass fixing bed gasification furnace said air distribution device comprises an air pipeline and a blower, wherein said air pipeline is composed of 1 air inlet main pipe and the air inlet 4 of the tube, said air inlet main pipe from said gasification furnace top of one side, extends downwards to the gasification furnace main body height of the gasification furnace 1/3 at the center axis of folding, separating 4 uniformity distribution on said air inlet main pipe upper end tube wall of the air inlet tube, a 4 air inlet tube to the four directions are downwards extended to the radial size of the folded 1/2 gasification furnace until the distance a gasification furnace 1/3 gasification furnace height, and the size of the air inlet main pipe of size 1/2. Said air distribution device provide sufficient uniformity of contact with the raw material of preheating, gasifying medium can be valid to solve in gasification furnace in running process of air distribution is not uniformity of reaction is not caused by uniformity and layer temperature difference is large, it valid improves the gasification efficiency and the yield rate of ash, which is good for high-efficient stable of gasification furnace.
NOVELTY - This utility new type provide the one flammable gas chemical composition of a purifying system, in particular one a biomass fuel gas purifying system, comprising the first water washing tower, a second water washing tower, a first purifier, a second purifier, a first valve, a second valve, a third valve, a fourth valve and a connecting pipeline. Washing gas through first and second water washing water washing tower of the tower top part of water after washing of heavy tar and dust particles in biomass fuel gas, the fuel gas after washing of the adsorption of purifier to remove light tar of fuel gas and water in gas of the output meet the standard. Is provided with storage box bracket in the first purifier and the second purifier, the upper bracket can be detachably placed on storage box, the storage box is filled in, the purifying time is saturated, the process for replacing, and four valve is closed by the combination to make the whole system can continuously operation time in the replacement purifying agent.
NOVELTY - This utility new type relates to one a biogas bio-desulfurization device, especially relates to a biological desulfurizing tower filling one washing device. The bottom of the biological desulfurizing tower filler washing device, a desulfurizing tower is lengthways arranged with multiple filling layer, comprising a water inlet tube, a drain tube and through hole aeration disc, the water inlet tube, the drain tube of the desulfurizing tower, the lower part of the filler layer are each provided with a through hole aeration disc, the aeration disk through hole is connected with the air source, the lower part through hole aeration disk is densely distributed with aeration holes. This utility new type has the valid one by one cleaning process for filling layer, the filling layer is blocked, the filling layer for desulfurizing effect of marsh gas, short time and improve the efficiency of cleaning, the beneficial effects so as to improve the efficiency of marsh gas.
NOVELTY - This utility new type relates to a biomass forming particle one machine between the wheel support plate and the bearing base of dust-proof structure is provided with an opening on the upper wheel supporting plate, the opening plate is provided with a groove in the upper bearing base, the positon of scraping plate corresponding to the groove of bearing base. Using the scraping plate at the accumulation of dust, dust-proof structure of simple structure, preventing the dust accumulation, it will not produce dust sintering phenomenon, reduces the working temperature of the whole machine, which is good for improving the service life of the whole machine.
NOVELTY - This utility new type relates to one a large biomass forming, stacking the wet region and dry region by the stacking machine and a crusher respectively connected with the wet material conveying device and a material conveying device is connected with wet material conveying device and conveying system and drying with drying hopper, drying bin, conveying device and the material storage hopper is connected with the material storage hopper is respectively connected with the recycling room and powder material lifting belt is connected with the powder material lifting belt and the material distributing system, distributing system and the platform of storage hopper is connected, the platform of storage hopper and feeding device, the feeding device by the finished product cooling exhaust device, a finished product conveying device classifying screen is connected with the roller, the roller grading through lifting conveying system and the particle finished goods barn and packing system. System is simple, each link, high degree of automation, reduces labour and reduces the cost.
NOVELTY - This utility new type provide a one biological fuel station. This utility new type comprising a steel structure, a steel structure is provided with upper algae photo-biological reaction tube, a algae photo-biological reaction tube space of algae, algae reservoir connecting with said algae photo-biological reaction tube and algae circulating tube, a algae circulating tube and processing system, a processing system with the output pipeline, the output pipeline is connected with the oil storing tank. This utility new type can time the algae into biological diesel oil, the utilization rate is high, the energy regeneration.
NOVELTY - Input output device and electrolysis device this utility new type relates to one a hydrogen oxygen generating system, comprising a supporting device and is set up on the supporting device of connected of the hydrogen oxygen device and power supply device, the hydrogen oxygen generating device comprises a control device and a control of the connecting of the, wherein, the power supply device is a one or two a hydrogen oxygen generating device further comprises a shell, control device is set inside of shell, an input output device passes through the shell, electrolysis device is set in the shell, an input output device and electrolysis device in solar battery plate and wind power generator of from up to down are connected in turn, the input output device and the power supply device are connecting. This utility new type structure to simple optimization of the light energy, wind energy can obtain full use of renewable energy source, reduces the time of system device cost and saves a lot of energy, which greatly improves the safety stability of green production of hydrogen and oxygen, it saves efficiency of green environment-friendly production and is suitable for the related production field of industrial popularization and application.
NOVELTY - This utility new type relates to a one pure water electrolysis hydrogen generator, comprising one side is provided with a drain tube, and the other side is provided with a cylindrical tube of the water tank, the other side of water tank is provided with a hydrogen generating device. Said hydrogen generating device comprising an anode room and cathode room, one side said anode room is provided with inserted of the water inlet tube of the water tank cylinder tube, said anode room and two sides of the inner end part of the cathode room of plate groove are respectively provided with a plate groove is provided with an anode plate and cathode plate, said anode plate and the cathode plate is provided with electrolytic film. Said upper anode plate and cathode plate respectively connect with anode room and cathode respectively extend outside of anode plate and cathode plate screw screw, said anode room is set on the top of air inlet tube is set on the upper end of the water tank is connected with an exhaust tube, a cathode room of one side upper end is provided with a hydrogen tube. This utility new type has a mounting and is convenient to disassemble and easy to change, can be valid to prevent leakage and can reduce the manufacturing cost and maintenance cost and so on.
NOVELTY - Device comprises a pipeline, which connects stirring tank (3) and reaction kettle (10). The top end of the stirring tank is provided with a feeding port (1), and the bottom end of the stirring tank is provided with a discharging port (11). A stirring device is also provided which is turbine stirrer, spiral propeller type stirrer, paddle type stirrer or inclined paddle type stirrer. A top end of pressure reaction kettle is provided with the feeding port, a pressure gauge (7), a thermometer (8), and bottom end of pressure reaction kettle is provided with a discharging port.    USE - Device used for producing fuel (claimed).    ADVANTAGE - The device ensures the production of fuel in an efficient, eco-friendly and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing fuel, which involves:    (A) mixing (in pts.wt.): methanol (40-60), diesel (10-30), dimethyl methacrylate (1-5), barium sulfonate (0.2-1), fatty acid (1-3), phosphate ester (0.2-1), butene sulfide (0.2-1), methyl silicone oil (1.2-2) and sodium phosphate (1-5) uniformly at room temperature in stirring tank;    (B) transferring the obtained mixture into reaction kettle and then adding methanol, diesel, barium sulfonate and sodium phosphate;    (C) processing the obtained mixture for 1-4 hours; and    (D) filtering the obtained mixture to obtain fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel producing device.    Feeding port (1)    Stirring tank (3)    Pressure gauge (7)    Thermometer (8)    Reaction kettle (10)    Discharging port (11)
NOVELTY - Preparing ruthenium catalyst involves impregnating biomass for 2-8 hours in alkali solution (hydroxyl ion concentration is 3-7 mole/L). The mixture is filtered to obtain residue that is cracked in nitrogen atmosphere at 500-1000 degrees C for 15 hours. The obtained residue is washed with deionized water and then impregnated in strong acid solution (hydrogen ion concentration is 0.5-2 mole/L) for 3-8 hours to obtain activated carbon. Carbon is refluxed in nitric acid (0-65 %) for 3-10 hours. The refluxed mixture is washed with deionized water, heated and dried.    USE - Method for preparing ruthenium catalyst used for reducing methane (claimed).    DETAILED DESCRIPTION - Preparing ruthenium catalyst involves impregnating biomass for 2-8 hours in alkali solution (hydroxyl ion concentration is 3-7 mole/L). The mixture is filtered to obtain residue that is cracked in nitrogen atmosphere at 500-1000 degrees C for 15 hours. The obtained residue is washed with deionized water and then impregnated in strong acid solution (hydrogen ion concentration is 0.5-2 mole/L) for 3-8 hours to obtain activated carbon. Carbon is refluxed in nitric acid (0-65 %) for 3-10 hours. The refluxed mixture is washed with deionized water, heated and dried. The dried mixture is stirred ultrasonically with ruthenium salt solution (0.01-0.5 mole/L) and then dried to get ruthenium catalyst.
NOVELTY - This new type utility claims one applied to a biomass hot blast system of industrial coating line, to makes full use of biomass fuel, reduces the environment pollution and reduce the cost. The biomass hot blast system comprises upper suction type fixing bed gasification furnace, a burner, a hot air boiler and drying room, gas output pipeline of the burner upper suction type fixing bed gasification furnace, a hot air boiler comprising a combustion hearth and around the combustion hearth of the heat exchange pipe, the heat exchange pipe is provided with an air inlet in the nozzle of a burner extends into the combustion chamber of a hot air furnace, drying room comprises of the cold hot air temperature regulating chamber and drying chamber, a heat exchange pipeline of hot air furnace via the hot air conveying pipeline and the drying room of cold-hot air temperature regulating chamber is connected with cold and hot mixing temperature adjusting chamber is provided with a cold air inlet, a drying chamber is provided with a waste gas outlet. This utility new type using upper suction type fixing bed gasification furnace is the biomass fuel gas, and is directly sent to burner, realizes the full use of hot source, reduces the operation cost of the enterprise.
NOVELTY - Manufacture of solid catalyst involves dissolving ferrous sulfate and ferric sulfate in distilled water, adding concentrated aqueous ammonia, adjusting pH to more than 8, stirring, forming black precipitate, decanting supernatant solution, filtering, washing and drying, forming magnetic matrix, impregnating magnetic matrix in magnesium acetate solution, drying, calcining under nitrogen atmosphere, forming magnesium oxide/magnetite magnetic carrier, impregnating the magnetic carrier in 20-25% calcium acetate solution and calcining at 500-600 degrees C for 2 hours.    USE - Manufacture of solid catalyst used for biodiesel (claimed).    ADVANTAGE - The solid catalyst is manufactured efficiently with excellent catalytic activity and productivity, by simple method.    DETAILED DESCRIPTION - Manufacture of solid catalyst involves dissolving ferrous sulfate and ferric sulfate in mass ratio of 1:2 in 250-500 mL distilled water, adding 20% concentrated aqueous ammonia, adjusting pH to more than 8, stirring, forming black precipitate, decanting supernatant solution, filtering, washing, drying at 50-60 degrees C for 8-10 hours, forming magnetic matrix, impregnating magnetic matrix in 20-25% magnesium acetate solution, drying at 50-60 degrees C for 8-10 hours, calcining at 500-600 degrees C for 2-4 hours under nitrogen atmosphere, forming magnesium oxide/magnetite magnetic carrier, impregnating the magnetic carrier in 20-25% calcium acetate solution and calcining at 500-600 degrees C for 2 hours. The total content of ferrous sulfate and ferric sulfate is 30-50 g.
NOVELTY - Catalytic preparation of solid catalyst for bio-diesel involves: making solution A: adding 0.01-0.02 mol potassium ferrocyanide to 40-80 ml water; making solution B: adding 0.1-0.2 mol zinc chloride in 10-20 ml water and 10-20 ml tertiary butyl alcohol; making solution C: dissolving 30 g polyethylene glycol in 80 ml tert-butanol; at constant temperature of 45-50 degrees C under magnetic stirring solution C slowly dropwise adding into solution A, then dropwise adding solution B to form precipitate, continuously stirring for 1-1.5 hours, then filtering and vacuum drying 50-60 degrees C for 6-8 hours.    USE - For catalytic preparation of solid catalyst for bio-diesel (claimed).    ADVANTAGE - The present catalytic process provides high efficiency; is simple; and is suitable for industrial production. The solid catalyst obtained by the present process is non-corrosive and reusable.
NOVELTY - This new type utility claims one a disease livestock and poultry dead of processing device, in particular a one animal harmless biological processing special device, the utility model is new type aims to provide one of a full-seal, small floor area is small, the processing process is simple, reduces the labour intensity and the safety of animal harmless biological processing special device, it comprises a segmentation mechanism, a gas valve, a sterilizing container, storage distribution module, a fine crushing machine, mixing machine, auxiliary machine and so on, it is provided with simple structure, convenient use and reasonable design and so on.
NOVELTY - Preparing substrate involves pulverizing vegetable stump to adjust carbon and nitrogen ratio to 22-25 and moisture content to 55-57%. The vegetable stump comprises spinach stump, cucumber residual strain and eggplant stump in volume ratio of 2:3:2. Bacterial cells (more than 2asterisk109 colony forming unit per gram), enzyme and chicken manure are added to vegetable stump and then decomposed for 3 days. Humus, ash, rapeseed cake, ammonia water and garlic powder are added to obtain substrate and then pH value is adjusted.    USE - Method for preparing substrate (claimed) used for cultivating lettuce seedling.    ADVANTAGE - The method enables to prepare substrate in simple, eco-friendly and cost-effective manner.
NOVELTY - Organic fertilizer preparation involves utilizing (in wt.%): dry sludge (50-70), maifanite (5-10), fluoride powder (5-20), auxiliary agent (20-30) and bio-fermentation agent (0.1-0.3).    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer in simple and cost-effective manner.
NOVELTY - A sulfuric acid from biodiesel waste oil is prepared by collecting waste acid, heating at 70-80 degrees C under - 0.098 MPa, removing water and methanol, purifying, dehydrating, lowering temperature at 50-60 degrees C, stirring, pouring waste sulfuric acid, and filtering.    USE - Method for preparing sulfuric acid from biodiesel waste oil (claimed).    ADVANTAGE - The method is environment-friendly. The sulfuric acid has high concentration.
NOVELTY - A wet sludge drying device comprises discharge funnel (2), granulating roller (1), drying chamber (7), conveyor belt (6) and scraping plate (4). Wet sludge is dried by starting drying device, feeding wet sludge into discharge funnel, granulating, drying in drying chamber, monitoring moisture content, and ending drying when moisture content is less than set value.    USE - Wet sludge drying device.    ADVANTAGE - The process reduces energy consumption and drying time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of wet sludge drying device.    Granulating roller (1)    Discharge funnel (2)    Scraping plate (4)    Conveyor belt (6)    Drying chamber (7)
NOVELTY - Nutritious soil comprises 30-70% dried peat moss, 10-30% dried chicken manure at high-temperature, 10-50% dried cow dung at high-temperature, 5-10% seaweed powder, 3-5% fermented protein composition, and 1-5% potassium humate.    USE - The nutritious soil is useful for inducing root growth of blueberry seedling (claimed).    ADVANTAGE - The nutritious soil enables to induce root growth diameter to greater than 3 cm.
NOVELTY - Purification of crude glycerine waste oil comprises adding 20-30 wt.% diluent to crude glycerine waste oil; adjusting pH value to 6-7, stirring at room temperature, heating to 60-70 degrees C, adding 5-10 wt.% activated clay, heating to 100-120 degrees C, stirring, vacuum filtering to remove impurities, and refluxing; adding 5-10 wt.% sodium chloride, heating to 80-90 degrees C, stirring, and filtering; and vacuum distilling at 164-204 degrees C to obtain refined glycerine.    USE - Method for purifying crude glycerine waste oil (claimed) used for producing biodiesel.    ADVANTAGE - The method has high quality refined glycerine, is simple, has high product yield, and avoids environment pollution.
NOVELTY - Synthesis of vanillin comprises isomerizing natural eugenol and alcohol organic solvent in the presence of alkali catalyst, diluting, washing with alkali solution, extracting, acidifying, extracting, distilling under reduced pressure, and crystallizing.    USE - Method for synthesis of vanillin (claimed).    ADVANTAGE - The method achieves vanillin yield of up to 95%, avoids isomerization process using carbonyl iron and other toxic catalysts, can recycle extractant, and has simple and easy to operate post-treatment process and reduced cost.
NOVELTY - 25-hydroxycholesterol (I) is synthesized by adding acid binder, 4-dimethylaminopyridine catalyst, 24-dehydrocholesterol, acid anhydride and/or acyl chloride to solvent, and reacting at not less than 10 degrees C for 10-24 hours; adding manganese salt catalyst, epoxidation reagent and solvent, performing epoxidation at - 20 to - 1 degrees C for 1-3 hours, filtering, diluting, extracting, vacuum drying, and purifying by column chromatography; and adding reducing agent, carrying out ring-opening reaction at 20-70 degrees C for 3-8 hours, cooling, pickling, extracting, washing, vacuum-drying, and recrystallizing.    USE - Method for synthesizing 25-hydroxycholesterol (claimed).    ADVANTAGE - The environment-friendly synthesis has non-toxic and low-cost reagents, mild reaction conditions, and high selectivity.    DETAILED DESCRIPTION - 25-hydroxycholesterol of formula (I) is synthesized by:    (A) adding acid binder, 4-dimethylaminopyridine catalyst, 24-dehydrocholesterol, acid anhydride and/or acyl chloride to solvent, and reacting at not less than 10 degrees C for 10-24 hours;    (B) adding manganese salt catalyst, epoxidation reagent and solvent, performing epoxidation at - 20 to - 1 degrees C for 1-3 hours, filtering, diluting, extracting, washing, vacuum drying, and purifying by column chromatography; and    (C) adding reducing agent at molar ratio of 2-6:1, carrying out ring-opening reaction at 20-70 degrees C for 3-8 hours, cooling, pickling, extracting, washing, vacuum-drying, and recrystallizing.    Molar ratio of 24-dehydrocholesterol, acid anhydride/acyl chloride and acid binder is 1:1.2-2:1.8-10. Mass ratio of 4-dimethylaminopyridine and 24-dehydrocholesterol is 0.005-0.05:1. Molar ratio of first reaction product, epoxidation agent and manganese salt is 1:1-4:0.01-0.1.
NOVELTY - This utility new type relates to one a desulfurization system, specifically to a marsh gas generating one desulphurization system, comprising a desulfurizing tank, an air inlet tube, an air outlet tube and control valve, said air inlet tube and desulphurization tank is connected with the bottom, the air outlet tube and desulphurization tank is connected with control valve are provided with upper air inlet tube and the air outlet tube is provided with two parallel of the desulfurizing tank in the marsh gas power generation and system, and is set with an air inlet pipe and an air outlet pipe, a desulfurizing tank is led out of two air inlet tube, an air outlet tube are respectively connected with the air inlet pipe and the air outlet pipe. Time using this utility new type marsh gas power generation and system not only can guarantee the marsh gas when large amount of lower and completely, and needs to be repaired, it can ensure the continuous power generation.
NOVELTY - A continuous outer hot vertical type biomass pyrolysis carbonization device comprises feeding system, carbonization reactor (6), carbon discharging system, and purifying system. The feeding system comprises first-stage spiral feeding conveyor (1), feeding tank (3), second level feeding screw conveyor (5), and buffer feeding box (3). The carbon discharging system comprises discharging and cooling tube (7), spiral discharging conveyor (8), first-stage carbon storage tank (9), second level storage carbon box (11), and movable carbon box (13).    USE - Continuous outer hot vertical type biomass pyrolysis carbonization device.    ADVANTAGE - The device has simple structure and provides high yield with stable quality.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the continuous outer hot vertical type biomass pyrolysis carbonization device.    Feeding conveyor (1)    Buffer feeding box (3)    Feeding tank (3)    Second level feeding screw conveyor (5)    Carbonization reactor (6)    Cooling tube (7)    Spiral discharging conveyor (8)    First-stage carbon storage tank (9)    Second level storage carbon box (11)    Movable carbon box (13)
NOVELTY - A straw bio-char is prepared by naturally drying straw to make the water content be 10%, and crushing into powder grain of 2-10 mm; placing crushed straw in biomass carbonizing furnace, and performing anoxic carbonization decomposition at 300-500 degrees C; and cooling, taking out, crushing, passing through 100-200 meshes sieve to obtain straw biomass carbon powder.    USE - Method for preparing straw bio-char (claimed).    ADVANTAGE - The method is simple, and reduces cost in the transportation process.
NOVELTY - An environmentally-friendly bio-alcohol fuel oil is obtained by mixing 60-90 wt.% methanol, 1-30 wt.% ethanol, 1-10 wt.% water, and 1-10 wt.% additive, and stirring.    USE - Environmentally-friendly bio-alcohol fuel oil (claimed).    ADVANTAGE - The environmentally-friendly bio-alcohol fuel oil has reduced energy consumption, and is nontoxic, and tasteless.
NOVELTY - An industrial fuel comprises coal tar, xylene, ethyl acetate, methanol, ethanol, and propyl triazole containing benzene sulfonic acid barium(sic) as additive.    USE - Industrial fuel (claimed).    ADVANTAGE - The industrial fuel is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of industrial fuel, which involves adding raw material, heating and refluxing, obtaining solution, dissolving obtained solution in mixed solution at 20-30oC, adding mixed solution to the methanol and ethanol in the mixed solution, and stirring.
NOVELTY - Preparation of bio-oil involves pre-processing waste oil in an oil tank to remove impurities, degumming, decoloring, dehydrating, obtaining standard raw material oil, adding 30-40 pts. wt. ethyl acetate and 40-50 pts. wt. ethanol, stirring, adding 5-10 pts. wt. potassium hydroxide, stirring for 8-12 minutes, adding 5-10 pts. wt. sodium hydroxide, stirring for 15-25 minutes, adding 70-80 pts. wt. resultant mixture (A), 5-10 pts. wt. emulsifying agent and 10-15 pts. wt. water into a reactor, adding 5-10 pts. wt. oleic acid, oiliness agent and quality improver, stirring and curing.    USE - Preparation of bio-oil (claimed).    ADVANTAGE - The method provides bio-oil, by simple and environmentally-friendly process. The bio-oil does not contain plumbum and hydrargyrum.    DETAILED DESCRIPTION - Preparation of bio-oil involves pre-processing waste oil in an oil tank to remove impurities, degumming, decoloring, dehydrating, obtaining standard raw material oil, adding 30-40 pts. wt. ethyl acetate and 40-50 pts. wt. ethanol, stirring uniformly for 3-8 minutes in rate of 280-320 rpm, adding 5-10 pts. wt. potassium hydroxide, stirring for 8-12 minutes, adding 5-10 pts. wt. sodium hydroxide, continuously stirring for 15-25 minutes, maintaining the resultant mixture for 1-5 hours, adding 70-80 pts. wt. resultant mixture (A), 5-10 pts. wt. emulsifying agent and 10-15 pts. wt. water into a reactor, adding 5-10 pts. wt. oleic acid, stirring for 30-60 minutes, adding oiliness agent and quality improver, stirring for 20-30 minutes to obtain clear and transparent oil, maintaining the obtained oil and curing for more than 18 hours.
NOVELTY - An environment-friendly clean fuel oil comprises 40-60 pts. wt. ethanol or methanol, 10-30 pts. wt. diesel and 4-20 pts. wt. functional additive. The functional additive contains anticoagulant, anti-rust agent, oiliness agent, antiwear agent, extreme pressure agent, antifoaming agent and antioxidant.    USE - Environment-friendly clean fuel oil (claimed).    ADVANTAGE - The environment-friendly clean fuel oil is economically and efficiently prepared with excellent corrosion resistance and oxidation property, and high cetane number.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of environment-friendly clean fuel oil.
NOVELTY - This utility new type relates to a portable self-one stacking structure, wherein it comprises machine frame, a driving device, a walking mechanism, a roller device, a roller motor and oil material device, said walking mechanism is set on the said of machine frame and connected with the running of said drive device is connecting, wherein the roller device is set on the two end of said machine frame and the roller device of respectively fixing the two side of a machine frame of said oil motor is set on a roller of the roller device and the drum oil motor and a drive device of the connecting said material device is set on the front end of said of machine frame. Using portable type self-stacking structure of the structure, can realize a good linear walking, a roller change is convenient, controllable of turning material sputtering angle, the action compatibility, it not only can be used for fermenting device of liquid fertilizer, but also using the municipal sludge to prepare fertilizer and garbage processing and so on, has wider application range of.
NOVELTY - This utility new type granulator one relates to a fertilizer production device, specifically to a one nitro long-acting high tower compound fertilizer production using high-efficient prilling tower, comprising a tower body, a tower body is set on the upper end of and set of a discharging port on the lower end, the lower end of said tower body is provided with an air inlet, upper end of said tower body is also provided with a air outlet, wherein said air outlet is inserted in exhaust pipe, the air outlet end of the exhaust tube extends to a heat recycling device in said heat recovery device comprises a shell, in the shell, because of using said structure, this utility new type a one of a nitro-long-acting high tower compound fertilizer production using high tower can be for discharge of hot air process heat recovery, and prevent waste of resource, and for discharge of air purifying process to prevent of dust in air entering into the atmosphere to cause air pollution.
NOVELTY - The system has a funnel-shaped cotton stalk section machine (1) that is connected with a crusher (2). The cotton stalk section machine, crusher, separating machine (3), granulating machine (4), drying machine (5) and total control panel (6) are connected in turn with each other through pipeline.    USE - Biomass fuel system.    ADVANTAGE - The working efficiency of the biomass fuel system can be effectively improved. The fuel system is convenient to feed and discharge. The dust collection and separation effect of the system can be improved, so as to ensure the health of the workers. The damage of the granulating machine can be avoided. The system can be easily manufactured at short time at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass fuel system.    Cotton stalk section machine (1)    Crusher (2)    Separating machine (3)    Granulating machine (4)    Drying machine (5)    Total control panel (6)
NOVELTY - Scrapped-automobile disassembled garbage is crushed, and mixed with nitrogen-containing material. The mixture is reacted, and garbage is carbonized to form carbide. The carbide and nitrogen-containing material are reacted, to obtain solid ammonium chloride. Waste gas is discharged, cooled, and carbide is crushed, to obtain carbide particles. Crushed carbide particles are mixed with water, heated, and filtered to obtain pure carbide. 100 parts mass pure carbide is added to 1-5 parts mass calcium carbonate powder, mixed, dried, and crushed, to obtain solid fuel.    USE - Preparation of solid fuel (claimed).    ADVANTAGE - The method provides solid fuel having low chlorine content, and high calorific value.    DETAILED DESCRIPTION - Scrapped-automobile disassembled garbage is crushed to particle size of less than 5 mm, and scrapped-automobile disassembled garbage and nitrogen-containing material are mixed. The mixture is fed into reactor, reacted at 300-360 degrees C for 30-60 minutes, and the resulting mixture is maintained at a pressure of 10-15 MPa. The garbage is carbonized to form carbide. The carbide and nitrogen-containing material are reacted in presence of hydrogen chloride gas, to obtain solid ammonium chloride. The valve of reactor is opened, waste gas is discharged, cooled, and carbide is crushed to 1-5 mm, to obtain carbide particles. 100 parts mass crushed carbide particles are mixed with 500-1000 parts mass water, heated to 50-80 degrees C, stirred for 20-30 minutes, allowed to stand for 10-20 minutes, and filtered to obtain pure carbide. 100 parts mass pure carbide is added to 1-5 parts mass calcium carbonate powder, mixed uniformly, dried, and crushed, to obtain solid fuel. The ratio of scrapped-automobile disassembled garbage and nitrogen-containing material is 1:0.4-0.8.
NOVELTY - Sludge treatment comprises carrying out Fenton reaction by adjusting pH value to 1.5-3.5 at 50-70 degrees C for 0.5-2.0 hours using 7-21 g/L hydrogen peroxide and 0.1-3 g/L iron ions, performing ultrasonic fragmentation with acoustic energy density of 0.l-3 w/m3 for 10-50 minutes and crushing sludge in anaerobic digestion tank to produce biogas.    USE - Sludge treatment used for treating food industry, textile industry, municipal and metallurgical industrial sludge (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic digestion device.
NOVELTY - Method for preparing cultivation substrate of mushroom, involves using raw materials comprising 50-80 pts. wt. cottonseed hulls, 10-40 pts. wt. river sand, and 10 pts. wt. peat, uniformly mixing the raw materials, adding 800 times carbendazim solution to mixture, and adjusting moisture content of substrate to 65-70%.    USE - The method is useful for preparing cultivation substrate of mushroom (claimed).    ADVANTAGE - The method prepares substrate with excellent water permeability, utilizes cost-effective raw material, cultures seedling of good quality, reduces environmental pollution, is environmentally-friendly, and realizes comprehensive utilization and recycling of cottonseed hulls.
NOVELTY - This new type utility claims nitrate benzene to translate a sustained-release blocker and dosing device, comprising a can, the can fixing connect of the hopper tank, tank connecting with the funnel of liquid feed port, a upper opening is provided with a charging switch, it has reasonable design, simple structure, easy manufacturing, convenient use, simple operation, and prevent waste, saves the cost and protects the environment, the production, strong commonality and improves the efficiency.
NOVELTY - This utility new type provides a one by glyphosate mother liquor constant temperature calcining sodium pyrophosphate production of device. The incinerator of three inlet respectively connect glyphosate mother liquid pipeline, a combustion-supporting air pipeline, gas pipeline, burning furnace upper part of connecting dust outlet in upper part of inlet, the top of connecting dust outlet of the waste heat boiler, the outlet on the bottom of furnace, the bottom outlet of cyclone dust collector and the bottom outlet of the waste heat boiler are connecting slag remover, the outlet connecting sodium packing machine, waste heat boiler of upper part outlet connecting bag-type dust remover, a bag-type dust collector of upper part outlet connecting water washing spray tower of lower part inlet; the lower part outlet of bag-type dust remover connecting sodium packing machine of water washing spray tower of upper part connecting the outlet of draught fan inlet, a draught fan connecting outlet of slag remover; This utility new type device can realize continuous, stable and effective treatment of high concentration organic phosphorus pesticide waste water, combustion of the flue gas reaches the national environmental protection standard.
NOVELTY - This utility new type relates to a one fertilizer production device, specifically to a production one or nitro long-acting urea fertilizer using high tower, comprising a tower and tower, a secondary tower in is equipped with hoisting machine, a tower upper part with molten and the molten shell is connected with the shell of granulating nozzle, wherein a tower, pelleting spray head is provided with an annular surrounding of upper dust-removing shell, bottom of said dust-removing shell is provided with multi-jet, using the structure, the utility model is new type a one of a production or nitro long-acting urea fertilizer rear using high tower granulating can be for internal tower for spraying and dust-removing process to prevent the dust pollution to atmosphere, and for the next and will not produce, improves the whole quality of fertilizer.
NOVELTY - This utility new type relates to a biomass particle machine of one groove type mould are respectively equipped with one mould and second mould in the groove of two side frame of the mould one and two of the outer mould trapezoid, particle forming hole is set at the bottom of the groove of trapezoid. The mould hole is processed into trapezoidal surface, forming holes in the groove bottom of trapezoid, when the raw material falling time of the mould upper ladder, comprising a ladder-shaped groove raw material, to make it only by forming hole, improves the utilization rate of forming hole, improves the grain yield.
NOVELTY - This utility new type relates to a biomass particle machine of one material distributing device is equipped with material distributing cap, a pressing wheel shaft and the main shaft power is connected on the upper pressing wheel shaft of the hopper. The raw material uniformity distribution inside the mould, using pressing stress balance, preparing material process is more stable and smooth.
NOVELTY - Preparation of biological carbon involves collected agriculture and forestry waste biomass raw material by naturally drying rear, cleaning silt and non-biomass impurities, pulverizing, sieving through 40 meshes sieve, dissolving rare-earth chloride in distilled water and obtaining rare earth chloride solution, mixing biomass raw material and rare earth chloride solution, stirring, sealing for 12 hours, vacuum-filtering, drying at 105 degrees C, processing in tubular furnace by supplying nitrogen as protective gas, pyrolyzing, and cooling to room temperature.    USE - Preparation of biological carbon (claimed).    ADVANTAGE - The method efficiently and economically provides biological carbon having nitrate absorption amount of 38.44 mg/g, ammonia absorption amount of 15.58 mg/g and phosphorus absorption amount of 19.74 mg/g.
NOVELTY - A catalyst comprises 10-70 wt.% active component comprising copper and 30-90 wt.% cocatalyst comprising oxides of nickel, manganese, iron, zinc and/or aluminum.    USE - Catalyst used for removing ethanol in coal bed gas, shale gas and oxygen gas.    ADVANTAGE - The catalyst has good stability, high mechanical strength, mild operating temperature and gas processing capacity. It reduces oxygen content below 0.1% from 0.1-5% original volume.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of catalyst comprising mixing aqueous solution of active component and cocatalyst, adding precipitating agent, filtering, washing precipitate, drying at 100-200 degrees c for 1-5 hours, calcining at 300-600 degrees C for 10 hours to obtain catalyst precursor, charging into reaction tube at 150-500 degrees C under reducing gas and air speed 1000-30000/hour, and restoring for 1-5 hours to obtain catalyst.
NOVELTY - This utility new type relates to a one machine of double-roller biomass granule forming machine of the whole structure, the two side of the groove in the frame, and one mould of die one and die two is provided with two drilled particle forming hole of second hydraulic motor is respectively connected with the power. Using hydraulic way of power source, two hydraulic motor drives the two moulds, the mould for pressing, the raw material of the forming hole in the mould prepared into granule, simplifies structure, reduces machine cost, host machine the whole size is reduced, which is good for production line.
NOVELTY - Solar energy and normal pressure direct current glow plasma photocatalytic decomposition of water into hydrogen comprises taking distilled water as raw material, projecting sunlight intensity to reactor by solar condenser, yielding mixed gas of hydrogen and oxygen, collecting and separating hydrogen main product and oxygen by-product.    USE - Method for solar energy and normal pressure direct current glow plasma photocatalytic decomposition of water into hydrogen (claimed).    ADVANTAGE - The method has no pollution and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solar energy and normal pressure direct current glow plasma photocatalytic decomposition of water into hydrogen device comprising light stopping diameter (11), main shaft (12), actual light spot (13), front window (20), inner wall (21), wire connecting terminal (22), plasma space (23), needle-type electrode (25), plate electrode (26), electrode rod (24), main tube (27), air tube (28), water inlet tube (29), ammeter (54), voltage meter (55), air inlet tube (60), collecting tank (61), water chamber (63), gas collecting system (68), three-way valve (69) and water replenishing tube (71).    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of solar energy and normal pressure direct current glow plasma photocatalytic decomposition of water into hydrogen device.    Actual light spot (13)    Inner wall (21)    Plasma space (23)    Electrode rod (24)    Needle type electrode (25)    Plate electrode (26)    Main tube (27)    Air tube (28)
NOVELTY - Organic liquid active materials produced by cultivation wastewater are treated by flocculating cultivation wastewater, concentrating, sterilizing concentrated solution, adding solid 6-15 kg nitrogen-fixing bacteria to 1000 kg wastewater concentrate, uniformly stirring, anaerobic fermenting at 40 degrees C for 10-45 days to obtain liquid activity ecological organic raw material, and sending to organic fertilizer factory to process into organic fertilizer.    USE - Cultivation wastewater treatment for producing organic liquid active materials used as organic fertilizer (claimed).    ADVANTAGE - Production process has simple and convenient operation, effectively solves environmental pollution problem of farm cultivation wastewater treatment, protects ecological environment, improves economic value of cultivation wastewater, and promotes continuous health development.
NOVELTY - Preparation of water hyacinth organic fertilizer comprises drying fresh water hyacinth, crushing, adding compost, composting at height of 0.5-1 m, covering, attaching mercury thermometer on top, sprinkling bacteria, fermenting, monitoring temperature at 9:00 a.m. to 3:00 p.m., maintaining water content at 50-70% for 3-4 days, stabilizing at 35-45 degrees C, stacking for 7 days, drying, crushing, sieving, screening and packaging.    USE - Method for preparing water hyacinth organic fertilizer (claimed).    ADVANTAGE - The method reduces manufacturing time and cost.
NOVELTY - Preparation of glucosamine potassium sulfate comprises adding water to tetrahydrofuran at 1:10-15 volume ratio and preparing into a mixed solution, raising the temperature to 30-60 degrees C, adding potassium bisulfate and glucosamine hydrochloride at 1.0:2.0-2.2 mol ratio into the mixed solution, stirring for 10-20 hours, cooling to - 5 to 5 degrees C, crystallizing for 3-6 hours, filtering to obtain crystals, and vacuum drying at 40-60 degrees C for 0.5-5.0 hours to obtain glucosamine potassium sulfate.    USE - Preparation of glucosamine potassium sulfate (claimed).    ADVANTAGE - The method has simple and controllable operation, high yield, and little pollution, is easy to implement and suitable for industrial production, provides product, which has better uniformity and meets the requirement of medical grade product, and achieves convenient recycling of solvent.
NOVELTY - A stirred biomass carbonizing furnace (1) comprises a furnace body, a combustion chamber, a pre-heating chamber, a carbonization chamber (4), a chimney, a pre-heating chamber, a burning room, and a carbonizing room provided with a stirrer.    USE - A stirred biomass carbonizing furnace.    ADVANTAGE - The furnace does not require additional fuel, thus saving energy.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the furnace.    Stirred biomass carbonizing furnace (1)    Carbonization chamber (4)    Insulation (10)    Separator (13)    Airway (14)
NOVELTY - A hybrid biomass briquette comprises oil plant fruit pressed cake or oil plant fruit pressed and pressed mixture of plant fruit oil pyrolysis solid product and cellulosic biomass.    USE - Hybrid biomass briquette.    ADVANTAGE - The method solves problems such as high combustion rate and processed plant fruit oil waste treatment, has low energy consumption, and is convenient, environment-friendly, and simple. The briquette is convenient to transport, use and store, has high intensity, and optimizes oil waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the production of hybrid biomass briquette comprising pretreating biomass chips at 20-30 degrees C and at 70-90% humidity, stacking for 2-3 weeks, drying at 40-60 degrees C until water content is 10-25%, sieving, drying raw material at 40-60 degrees C, until water content is 4-6%, crushing, and sieving to not greater than 2 mm particle size; and mixing plant fruit oil pyrolysis solid product and cellulosic biomass at mass ratio of not greater than 1:1, stirring, adding 1-3 wt.% quicklime, adjusting water content to 5-20%, and carrying out extrusion molding.
NOVELTY - A Penicillium oxalicum C2 (CGMCC N0 8335), is new. The 18S ribosomal DNA (rDNA) of P.oxalicum C2 comprises 595 base pair sequence (SEQ ID NO: 1) fully defined in the specification.    USE - The P.oxalicum C2 is useful in spore microbial inoculum for composting rotten silkworm dropping (claimed).    ADVANTAGE - The P.oxalicum C2 has high cellulase degradation ability of 132.26 U/ml, enables to prepare microbial inoculum simply and cost-effectively with high quality, increases carbon and nitrogen ratio (C/N) and seed germination, and improves fertilizer stack temperature for long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage method of P.oxalicum C2 which involves preparing seed liquid by inoculating P.oxalicum C2 strain into potato dextrose agar culture plate and shaking at 180-220 revolutions/minute and 28-30 V for 18-20 hours, adding the seed liquid into solid culture medium and then into solid sporulation culture medium at 28 degrees C and relative humidity of 60-80% for 4-6 days, and natural drying, crushing and sieving the cultured product, where the solid sporulation culture medium comprises 40 g bran, 20 g corn powder, 5 g sucrose, 1 g potassium nitrate, 0.5 g potassium dihydrogen phosphate, 0.1 g magnesium sulfate, and 300 ml water.
NOVELTY - This utility new type belongs to environmental protection device technology field, especially relates to a one divided rotary oil manufacturing fertilizer device, comprising a first fermentation tank, decomposition tank, the second fermentation tank, a secondary fermentation tank, first decomposing tank, the second time ferment tank two side are provided with an upright post, said upper upright post is provided with a rotating shaft, said rotating shaft and first fermentation tank, decomposition tank, the second time ferment tank fixing connect, a first fermentation tank, decomposition tank, the second time ferment tank are respectively provided with a feeding port A, port B, port C.
NOVELTY - Cultivation waste and agriculture and forestry waste sealed aerobic preparing biological organic fertilizer system comprises agriculture and forestry waste collecting cabin, cutting device, drying device, crushing device, agriculture and forestry waste temporary storage tank, cultivation waste collecting chamber, first cultivation waste temporary storage tank, the second cultivation waste temporary storage tank, centrifugal dewatering device, stirring and mixing device, a horizontal double-layer tube aerobic fermentation tank, a closed type aerobic fermentation tank, crushing, homogenizing storage bin, organic fertilizer packing device, an air supply device and an exhaust device. This utility new type of process is simple, the processing amount is large, the fermentation period is short, the material ferment level uniformity, treatment effect is good, high degree of automation, low cost, processing primary aerobic fermentation and one second primary aerobic fermentation treatment are totally enclosed operation, processing process has no peculiar smell, the agricultural waste by waste into valuable, the production has great market value of organic fertilizer and liquid fertilizer.
NOVELTY - Municipal sludge or kitchen closed aerobic biogas residue organic fertilizer producing system, comprising a waste collecting cabin, and cutting device, drying device, crushing device, storage tank, a sludge or kitchen biogas residue storage bin, stirring and mixing device, a horizontal double-layer tube aerobic fermentation tank, a closed type aerobic fermentation tank, crushing, homogenizing storage bin, organic fertilizer packing device, an air supply device and an exhaust device. This utility new type of simple structure, processing amount is large, the fermentation period is short, the material ferment level uniformity, treatment effect is good, high degree of automation, low cost, processing primary aerobic fermentation and one second primary aerobic fermentation treatment are totally enclosed operation, processing process has no peculiar smell, the biogas residue and municipal sludge kitchen waste into valuable, the production has great market value of organic fertilizer and liquid fertilizer, it also avoids the kitchen biogas residue and municipal sludge for environment and human body caused by the threat of, so as to realize harmless and recycling of kitchen biogas residue and municipal sludge.
NOVELTY - Municipal domestic sewage recycling system, comprising a sewage filtering classification tank and excrement sewage purifying treatment tank, a sewage feces filter classification tank left and right two side are respectively provided with fecal sewage inlet and overflow water, said excrement filtering sewage pool classification to bottom is vertically provided with floating isolating device and sundries filter screen left side from upper and right side inclined of excrement sewage filtering classifying excrement pool is provided with filter screen, excrement sewage filtering and classifying the bottom of middle position is provided with an excrement extracting pipeline, the utility model is new type by the waste water process for classifying the floater, firstly filtering out, then the excrement is sent to the marsh gas tank, at the same time, using the filter sewage and excrement, the rear process effectively processing sewage is sent resident user or field storage pool. Excrement with pressure conveying entering into marsh gas harmless treatment plant, waste gas to the fertilizer, and biogas residue for further processing, such as to manufacture organic compound fertilizer.
NOVELTY - This utility new type belongs to a sterilizing organic fertilizer of one preparation device, specifically a preparation device of a new one sterilizing organic fertilizer, comprising a mounting of straw processing device, the fermentation device, drying device, crushing device, stirring device, granulating device and packaging the finished product discharging port of a feeding port, drying device discharging port of the fermentation device through pipeline connect drying device of directly connected with the feeding port of crushing device, the discharge hole of crushing device through a pipeline connecting device of stirring a feeding port, a discharging port of the stirring device through a pipeline connecting device and a feeding port of the whole process realizes automatic production, simple structure, environment-friendly and energy-saving, stable product, production cost is low, the operation is convenient.
NOVELTY - This utility new type belongs to the garbage processing device technology field, especially relates to a vegetable one garbage treatment device, comprising a top opening of garbage treatment tank, the outer wall of said garbage treatment tank is provided with an insulating layer, the bottom of a garbage treatment tank is provided with , a cavity of a garbage treatment tank segmentation is the vegetable garbage rotten cavity of said and the upper part of the liquid collecting cavity under said , one end said vegetable garbage rotten cavity of is provided with an opening, said upper plate is provided with a multi-anti-corrosive through hole, the lower part of a garbage treatment tank opening end is provided with a filtrate collecting chamber of liquid collecting device. The vegetable waste compost processing the vegetable waste treatment device is formed with use of fertilizer, the processing is convenient, the processing cost is low, and it does not pollute the environment, which is good for popularization.
NOVELTY - This utility new type relates to a one, especially claims a biomass burner is one of biomass carbonizing furnace carbonizing hot source. It comprises a furnace body (1), a furnace door (2), a combustion chamber (3), carbonization chamber (4) and carbonization cylinder (5), a carbonization chamber (4) and the combustion room (3) is located in the furnace (1), a carbonizing tank (5) fixing in the carbonization chamber (4), it further comprises a furnace body (1) is set on the upper of the biomass burner (9), a biomass burner (9) of (9a) and the combustion room (3). This utility new type by biomass combustor with intelligent control function of the outlet temperature (9) control chamber (3), substituted the manual control fuel feeding amount to control combustion chamber (3) is manual mode of temperature, which can accurately adjust and control the combustion chamber (3) in the temperature, so as to timely adjust carbonization cylinder (5) of the temperature, which not only improves the biomass carbonizing speed and stable biomass carbonizing and improves the quality of the product.
NOVELTY - This utility new type relates to biomass energy device technology field, especially relates to biomass reaction furnace feeding device, comprising a hopper, the blanking base, a blanking base in is provided with a feeding channel, discharging base is provided with upper, lower blanking, blanking upper and lower blanking opening are staggered with each other, the sliding connecting with the raw material is composed of upper blanking port is sent to the feeding slide base lower blanking opening of the blanking base upper is provided with a drive device feeding channel in staggered opening this utility new type by intermittently feeding structure, upper and lower blanking blanking and alternately opened, can prevent flame in the furnace body from the bottom upwards skewered blanking, and prevent the inner wall of the furnace for producing gas from the bottom of the blanking port leakage, the safety coefficient is high.
NOVELTY - This utility new type relates to one can cure a slaughtering waste problem of slaughtering industry to seal the fermentation tank of the problem environment pollution. Fermentation tank seal of slaughter waste fermentation treatment, wherein the seal fermentation tank, using upper seal integral reinforced concrete structure or steel structure, the tank body is provided with waste channel interface, accelerate fermenting device, marsh gas collecting device interface, a discharging channel interface, a temperature safety valve interface, a door device. Fermentation tank process seal process produce three circulating chain, the one and by fermenting after produce combustible marsh gas, marsh gas conveying boiler to generate electricity, produce steam back seal of allixiary fermentation, fermentation tank into the marsh gas fermentation drying combustion heat; the second, dehydrating and drying leavening rear as production raw material production animal organic compound fertilizer, the three, out of water by simple chemical treatment, industrial into cleaning of using water. Resource is circularly used, the slaughter industry zero discharge can be sustainable development, and provides support of up technology.
NOVELTY - This utility new type relates to a one capable of accelerating oxygen/hydrogen from electrode plate of water electrolytic bath device, comprising one water groove main body, the main body is provided with water containing electrolyte of containing space and the inner electrode and the electrode plate, the water device is further provided with one power control part and the connecting of the ultrasonic vibration mechanism, the utility model is new type the water up the power control part and an ultrasonic vibration mechanism, a power control part can be loaded on the real-time monitoring of current and voltage upper electrode plate, and according to the feedback result to the electrode plate supplying the proper voltage and electric current, the electrolytic reaction to reach the best status, increasing electrode surface of the air bubble of the amount, at the same time, the ultrasonic vibration mechanism by ultrasonic wave in the form of vibration communicated to the upper electrode plate of the electrode plate vibration to make up the adhesive of the bubble is forced vibration and quickly from upper, of the accelerating oxygen hydrogen mixed gas, the mixed gas of more convenient.
NOVELTY - This utility new type claims a one gas generator belongs to the technical field of new-type hydrogen-oxygen mixed gas generator, comprising a shell, a control circuit board of the shell, control circuit board is set on the upper of the electrodes for electrolysis, of water circulation device and an air pump in the shell, said shell is provided with a power supply inlet and an air outlet, a side wall of the upper shell is provided with a water inlet, a electrolysis electrode comprising an electrolytic positive electrode and electrolytic negative electrode, a cell positive electrode is columnar, a cell negative electrode is a sheet circular arc shape, said electrolytic positive electrode is set on the electrolytic negative electrode, a cell negative electrode upper is provided with several through holes, the electrodes for electrolysis using a chromium alloy material, improves the service life, of electrode, electrolytic effect is better, at the same time, for The of water quality is not high, convenient maintenance, good radiation, electrolysis of hydrogen and oxygen from the pure drying, making the fuel combustion is more sufficient, which saves the fuel, reduces the discharge, energy-saving and environment-friendly.
NOVELTY - Method of using Ambrosia artemisiifolia extract for reducing hazards of rice involves (a) diluting the extract, spraying directly on growing rice leaves and stems, or spraying 1-50 g/m2 extract in combination with fertilizers and pesticides on rice leaves and stems, or (b) diluting the extract, soaking roots on diluted extract, and transplanting seedling, or mixing 1-50 g/kg extract and basil extract, soaking the roots in mixture and transplanting the seedling.    USE - The method is useful for reducing hazards of rice caused by Hirschmanniella using A.artemisiifolia extract (claimed).    ADVANTAGE - The method is environmentally-friendly and increases yield.
NOVELTY - Preservation method of loquat fruit comprises selecting loquat fruit, transferring in polyethylene plastic bag, oven drying at 48 degrees C for 3 hours, cooling, soaking in mixed vitamin E and sodium alginate solution for 5 minutes, adding plant extract, soaking for 8-12 minutes, drying, and storing at 8 degrees C for 3 days, at 4 degrees C for 3 days, and 1 degrees C.    USE - Preservation method of loquat fruit (claimed).    ADVANTAGE - The method is environment-friendly and suitable for large-scale production.
NOVELTY - This utility new type belongs to environmental protection device technology field, especially relates to a full-automatic bunker oil one fertilizer preparing device, a shell is provided with a first fermentation chamber, decomposing chamber, in the second chamber, a first fermentation chamber is provided with a water pipe, said water pipe is S type, and through a first fermentation chamber, a water transmission pipeline of the gap are respectively provided with a stirring shaft, the stirring shaft B, a stirring shaft A and a stirring shaft B passes through the first fermentation are respectively connecting with a motor A and motor B, a stirring shaft A and a stirring shaft B upper fixing with a stirring blade, the first fermenting chamber and said decompression cabin is provided with a first baffle plate, a first baffle comprises a first baffle plate A and baffle plate B, first a first baffle plate A and baffle plate B and first shell is hinged between said decompression cabin and the second fermentation chamber is provided with a second baffle plate, a second baffle plate comprises a second baffle plate A, A second baffle plate B, a second baffle plate A, A second baffle B are respectively and the shell.
NOVELTY - A hydrogenation catalyst comprises a composite rare-earth-transition metal/cobalt metal oxide with perovskite structure and 1-15 wt.% metal additive.    USE - Catalyst is used for carbon-monoxide hydrogenation.    ADVANTAGE - The catalyst increases the ratio of liquid hydrocarbon product oil fraction and lowers methane selectivity.    DETAILED DESCRIPTION - A hydrogenation catalyst comprises a composite metal oxide with perovskite structure and 1-15 wt.% metal additive. The composite metal oxide is of formula: AB'O3-y.    A=rare-earth metal;    B'=transition metal comprising cobalt, with molar ratio of cobalt and other transition metal being 3:1;and    y=number of moles of oxygen present in the composite oxide vacancies.    INDEPENDENT CLAIMS are included for the following:    (1) preparation of catalyst, which involves preparing composite metal oxide and loading metal additive; and    (2) reduction method of catalyst at 400-1000 degrees C in 5 hours in a reducing atmosphere of hydrogen or 1-3C hydrocarbon.
NOVELTY - Method for preparing organic fertilizer, by (a) mixing earthworm manure, straw and effective microorganism (EM) to obtain EM compost, (b) mixing EM compost, EM stock solution, molasses and water and spraying the solution uniformly on EM compost obtained in step (a), mixing uniformly, sealing the mixture and performing anaerobic fermentation for 5-7 days to obtain fermented product, and (c) mixing the fermented product with polyacrylamide to obtain the product.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The fertilizer is prepared by simple method and non-toxic, and has high water holding capacity, and requires short cycle decomposition, provides variety of nutrients for plant growth, control moisture loss in soil, increases water content in crop and alleviate drought crops.    DETAILED DESCRIPTION - Method for preparing organic fertilizer, involves (a) mixing earthworm manure, straw and effective microorganism (EM) in a weight ratio of 100:10:0.3 to obtain EM compost, (b) mixing EM compost, EM stock solution, molasses and water and spraying the solution uniformly on EM compost obtained in step (a), mixing uniformly, sealing the mixture and performing anaerobic fermentation for 5-7 days to obtain fermented product, where the weight ratio of EM compost, EM stock solution, molasses and water are 90-92:4-6:0.5:3.5, and (c) mixing the fermented product with polyacrylamide in ratio 85-95:5-15 to obtain the product.
NOVELTY - Method for preparing vegetable seedling matrix, involves (a) obtaining e.g. wheat straw and sheep manure, drying and crushing the components with straw decomposition agent and acidic compound fertilizer, mixing the components, and stirring and fermenting the mixture to obtain organic mixed particle, (b) mixing nitrogenous fertilizer, phosphate fertilizer, potash fertilizer and filling agent, and stirring the mixture to obtain seedling promoting agent, and (c) mixing the organic mixed particle and seedling promoting agent with black soil, and stirring the mixture.    USE - The method is useful for vegetable seedling matrix (claimed) which is used in cultivation of seedlings.    ADVANTAGE - The method saves labor and work, is cost-effective, and prepares matrix which is convenient to use.    DETAILED DESCRIPTION - Method for preparing vegetable seedling matrix, involves (a) obtaining wheat straw, rapeseed, straw, branches of shrub and trees, cotton straw and sheep manure as raw material for seedling matrix, drying and crushing the above-mentioned components with straw decomposition agent and acidic compound fertilizer, mixing the crushed components, uniformly stirring and discharging the mixture, and fermenting the mixture to obtain organic mixed particle, (b) mixing the nitrogenous fertilizer, phosphate fertilizer, potash fertilizer and filling agent, and uniformly stirring and discharging the mixture to obtain seedling promoting agent, and (c) mixing the obtained organic mixed particle and seedling promoting agent with black soil, and uniformly stirring and discharging the mixture to obtain product.
NOVELTY - Under this utility new type of straw gasification furnace, wherein it comprises a main machine and secondary machine of integrated, and a main machine is provided with a feeding port, the middle part is provided with an observation opening and a fire grate, the lower part is provided with an ash outlet, a grate located at the viewing port, the auxiliary top is provided with an air outlet, in upper part is provided with an observation opening and filter screen, the lower part is an ash outlet, the lower filter screen is located viewing port, the lower part and the host machine, the host machine produce gas from lower part of blowing. This utility new type of beneficial effects, simple structure, convenient use, integrated structure of host machine and secondary machine, saves space, it can primarily purified gas, the dust, prevent the conveying process in an ash is easy to block the pipe and of setting special dust removing device and reduce the cost. And the gas passing through the primary cooling of machines to prevent burning conveying pipeline.
NOVELTY - This utility new type belongs to one a lower suction biomass fixing bed gasification furnace heating system, comprising one time storage hopper (1), a second secondary chamber (3) and gas storage device (9), wherein the second secondary chamber (3) under the gasifying furnace body (4) and the waste heat recovery device (6) is connected, a waste heat recycling device (6) upper part of the exhaust tube with the gas storage cylinder (27) is connected with air cylinder (27) of the air outlet tube and the spiral purifier capable of dust removing washing device (7) is connected with spiral purifier capable of dust removing washing device (7) upper end two secondary oxygen supply (22) and the frequency conversion Roots blower (8) is connected with the waste heat recycling device (6) of upper end using pipeline and the air cylinder (27) is connected with air cylinder (27) is connected with the spiral purifier capable of dust removing using washing device (7), waste heat recovery device (6) of the lower end pipe and valve and the using water vapour to hydrogen reduction device (13). The utility model is high temperature in the furnace, the hot efficiency is high, low, which is beneficial to environment protection, low cost heat device high, fuel source.
NOVELTY - This utility new type of fire grate upper gasification furnace of straw, wherein a detachable grate is equipped with flat opening of one of the horizontal middle part of the furnace body, a furnace body middle part, upper flat opening is welded with a cylinder, the cylinder is welded with a flange plate of rectangle; grate support pole up correspondingly welded with a flange plate of rectangle, fire grate is flat frame, a grate furnace body are inserted into the cylinder and with two joint and flange through a bolt and nut is installed; the fire grate composed of several pieces of metal tube are crossed with each other are welded together with the inner metal tube with a circulating cooling water, wherein there are two metal tube as the supporting pole of as water inlet tube and water outlet tube. This utility new type of beneficial effects, simple structure, convenient use, convenient to disassemble, it is not easy to burn and the service life is long.
NOVELTY - This utility new type claims a one wood waste fuel, which is composed of bamboo-wood waste particles 1 is formed by extrusion of a cylinder, two end of said cylinder is a natural bending section, wherein a circumferential surface of a cylinder is pressed into a plurality of axial ribs 2 and axial grooves 3. The axial ridge 2 and an axial groove 3 is formed are arranged at intervals; the advantages, this utility new type bamboo-wood waste fuel of upper peripheral surface is pressed with several axial ridge 2 and the axial groove 3, in the fuel reactor, the axial convex ridge of 2 in contact with each other, and the axial groove 3 the air passage is smooth, which is good for entering into fuel reactor process oxygen combustion-supporting, the forming fuel burn fully, hot energy of full of fuel.
NOVELTY - Biofertilizer composite comprises 30-70 pts. wt. Aspergillus niger, 5-10 pts. wt. large spore solubilizing Bacillus, 20-30 pts. wt. Lactobacillus plantarum, and 10-40 pts. wt. Bacillus subtilis.    USE - As biofertilizer composite.    ADVANTAGE - The biofertilizer composite improves grain yield to 8-30%, vegetable yield to 10-40%, vegetable quality and flavor of food, and is required in a quantity of 50-100 g for per acre of land.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the biofertilizer composite, which involves culturing A.niger, large spore solubilizing Bacillus, L.plantarum, and B.subtilis, fermenting the culture, and mixing the complex microbial culture.
NOVELTY - Bio-organic fertilizer comprises fermented bacteria, urea, and phosphate mixture comprising phosphate acid, slaughtered meat and poultry livestock manure in a weight ratio 1:40:50.    USE - The bio-organic fertilizer is useful for urban greening, and cultivation of green vegetables, and ornamental flower.    ADVANTAGE - The fertilizer consumes minimal energy, changes waste products into valuable products, and has wide availability of raw materials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the bio-organic fertilizer, which involves mixing the phosphate acid, slaughtered meat and poultry livestock, adding 0.2 wt.% fermentation bacteria to the mixture, adding water to the mixture, adjusting humidity of the mixture to 45-55%, stacking the layers, stacking the other layer using yeast and urea, covering the stacked mixture using black plastic film, naturally fermenting the mixture, turning the fermented mixture for every 15-30 days, composting the mixture, crushing the compost, sieving the crushed mixture, and packing the sieved mixture.
NOVELTY - Method for performing soil cultivation of cucumber, involves (a) pulverizing vegetable mixture, adjusting carbon/nitrogen (C/N) ratio, maintaining moisture content of the mixture, (b) inoculating 0.3 %mass inoculants composite to the vegetable mixture, mixing chicken stubble with the vegetable mixture, naturally aging mixture, turning the mixture, reducing the temperature of the mixture and crushing the vegetable mixture, (c) crushing the grassy straw, and (d) mixing e.g. dried cow dung and chicken, meat, cultivating cucumber in soil and adjusting pH of the soil.    USE - The method is useful for performing soil cultivation of cucumber (claimed).    ADVANTAGE - The method is simple, convenient to perform, and environmentally-friendly, saves grass peat resource, and reduces insect pests.    DETAILED DESCRIPTION - Method for performing soil cultivation of cucumber, involves (a) pulverizing vegetable mixture, adjusting carbon/nitrogen (C/N) ratio to 24-26 and maintaining moisture content of the mixture to 59-61%, where the vegetable mixture comprises sweet potatoes stubble, cucumber stubble, and cabbage stubble in a volume ratio of 4:1:2, (b) inoculating 0.3 %mass 2x 109 colony-forming unit (CFU)/g inoculants composite to the vegetable mixture, mixing chicken stubble with the vegetable mixture, naturally aging the mixture, turning the mixture for every 3 days, reducing the temperature of the mixture to 26 degrees C or less and crushing the vegetable mixture, (c) crushing the grassy straw to mesh size of 80-120 meshes, and (d) mixing dried cow dung, chicken, meat, potassium chloride, trace elements, and the mixture obtained in step (b) and step (c), cultivating cucumber in the soil and adjusting pH of the soil to 6.5-7.
NOVELTY - Method for fermenting grape liquid fertilizer, (a) digging a pit of 50-70 cm deep, (b) adding farmyard manure to the pit (covering thickness of 20-40 cm), and adding 100 kg superphosphate to the pit, (c) sprinkling composting agent in the pit (20-40 cm thickness), (d) carrying out mulching process and covering the pit using film, (e) uncovering the film after every half a month, turning the compost once, and recovering the pit using film (product can be used for 2-3 months).    USE - The method is useful for fermenting grape liquid fertilizer (claimed).    ADVANTAGE - The liquid fertilizer fermented by the method is effective for a long period of time, and is highly nutritious.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fermented liquid fertilizer for grape, which is obtained by the above-mentioned method.
NOVELTY - Preparing magnetic solid base catalyst comprises mixing nickel sulfate hexahydrate, and ferric chloride hexahydrate and then stirring and dissolving in 15 ml of water, dissolving a certain amount of sodium hydroxide in 15 ml of water, adding solution A and solution B and then mixing with 15 ml of water in a beaker and stirring to obtain a mixed solution, adding sodium hydroxide to the mixed solution and then stirring and reacting, placing the reacted mixture in 150 ml of water in autoclave and then reacting, cooling, separating out, washing with water for 35 times and drying.    USE - The method is useful for preparing magnetic solid base catalyst, which is useful for synthesizing biodiesel (claimed).    ADVANTAGE - The method economically prepares the magnetic solid base catalyst with high activity and good stability in an eco-friendly manner.    DETAILED DESCRIPTION - Preparing magnetic solid base catalyst comprises mixing nickel sulfate hexahydrate, and ferric chloride hexahydrate according to a molar ratio of 1:2 and then stirring for 10-30 minutes and dissolving in 15 ml of ultrapure water to obtain solution A, dissolving a certain amount of sodium hydroxide in 15 ml of ultrapure water to obtain solution B, adding solution A and solution B and then mixing with 15 ml of water in a beaker and stirring to obtain a mixed solution, adding sodium hydroxide to the mixed solution and then stirring for 20-60 minutes and reacting, placing the reacted mixture in 150 ml of water in autoclave and then reacting at 150-240 degrees C for 6-12 hours, cooling, separating out in a magnetic field, washing with ultrapure water for 35 times and drying at 180-240 degrees C for 2-6 hours.
NOVELTY - This utility new type is a refining device, device of one high quality biological diesel oil comprises a neutralizing kettle is provided with a raw material feed port up the neutralization kettle, neutralizing kettle through a pipeline connecting a first centrifuge, a first centrifugal machine through the pipeline connecting a water washing kettle, washing is further provided with a soft water inlet kettle up in water, adding soft water and stirring the water washing kettle, washing kettle connect with a second centrifuge, the centrifuge by pipeline connecting with a pre-heater, a pre-heater through the pipeline connecting with evaporator, the evaporator of high water ratio of low acid value of biologic diesel oil low metal the evaporation of water, the pump is qualified of high quality biological diesel oil. This utility new type has novel structure, production efficiency is high, convenient for mass production, and the production of bio-diesel through the detect are for which meets the national standard of bio-diesel.
NOVELTY - This utility new type claims a sludge fermentation pool belt one bulk device, comprising a guide rail and can move along the guide rail of trolley, a trolley fixing upper is set with a bracket, upper fixing bracket with a hopper, and the upper and lower end of hopper is respectively provided with an air inlet and a discharging port, a discharging port is rotatably installed with a rotating shaft, the rotating shaft of the outer wall are respectively provided with four T-shaped blade, the upper of trolley below the discharging port is provided with a material port. fermenting tank is set on the two side of the opening This utility new type has simple structure, uniformity of adding dehydrated sludge and aerobic microbial thalli to the fermenting tank in to make the dehydrated sludge of aerobic microbial cells in a fermenting tank and can be flat paving, improves the fermentation efficiency and the dewatered sludge, of conversion efficiency.
NOVELTY - This new type utility claims first-stage reaction device of fluorin silicic acid and liquid ammonia preparation device of ammonium fluoride or ammonium hydrogen fluoride, comprising a raw material storage device, second level reaction device, the reaction product separating and condensing device, a pipeline waste liquid treatment device and a recycling device connected with and valve of the raw material storage device is respectively connected with the first-stage reaction device, second level reaction device, a waste liquid treatment recycling device is connected with the first-stage reaction device and the second level reaction device is connected with the second level reaction device and reaction product separating and concentrating device is connected with the, and the reaction product separating and condensing device and the waste liquid treatment recycling device are connected with each other. This utility new type product by phosphate fertilizer production of fluorin silicic acid industrial large scale production high quality ammonium fluoride or ammonium hydrogen fluoride, absorption of by-product of phosphate fertilizer in production process, provides a specific implementation solution of environment-friendly and economical dual benefits.
NOVELTY - One controlling a continuous decomposing sulfureted hydrogen to prepare hydrogen of device, belonging to the hydrogen and gas purification technology field. One is specifically a controllable dielectric barrier discharge type plasma generating device, hydrogen sulphide gas or hydrogen sulfide in the device of gas can be continuously and stably in ionization decomposition for preparing hydrogen. Wherein, the reactor is a coaxial sleeve type structure, the reactor tube using insulating medium, the center electrode is a metal, a grounding electrode is controllable temperature of circulating liquid, the temperature control, the produce decomposition of sulphur is separated, the hydrogen sulphide for preparing decomposition of hydrogen process continuously and stably. This utility new type has the advantages of, in this device is suitable for natural gas, petroleum and coal chemical industry containing hydrogen sulphide gas dissociation of hydrogen and elemental sulphur, the device for gas source and is composed of or has no special requirement, so that hydrogen and sulphur with universal applicability for hydrogen sulfide.
NOVELTY - This utility new type claims a one LED gallium nitride production furnace waste gas recycling device, comprising a buffer tank, a filter, a vaporizer, a condenser, a rectifying tower and high-level tank, wherein a of the filter is two, there are three said condenser, said vaporizer there are two, the buffer tank left side is provided with a waste gas pipeline, the buffer tank is outlet of the first-stage filter one end, the first-stage filter of the other end and the second level filter, the second level filter outlet of the condenser I inlet, a condenser upper end I is connected with an emptying pipe, the lower end outlet of the vaporizer I left inlet connected with the evaporator I the right side middle part II is connected with the condenser, condenser upper end II is connected with an emptying pipe, the lower end outlet of the vaporizer left inlet II is connected with the bottom of the evaporator II connected with a drain pipeline, and the top is set with rectifying tower, a rectifying tower top outlet of the condenser III. The device eliminates the environment pollution and realizes recycle of waste gas, and saves the cost.
NOVELTY - This new type utility claims small poultry corpse, the stirring unit comprises a fermenting, crushing unit and heating unit, body processing chamber a crushing unit, the fermentation stirring unit are arranged with a feeding port of the shell of, said crushing unit comprises two parallel of tool group, the two groups of opposite rotating process cutter crushing; the lower part of fermenting and blending unit in said crushing unit and comprising a stirring shaft and the stirring blade, said stirring blade groups are respectively four fixing on the stirring shaft, stirring blades of each of the adjacent stirring blade set is vertical, said heating unit comprises a hot air heater and a guide oil heater, a hot air heater and a guide oil heater are sent to the shell by pipeline, forming sterilizing allixiary fermentation. This utility new type small poultry corpse can be effectively converted into stable quality of organic fertilizer, processing abiligy, and the cost is low.
NOVELTY - This utility new type relates to a one by domestic garbage fast fertilizer system, comprising a feeding robot, breaking drum screening machine, a permanent magnetic separator, a winnowing machine, a steam ejection type organic garbage disposer, drum-type drier, a cylinder scalping sieve, and organic fertilizer production device, a feeding conveyor connecting the robot through breaking drum screening machine inlet, a bag-breaking drum screening machine outlet connecting permanent magnetic separator inlet, outlet connecting permanent magnetic separator for winnowing machine inlet, a winnowing machine connecting steam-type organic garbage disposer, steam-type organic garbage processor connecting the roller shape drier inlet, a drum-type drier through conveyer connecting cylinder scalping sieve inlet, a cylinder scalping sieve conveyor connecting organic fertilizer production device. This utility new fertilizer time short, garbage processing amount is large, high fertilizer effect, convenient production, strong operability, which effectively solves the garbage pollute the environment, damage of the problem, realizes the recycling use of green and environment-friendly.
NOVELTY - This utility new type relates to one coal or biomass of a gasification furnace, especially relates to remove gasifying furnace of tar, comprising a coke oven and gasifying furnace, wherein said coke oven is set on the gasifying furnace, coking furnace is provided in one inner container between the furnace wall and the liner form one interlayer. Working principle is as follows: the coke furnace coal or biomass fuel into coke oven and coke, the coke oven gas and air mixed rear burn, to thoroughly remove tar, coke-oven gas and air of the gasifying furnace and the coke to the combustible gas. This utility new type flammable in air of tar content is very low, it does not need purifying can be directly entering into the gas turbine. Small type device can be used in family.
NOVELTY - This utility new type relates to one coal or biomass of a gasification furnace, especially claims a gasification furnace of completely removing tar, comprising a coke oven and upper suction gasification furnace, wherein, the coke oven is set on the upper suction type gasification furnace, upper part of coke oven further is provided with a coke-oven gas guide tube and connected with the of air pump. Working principle is as follows: the coking furnace the material (coal or biomass fuel) into a coke oven and coke, the coke-oven gas and gasification agent (air, oxygen-enriched or pure oxygen) burn, to coke-oven gas and air of rear thoroughly remove tar, the upper suction gasification furnace and the coke to the combustible gas. This utility new type flammable in air of tar content is very low, it does not need purifying can be directly entering into the gas turbine. In addition, filtering most dust combustible gas through coke layer. Small type device can be used in family.
NOVELTY - One liquid depositing solid can be a chemical combustion device, comprising a liquid depositing solid matter feeding port (1), a liquid depositing solid matter storage chamber (2), a separating agent additive material feeding system (3), a deodorizing stirring tank (4), a biomass powder and additive feeding system (5) and a finished product material mixing tank (6), a separating additive feeding mixing system is provided with first screw feeding device, upper shell of first spiral feeding pole is provided with multiple separating agent feeding port, and stirring tank is impeller type stirring tank, and stirring tank is provided with a stabilizing agent feeding port of biomass powder and additive delivery system is a second screw device is provided with a plurality of biomass powder and additive feeding port on the shell of the upper spiral feeding pole the product material receiving tank is provided with a biomass powder and additive feeding system of material feeding port, material mixing tank is impeller mixing tank. This utility new type processing sludge speed is fast, and the product quality is stable.
NOVELTY - A salt-containing sewage water treatment is performed by reducing water amount in biochemical pool, maintaining gas to water ratio in metaplasia pool, enhancing biochemical pool outside reflux ratio, and suspending sludge discharge to improve sludge age, gradually increasing bacteria in water during domestication, improving water intake, decreasing biochemical pool outside reflux ratio, controlling sludge age while starting sludge discharge, decreasing biochemical pool outside reflux ratio during late domestication, and gradually reducing gas-water ratio, and sludge age.    USE - A salt-containing sewage water treatment (claimed).    DETAILED DESCRIPTION - A salt-containing sewage water treatment is performed by reducing water amount in biochemical pool to less than or equal to 40% in early stage of domestication, maintaining gas to water ratio in metaplasia pool at 4:1, enhancing biochemical pool outside reflux ratio, and suspending sludge discharge to improve sludge age, gradually increasing bacteria in water during domestication, improving water intake by 10-15%, decreasing biochemical pool outside reflux ratio by 50-55%, controlling sludge age to 13-20 days while starting sludge discharge, decreasing biochemical pool outside reflux ratio by 50% during late domestication, and gradually reducing gas-water ratio by 4:1 or less, and sludge age to 8-15 days.
NOVELTY - A mobile integrated device has container (10) as inner operating space comprising sand filter (30) connected to slurry storage tank (20) which is used for storing biogas and core filter (40) used as secondary filter medium, and disk-tube reverse osmosis membrane condensing device (50) connected with operating space and core filter which is used for concentrating filtered and treated biogas slurry.    USE - A mobile integrated device for treating concentrated biogas slurry (claimed).    ADVANTAGE - The device has simple structure, and excellent utilization rate, is easy to operate, and enables stable operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of mobile integrated device for treating concentrated biogas slurry.    Container (10)    Slurry storage tank (20)    Sand filter (30)    Core filter (40)    Disk-tube reverse osmosis membrane condensing device (50)
NOVELTY - Soil comprises 8-12 pts. wt. vegetable stump, 6-8 pts. wt. slag, 3-5 pts. wt. nitrogenous lime, 10-15 pts. wt. duck manure, 3-5 pts. wt. blood meal, 3-5 pts. wt. cypress, 0.1-0.3 pt. wt. compost fermenting bacteria and 2-4 pts. wt. cinnamon.    USE - Soil used for cultivating lettuce.    ADVANTAGE - The soil has environment-friendly effect and reduced cost by 30-40%.
NOVELTY - Method for preparing lettuce cultivation soil, involves pulverizing vegetable stubble having C/N ratio of 22-25 and moisture of 55-57%, preparing lettuce seedling substrate, where the vegetable stubble comprises canola stubble, cabbage stubble and eggplant stubble in a ratio of 2:4:3, adding greater than or equal to 2x 109 colony forming unit (cfu)/g viable cells to the vegetable stubble, mixing the materials with duck manure, aging the mixture, mixing aging materials once in every three days, reducing the temperature to 32 degrees C, and drying and crushing the vegetable stubble.    USE - The method is useful for preparing lettuce cultivation soil (claimed).    ADVANTAGE - The method is simple, cost-effective and easy to perform, reduces environmental pollution, and enhances lettuce breeding effect.
NOVELTY - This utility new type relates to one suitable for a dangerous solid waste of biomass fluidized bed gasification and combustion boiler, comprising a feeder, a main furnace body, a fuel gas high temperature combustion chamber, a feeder with the main body connecting the top part of the main body and the first-stage gas-solid separator connect, the bottom of first-stage gas-solid separator through the material returning valve is connected with the lower part of the main body connecting the top part with the second level gas-solid separator of first-stage gas-solid separator connect, the bottom of second level gas-solid separator connecting with an ash level second gas-solid separator of the top part and the high temperature burning room of gas inlet connecting gas high temperature combustion room of the outlet through the coal economizer, an air pre-heater and the tail flue connecting. This utility new type using circulating fluidized bed gasification and high temperature fuel gas re-burning combined structure and is suitable for biomass and dangerous solid waste of the energy, treatment of fly ash removing avoids coking and corrosion of combustion process, combustion is more clean, combustion temperature can reach more than 1300 degrees C, the dangerous solid waste is completely decomposed, high energy utilization efficiency reaches more than 80%.
NOVELTY - Sludge aerobic composting method, involves using green waste as conditioning agent for sludge aerobic compost process.    USE - The aerobic composting method is useful for sludge (claimed).    ADVANTAGE - The method is harmless, and can dissolve large amount of green waste.
NOVELTY - A methanol fuel contains uniformly mixed 5-30 vol.% methanol, 3-10 vol.% cosolvent, 5-15 vol.% cetane number improver, and balance diesel oil or diesel oil component oil in which cosolvent is isooctyl amine.    USE - A methanol fuel for compression ignition engine such as diesel engine (claimed).    ADVANTAGE - Methanol fuel is environment-friendly and low in cost, has convenient preparation, simple composition, good flexibility, high efficiency, and strong operability, eliminates corrosion and swelling effect, reduces additive components, and avoids complex components which can cause tail gas pollution.
NOVELTY - A mixed hydrogen gas fuel based on coke oven gas and natural gas (or methane (CH4)) contains 10-63 vol.% hydrogen, 35-88 vol.% methane, 1-2 vol.% carbon monoxide, and balance tail gas obtained by purifying coke oven gas and mixing with natural gas or CH4.    USE - A mixed hydrogen gas fuel based on coke oven gas and natural gas (or methane) for internal combustion engine (claimed) clean substitute fuel.    ADVANTAGE - Mixed hydrogen gas fuel is environment-friendly, uses widely available and low in cost coke oven gas resource, increases energy utilization efficiency, has improved flame propagation speed which improves combustion reaction speed, reduces fuel consumption rate, and reduces internal combustion engine emissions.
NOVELTY - A hydrogen mixed gas fuel based on coke oven gas contains 50-63 vol.% hydrogen, 20-38 vol.% methane, 4-9 vol.% carbon monoxide, and balance coke oven tail gas obtained by coke oven gas purification.    USE - A hydrogen mixed gas fuel based on coke oven gas for internal combustion engine (claimed) clean substitute fuel.    ADVANTAGE - Hydrogen mixed gas fuel is environment-friendly, uses widely available and low in cost coke oven gas resource, increases energy utilization efficiency, has improved flame propagation speed which improves combustion reaction speed, reduces fuel consumption rate, and reduces internal combustion engine emissions.
NOVELTY - An ecological oil preparation system comprises a reactor for cracking biomass fuel gas and carbon, a biomass gas condenser, a heater, and a tube heat exchanger.    USE - An ecological oil preparation system.    ADVANTAGE - The system has reduced energy consumption.
NOVELTY - The method involves pumping a grease-like compound into a tube-type reactor by a pump in a nitrogen atmosphere for carry out a catalytic decarboxylation reaction to obtain hydrocarbon fuel, where reaction temperature is 300-360 degrees C, pressure is normal pressure, reaction time is 1.5-3 hours, and feeding speed in 0.03-0.30 g/(cm2) min.    USE - Method for preparing oil-producing algae hydrocarbon fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for preparing oil-producing algae hydrocarbon fuel. (Drawing includes non-English language text)'
NOVELTY - The method involves adding water, hydrocarbon liquid fuel and hydrophilic emulsifier to obtain emulsified waste hydrocarbon liquid fuel, and carrying out cracking process with agriculture and forestry waste. Air or oxygen is mixed with the obtained product at 500-1400 degrees C to carry out a non-catalytic partial oxidation gasification process for obtaining a gas product. The product is dried for removing sulfide to obtain oil-based synthetic gas, where the cracking mass ratio of the bio-oil is 1: 0.25-1: 4.    USE - Bio-oil based synthesis gas preparation method.    ADVANTAGE - The method enables improving gas yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a bio-oil based synthesis gas preparation method. '(Drawing includes non-English language text)'
NOVELTY - The device has a furnace body integrally arranged with a refractory material layer and provided with a feeding port, slag outlet and a gasification agent inlet. An upper part of the furnace body is provided with a furnace gas outlet. A lower part of the furnace body is provided with a plasma torch.    USE - Plasma gasification device for a rural environment construction.    ADVANTAGE - The device utilizes the solid waste biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a plasma gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a plasma gasification method. '(Drawing includes non-English language text)'
NOVELTY - The furnace has a main body comprising a heating element and a thermoelectric couple. A gasification section equipped with a drive motor that is driven by a chain grate. A lower part of the grate is provided with a discharging port.    USE - Step chain type biomass gasification furnace.    ADVANTAGE - The furnace is flexible.    DESCRIPTION OF DRAWING(S) - The drawing shows a step chain type biomass gasification furnace.
NOVELTY - Production of high-efficiency biomass particles involves carrying out long fiber primary crushing process by primary crushing long fiber using crusher, drying the resultant product, thermal cracking the resultant product at 400-500 degrees C, separating coarse and fine particles by vibration sieve process, secondary crushing the coarse particles and fine particles, stirring and mixing the resultant product, then granulating the mixed material by rear artificial material machine pelletizing process, and cooling the resultant product.    USE - Production of high-efficiency biomass particles (claimed).    ADVANTAGE - The method provides high-efficiency biomass particles with improved calorific value and reduced wood tar content.
NOVELTY - The device comprises a thread cover tightly covered on a bottle opening of a reactor. An injector-type water bottle is provided with a water inlet tube and a water outlet tube. The water inlet tube is connected with a peristaltic pump and passed through the screw thread cover and a micro-filter membrane module to reach the reactor. The water outlet tube is connected with the peristaltic pump. The water inlet tube is passed through the screw thread cover. The micro-filter membrane module is arranged in the reactor and located on a magnetic stirrer.    USE - The anammox bacteria enrichment device is useful in sewage treatment.    DETAILED DESCRIPTION - The device comprises a thread cover tightly covered on a bottle opening of a reactor. An injector-type water bottle is provided with a water inlet tube and a water outlet tube. The water inlet tube is connected with a peristaltic pump and passed through the screw thread cover and a micro-filter membrane module to reach the reactor. The water outlet tube is connected with the peristaltic pump. The water inlet tube is passed through the screw thread cover. The micro-filter membrane module is arranged in the reactor and located on a magnetic stirrer. An air inlet tube and an air inlet tube are connected with a high pure nitrogen bottle. The air outlet tube is connected with the air inlet tube through the screw thread cover and immersed in a culture medium in the reactor. The air outlet tube is connected with a wet gas flow meter. The reactor is covered with an aluminum foil paper. An INDEPENDENT CLAIM is included for anammox bacteria enrichment method.
NOVELTY - Biological agent comprises 2-10 hundred million/g Trichoderma, 2-10 hundred million/g Aspergillus terreus, 2-10 hundred million/g Phanerochaete chrysosporium, 2-10 hundred million/g Bacillus and 2-10 hundred million/g white Torulopsis.    USE - The biological agent is useful for decomposition of straw (claimed), chosen from wheat, corn, and rice.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the biological agent, which involves subjecting the Trichoderma, A.terreus, P.chrysosporium, B.amyloliquefaciens and Torulopsis to solid fermentation, respectively performing liquid fermentation and solid fermentation, where the liquid fermentation involves cultivating strain in a slant culture flask fermentor, and solid fermentation involves feeding fermented liquid into clean fermentation chamber, incubating the culture, mixing wheat bran as carrier, preparing fermented products, and crushing, sieving, packaging and adding finished product into warehouse.
NOVELTY - The stabilizer comprise cathode and anode cells, a connecting pipe communicating between the cells, an anode tube inserted in to the anode cell, and a cathode tube inserted into the cathode cell, where a height difference between a horizontal plane of anode tube outlet and a horizontal plane of the cathode tube outlet is lower than the anode tube. A hydrogen recovery pipe is connected to a top of the cathode tube. A chlorine recovery pipe is connected to the top of the anode tube.    USE - Electrolytic cell voltage stabilizer.    ADVANTAGE - The stabilizer provides a stable and accurate differential pressure to an ion exchange film of the electrolytic cell.    DETAILED DESCRIPTION - The stabilizer comprise cathode and anode cells, a connecting pipe communicating between the cells, an anode tube inserted in to the anode cell, and a cathode tube inserted into the cathode cell, where a height difference between a horizontal plane of anode tube outlet and a horizontal plane of the cathode tube outlet is lower than the anode tube. A hydrogen recovery pipe is connected to a top of the cathode tube. A chlorine recovery pipe is connected to the top of the anode tube. The height difference is 450 mm. A nitrogen source is provided in the upper parts of the cathode and the anode tubes respectively. A water inlet pipe is set on the cathode tube.
NOVELTY - This utility new type relates to one solid fermentation machine of a heat supply system, a heating system of a combustion furnace, a dust remover and the fermentation heat supply tube, the combustion furnace comprises furnace and air channel of two side in the furnace, the inner top surface of the is provided with a feeding port, the upper part of the combustion furnace is provided with a blowing pipeline is connected with the dust remover, a dust remover of the top part is provided with air pipe and the fermentation heat supply tube is connected, the inner furnace and the air channel of the adjacent side wall is provided with upper air inlet, the lower part is provided with a lower air inlet channel, wherein the fermentation heat supply tube connecting with the exhaust fan, the combustion furnace of dust remover is set with an external cover. The system energy consumption, and there is no combustion of waste smoke discharge, energy-saving and environment-friendly.
NOVELTY - A low carbon high-efficient alcohol oil, comprises: 80-85 mass% methanol having purity of 99.9%, 0.1-0.3 mass% pine oil, 3-5 mass% acetone, 0.1-0.3 mass% dimethylbenzene, 0.1-0.3 mass% hydrogen peroxide, and 10-15 mass% purified water.    USE - As low carbon high-efficient alcohol oil (claimed) useful in hotel, restaurant, office, school dining hall, large gear and family as power fuel.    ADVANTAGE - The high efficient low carbon alcohol oil is environment-friendly and energy-saving, economic and safety; has high efficiency; is one of a renewable energy source, belonging to the field of biological liquid fuel; has wide raw material source; not only widely applied to hotel, restaurant, office, school dining hall, large gear and family as power fuel, but also suitable for a power boiler as fuel, having cheap price, low discharge, high efficiency, convenient to use, which meets our country economic sustainable development strategy and construction of energy-saving strategies and social development needs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the low carbon high-efficient alcohol oil, involving: using pressure automatic agitator stirring uniformity the above components, emulsifying and reacting for 24 hours, and then producing alcohol by the fine filter.
NOVELTY - In production of a biomass particles, a mixture of sawdust and bamboo shaving as raw materials, is used.    USE - In production of biomass particles (claimed).    ADVANTAGE - The method makes full use of the bamboo resource; opens up new field for the biomass particle manufacturing; does not need to add glue water to obtain product; and has higher heat value than the pure wooden product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass particle production device comprising: a raw material conveying belt (1), a hopper (2), a feeding device and granulating device (3), where the discharge end of the raw material conveying belt is located in the hopper; through the conveyer belt, the raw material directly entering into the lower part of the hopper; the feeding device raw material is sent to the granulating device, where the hopper and the feeding device further provided with a stirring device (4),where the stirring device (4) comprises a rotating pole and several groups of stirring paddle, where each group of stirring paddle is composed of 2-4 blades (5), where the blade in the same group are located at the same height, the blade and vertical to the plane of the rotating pole is 0-15 degrees of included angle.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of the biomass particle production device.    Raw material conveying belt (1)    Hopper (2)    Granulating device (3)    Stirring device (4)    Blades (5)    Paddle (6)
NOVELTY - Preparation of 1-(phenylethyl amino)-propan-2-ol (II) comprises reacting phenylethyl amine compound (I) with ethylene oxide to obtain compound (II).    USE - Preparation of 1-(phenylethyl amino)-propan-2-ol or its salt used as starting material for preparing lorcaserin or its salt (claimed).    ADVANTAGE - The method has cheap raw material, low cost production, simple operation, high yield, environment friendly, and produces 1-(phenylethyl amino)-propan-2-ol or its salt with improved quality and stability.    DETAILED DESCRIPTION - Preparation of 1-(phenylethyl amino)-propan-2-ol of formula (II) or its salt comprises reacting phenylethyl amine compound of formula (I) with ethylene oxide to obtain compound (II).    R1=H, straight or branched chain 1-4C alkyl, halo, methoxy, NO2, or OH; and    R2=H, straight or branched 1-4C alkyl, methoxy group, benzyloxycarbonyl group, tert-butoxycarbonyl group, methanesulfonyl group, toluenesulfonyl group, benzyl group, or benzyl group substituted straight or branched chain 1-4C alkyl, OH, straight or branched chain 1-4C alkoxy, halo, 4nitro, 4 amino, or 4-(difluoromethyl).
NOVELTY - Comminuting bacteria and organic solids in sludges from wastewater treatment plants and biogas by high-energy ultrasound, comprises: a first treatment step comprising irradiating sludge with ultrasonic transducers at high intensity of 50 W/cm3; and a subsequent second treatment step comprising irradiating pre-treated sludge with ultrasonic transducer having intensities below 5 W/cm2.    USE - The method is useful for comminuting bacteria and organic solids in sludges from wastewater treatment plants and biogas.    ADVANTAGE - The method reduces viscosity of the sludge, thus lowering the energy required for circulation.
NOVELTY - An underground fermentation installation has biomass production facility (B) on the ground having water barrier wall (W) which surrounds the ground surface part (G) and underground impermeable layer (L1), biomass fermentation site (D) where microorganisms are grown by anaerobic fermentation of biomass, biomass supply installation (6) where biomass produced with the biomass production facility is solubilized in water and supplied to biomass fermentation site, and biogas collection part (7) where the biogas produced during anaerobic fermentation in the biomass fermentation site is collected.    USE - Underground fermentation installation for micro-algae culture, edible plant production, and saccharification processing (all claimed).    ADVANTAGE - Biogas production cost is reduced, anaerobic fermentation is performed easily, has higher efficiency, and waste material is effectively used and reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the underground fermentation installation. (Drawing includes non-English language text).    Biomass supply installation (6)    Biogas collection part (7)    Biomass production facility (B)    Biomass fermentation site (D)    Ground surface part (G)    Underground impermeable layer (L1)    Water barrier wall (W)
NOVELTY - The system (200) has an outer can (210), which surrounds a recuperator can (238) to form a second annular gap between the recuperator can and an inlet port (234) for receiving an inlet cathode stream. A cathode feed tube (240) receives the inlet cathode stream near second end of a stack (202), in which a counter-flow recuperator is formed between the first and second annular gaps. A fuel processing reactor (218) processes the air fuel mixture in fluid communication with an anode feed plenum (224) to receive the air fuel mixture and distribute into the first end of stack.    USE - Solid oxide fuel cell system for generator.    ADVANTAGE - Reactant distribution is improved, and uniform heat distribution and efficient heat retention are achieved, since a hot zone with a center cathode air feed tube is provided.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of a solid oxide fuel cell system with a hot zone.    Solid oxide fuel cell system (200)    Stack (202)    Outer can (210)    Fuel processing reactor (218)    Anode feed plenum (224)    Inlet port (234)    Recuperator can (238)    Cathode feed tube (240)
NOVELTY - Producing a fermentation product comprises: (a) providing a feedstock slurry comprising fermentable carbon source, undissolved solids, and oil; (b) separating a portion of the undissolved solids and oil from the feedstock slurry to form an aqueous solution comprising fermentable carbon source, a wet cake comprising solids and an oil stream; and (c) adding the aqueous solution to a fermentation broth comprising microorganisms to produce the fermentation product.    USE - The method is useful for producing a fermentation product such as an alcohol product including ethanol, propanol, butanol, pentanol, hexanol, and fusel alcohol (all claimed), where the butanol is useful as a fuel additive, a feedstock chemical in the plastics industry, and as a food-grade extractant in the food and flavor industry.    ADVANTAGE - The method ensures efficient and environmentally friendly production of the fermentation product with high yield, reduced energy consumption, low toxicity and controlled amount of undissolved solids and/or oil.
NOVELTY - Cation-strung polymer comprising polymer backbone of a parent polymer and at least one side chain attached to the polymer backbone is new, where the side chains contain many of cationic sites.    USE - The cation-strung polymer is useful in: hydroxide exchange membrane; hydroxide exchange membrane fuel cell; anion exchange membrane; and device comprising anion exchange membrane fuel cells, electrolysis devices, solar hydrogen generation devices, redox flow batteries, dialysis devices, reverse osmosis devices, forward osmosis devices, pervaporation devices, ion exchange devices, sensors, and gas separation devices (all claimed).    ADVANTAGE - The cation-strung polymer provides membranes that have exceptional hydroxide ionic conductivity as well as low water uptake and excellent temperature resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for making cation-strung polymer.
NOVELTY - The filter has a support structure (3) placed adjacent to a ePTFE membrane (2). The ePTFE membrane is placed upstream of the support structure in a fuel stream. The structure fulfills a relation that a ratio of ePTFE membrane matrix tensile strength to support opening size or pore size is greater than 100000 per square inch/inch. The structure has Mullen burst pressure greater than fuel wet water penetration pressure of the ePTFE membrane. A composite membrane exhibits a ratio of resistances for water penetration to flow of the fuel stream that is greater than 104000 per square inch.    USE - Composite filter e.g. flat sheet form filter and pleated media form filter, for use in a filter housing for purifying fuel streams e.g. hydrocarbons such as petrol and middle distillate fuel e.g. diesel fuel, jet fuel, kerosene, fischer tropsch fuel and biodiesel, for an aerospace application, an industrial mining application and an automotive or trucking application (all claimed).    ADVANTAGE - The filter exhibits high resistance to water penetration with high resistance ratio so as to facilitate effective water separation under operating conditions covering a range of flows and differential pressures. The filter prevents penetration of water slugs to a down stream when wet with the fuel and faced with high impinging pressure without a possibility of deleterious leaching, extrusion or migration of super absorbent polymer.    DETAILED DESCRIPTION - The support structure comprises woven and nonwoven.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional side view of a composite filter.    Flow direction of fuel stream (1)    EPTFE membrane (2)    Support structure (3)
NOVELTY - A biodiesel composition (C1) comprises 4.5-95.5% a first 2-13 centistoke polyalphaolefin; 95.5-4.5% a second 2-13 centistoke polyalphaolefin; 4.5-5.5% polyolefinic ester; 4.5-80.5% calcium overbased sulfonate; and 19.5-20.5% bean oil or seed oil, where the first and second polyalphaolefins have different centistokes values and where the particle size of the calcium is 50-100 Angstrom .    USE - As biodiesel composition; for making a biodiesel fuel additive composition (claimed); and for diesel engine.    ADVANTAGE - The biodiesel composition has a shelf life of at least 9 months; and will not freeze up to a temperature of -33 degrees F. The addition to diesel, biodiesel, jet fuel, or bio jet fuels lowers the cloud point by at least 10 degrees F, preferably at least 25 degrees F; and reduces carbon emissions by at least 10%, preferably at least 14%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) making (M1) a biodiesel fuel additive composition involving combining at least 4.5-95.5% a first 2-13 centistoke polyalphaolefin, with 95.5-5.5% a second 2-13 centistoke polyalphaolefin, with 4.5-5.5% polyolefinic ester with, 4.5-80.5% calcium overbased sulfonate, and with 19.5-20.5% bean oil or seed oil, where the first and second polyalphaolefins have different centistoke values and where the particle size of the calcium is 50-100 Angstrom ;    (2) a method (M2) of using a biodiesel fuel additive composition involving adding into a fuel tank of an engine composition including 4.5-90.5% a first 2-13 centistoke polyalphaolefin, with 95.5-4.5% a second 2-13 centistoke polyalphaolefin, with 4.5-5.5% polyolefinic ester with, 4.5-80.5% calcium overbased sulfonate, and with 19.5-20.5% bean oil or seed oil, where the first and second polyalphaolefins have different centistokes values and where the particle size of the calcium is 50-100 Angstrom , and running the engine on contents in the fuel tank.
NOVELTY - Manufacture of solid fuel involves spin-drying (S1) multiple types of sludge, and drying (S2) the spin-dried sludge using a steam tube dryer.    USE - Manufacture of solid fuel used as granular solid fuel used for thermal power generation, manufacture of cement, and boiler.    ADVANTAGE - The method enables the manufacture of solid fuel from multiple types of sludge by an effective waste-treating apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid fuel manufacturing apparatus, which consists of the steam tube dryer and a spin-drying unit for spin-drying the sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart explaining the manufacture of solid fuel. (Drawing includes non-English language text)    Spin-drying sludge (S1)    Drying spin-dried sludge (S2)    Measuring amount of heat generated by dried material (S3)    Carrying out temporal storage of dried material (S4)    Burning odor component (S5)
NOVELTY - A basidiomycete strain, is new. The basidiomycete belongs to Phlebia which has 18S ribosomal RNA (rRNA) gene comprising 1761 base pair sequence (SEQ ID NO: 1) fully defined in the specification and lignin decomposability.    USE - The basidiomycete strain is useful for decomposing lignin in biomass resources (all claimed).    ADVANTAGE - The basidiomycete strain improves saccharification rate by saccharogenic amylase of biomass resources.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) decomposition method of lignin, involves culturing the basidiomycete strain in presence of biomass resources containing lignin;    (2) method for preparing saccharide, involves reacting sugar liquid which makes saccharogenic amylase with biomass resources which decomposes lignin, and preparing saccharide; and    (3) method for preparing target substance, involves culturing microorganisms which produce target substance and extracting target substance out of culture by culture medium which comprises the sugar liquid, or its fraction as carbon source.
NOVELTY - The solar-powered system (10) includes photovoltaic layer (30) disposed over the microstructure layer (20), and has positive-type layer (32) and negative-type layer (34). A cathode (52) is disposed within hydrogen collection micro-chamber (50) formed through microstructure layer and negative-type layer. An anode (62) is disposed within the oxygen collection micro-chamber (60) formed through the microstructure layer and the photovoltaic layer, with the oxygen collection micro-chamber spaced between 1 to 10 micrometers from the hydrogen collection micro-chamber.    USE - Solar-powered system for generation and storage of hydrogen gas in substrate microstructures at e.g. home, vehicle and power generating station.    ADVANTAGE - Micro electro mechanical system (MEMS) actuators are set at the ends of the hydrogen collection micro-chamber to facilitate storage and release of hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of the configuration of the solar-powered system for generation and storage of hydrogen gas in substrate microstructures.    Solar-powered system (10)    Microstructure layer (20)    Photovoltaic layer (30)    Positive-type layer (32)    Negative-type layer (34)    Hydrogen collection micro-chamber (50)    Cathode (52)    Oxygen collection micro-chamber (60)    Anode (62)
NOVELTY - Preparing pesticide comprises crushing aconite, rhizoma coptidis, pepper, radix aconiti carmichaeli, dandelion, purslane, herba houttuyniae and Andrographis to obtain powder, cooking the powder with water, filtering the cooked mixture to obtain medicinal liquid, then extracting water, adding Bdellovibrio, Metarhizium anisopliae and mushroom powders, emulsifier, penetrant and water regulator to obtain solution, dissolving turpentine and mineral oils by ethanol, and mixing synergistic agent, medicinal liquid, the obtained solutions and growth regulator and stabilizer.    USE - The method is useful for preparing pesticide for spinach planting (claimed).    ADVANTAGE - The method is capable of preparing pesticide with reduced toxic and residue, in eco-friendly manner.    DETAILED DESCRIPTION - Preparing pesticide comprises cleaning aconite, rhizoma coptidis, pepper, radix aconiti carmichaeli, dandelion, purslane, fructus xanthil, herba houttuyniae and Andrographis, crushing the cleaned raw material to obtain powder with 150-200 mesh, soaking the powder into water for 3 hours, cooking the mixture for 3-5 times, filtering the cooked mixture to obtain medicinal liquid, UV sterilizing the medicinal liquid, then extracting water, adding Bdellovibrio powder, bacteriophage powder, Metarhizium anisopliae powder, mushroom powder, emulsifier, penetrant and water regulator to obtain solution, adding turpentine oil and mineral oil, then dissolving with ethanol, adding synergistic agent into the medicinal liquid, stirring the mixture, then mixing the obtained solution, dissolved solution, and growth regulator and stabilizer, and diluting the mixture by 100 times of water.
NOVELTY - An ergosterol is prepared by fermenting penicillium mycelium waste with citric acid, washing with water to neutralize, adding dilute alkaline solution at volume ratio of 1:1-4, performing saponification at 85-95 degrees C for 2-2.5 hours, filtering, washing filtrate, adding organic solvent, mixing, heating, extracting at 90-100 degrees C for 1.5-2.5 hours, concentrating, dissolving in ethanol solution, filtering, and drying.    USE - Method for preparing ergosterol (claimed).    ADVANTAGE - The method is simple, low-cost and environment-friendly.
NOVELTY - The turbine (22) has a wind generating system comprising a wind capturing funnel (20), a turbine and a direct current generator (24). The system is connected to an electrolysis unit (26) for generating hydrogen, which is stored and used to power systems within a building (10). The funnel and another funnel are positioned along a face of the building that faces prevailing winds. The turbine comprises a windflow cavity and a conversion wheel adjacent to the windflow cavity. The electrolysis unit produces hydrogen gas (28) that is stored and used to power the building.    USE - Improved wind turbine for installation in a high-rise building e.g. office building and residential building.    ADVANTAGE - The turbine reduces architectural impact in new or existing high-rise buildings and reduces visual environmental impacts.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of functional elements and a process of a wind turbine.    Building (10)    Wind capturing funnel (20)    Wind turbine (22)    Direct current generator (24)    Electrolysis unit (26)    Hydrogen gas (28)
NOVELTY - The system (10) has a film water-retention-value detection unit (90) which detects the water retention value of the electrolytic membrane. The first pressure rise speed is set for making the target pressure value of hydrogen pressure, when detected water retention value is more than a threshold value. A pressure rise speed-regulation unit (92) sets the second pressure rise speed for making the target pressure value pressure, when detected water retention value is less than a threshold value. The second pressure rise speed is a speed slower than the first pressure rise speed.    USE - High-pressure water electrolysis system.    ADVANTAGE - Since the rapid pressure rise is suppressed after the system startup, the water retention value of the electrolytic membrane can be raised effectively, so that electrolytic membrane can ensure the desired water holding state. The film deterioration and decline in system efficiency can be suppressed effectively. The high-pressure water electrolysis system with favorable starting at simple structure can be achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for starting method of high-pressure water electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the high-pressure water electrolysis system. (Drawing includes non-English language text)    High-pressure water electrolysis system (10)    High-pressure water electrolyzer (12)    Water circulation apparatus (14)    Film water-retention-value detection unit (90)    Pressure rise speed-regulation unit (92)
NOVELTY - An earthworm breeding box comprises inner container which has space which breeds the earthworm enclosed with wall provided with vent hole, and outer container which includes gap. An inlet port is opened between clearance gap and external air below the outer container. An exhaust port is opened between the clearance gap and external air above the outer container. Air heated in the gap is raised by convection, and discharged from the exhaust port. Temperature rise in the gap is suppressed because cold external air enters in the gap from the inlet port.    USE - Earthworm breeding box for organic-refuse composting (claimed).    ADVANTAGE - The box is able to suppress temperature rise, thus decreasing the number of extinction and preventing approach of insect pest which accelerates proliferation of earthworm.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the earthworm breeding box.    Outer container cover (105)    Cold air intake (106)    Outside airflow (107)    Base (108)    Leg (112)
NOVELTY - The system 100 a hose fluidly connected to a dryer and adapted to connect to an engine, where the hose allows hydrogen gas to pass from the dryer to the engine. A controller is operatively connected to a positive electrode and a negative electrode in a generator to provide electric current to the positive and negative electrodes such that water in the generator is converted to oxygen and hydrogen gas through standard electrolysis, where the system is filled with water via an opening formed on a bubbler reservoir fluidly connected to an inner cavity of the generator.    USE - Electrolysis system for use in a truck for generating hydrogen gas.    ADVANTAGE - The system reduces exhaust and pollution from trucks in an economical, efficient and environmental-friendly manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an electrolysis system for generating hydrogen gas.
NOVELTY - The variable fuel cell power supply system (10) has at least one load bus (50), each connected to a power conversion unit (12) at the voltage converter device (40), at least one load coupler, each selectively connecting the load bus to a load line, and at least one process controller (20) responsive to operating parameters from the power conversion unit and load coupler. The process controller selectively engages at least one of the fuel cells (30), which dynamically adjusts the total generating capacity of all of fuel cells, to substantially meet the changing power needs of the load.    USE - Variable fuel cell power supply system used in e.g. local residence, building, plant.    ADVANTAGE - Monitors multiple components and controls the loads for balanced, reliable, robust, high power quality and independent power supply. Simulates the power reliability of a power grid, but generated within the physical boundaries of a service zone. The stand alone system includes redundancy that replaces the multi-feed network of the commercial power grid, to provide a robust power source that maintains the required energy balance within smaller, network as transient conditions occur. Provides a free-standing commercial non-rotating generation system, with no mechanical inertia, that meets the requirements of the residential customer for availability, reliability and durability because adaptive controls, switchable redundant capacities, and switchable loads mitigate the problems caused by imbalances and partial system failures.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell power supply system.    Variable fuel cell power supply system (10)    Power conversion unit (12)    Process controller (20)    Fuel cells (30)    Voltage converter device (40)    Load bus (50)
NOVELTY - Transparent ceramic material comprises a glassy matrix of silicon oxide containing nanocrystals of fluoride, such as lead (II) fluoride, sodium yttrium fluoride, yttrium (III) fluoride and potassium yttrium fluoride doped with rare earth ions. The rare earth ions are neodymium, thulium, holmium, erbium or ytterbium to absorb a wide range of energy from sun in red and infrared and efficiently convert to blue and UV range.    USE - Transparent ceramic material.    ADVANTAGE - The transparent ceramic material increases efficiency of hydrogen production via water photolysis in a photo-electrochemical cell, and extending range of spectral response of semiconductor catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for increasing efficiency of hydrogen production via water photolysis in a photo-electrochemical cell, which involves wrapping semiconductor catalyst with a transparent material.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation depicting spectrum of standard irradiance with main absorption band of dopant rare earth ions.
NOVELTY - Preparation of methanedisulfonic acid involves carrying out acidification process by reacting methanedisulfonate with acidifier to form mixture containing methanedisulfonic acid.    USE - Preparation of methanedisulfonic acid (claimed).    ADVANTAGE - The method economically and environmentally-friendly provides methanedisulfonic acid with high yield.
NOVELTY - Electrolysis device (1) comprises an electrolyzer (3) for electrolytic decomposition of water into hydrogen and oxygen, number of hydrogen-bearing components, and a chamber (2), which is present under negative pressure. The numbers of hydrogen-bearing components are arranged in the chamber.    USE - Used as an electrolysis device.    ADVANTAGE - The electrolysis device exhibits an explosion protective design; and is operated outside buildings in a simple manner.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the electrolysis device.    Electrolysis device (1)    Chamber (2)    Electrolyzer (3)    Electrolysis stack (4)    Valve (22)
NOVELTY - Method for processing white paeony root, by (a) collecting white paeony plant and washing to remove impurities and mud, (b) peeling outer skin and steaming, (c) adding alum and ginger to the steamed white paeony root and then adding water, soaking, and cooking the soaked material, baking and slicing, (d) subjecting the slice to ultraviolet light, and drying, and (e) storing the product using dry ice.    USE - The method is useful for processing white paeony root (claimed).    ADVANTAGE - The method is simple, prevents loss of active ingredient and pollution and improves white paeony root effeciency.    DETAILED DESCRIPTION - Method for processing white paeony root, involves (a) collecting four year old white paeony plant, choosing sunny day, removing stem and leaves, and washing the root to remove impurities and mud, (b) collecting fresh and cleaned roots and peeling outer skin and steaming for 10-20 minutes using steamer, (c) adding alum and ginger to the steamed white paeony root in ratio of 1:0.06-0.09:0.06-0.09 and then adding water to submerge and soaking for 6-8 hours, and cooking the soaked material at 100 degrees C for 30 minutes, baking the cooked material at 60 degrees C, until the water content reaches 24-28%, and slicing the dried material into 1.5-2 mm sheet, (d) subjecting the slice to ultraviolet light at 20-80 W for 2-4 hours, and drying at 60 degrees C for 7-8 hours, and (e) storing the product using dry ice, where the each bag contains 1 kg processed white paeony root and filling 10-20 g dry ice and sealing the bag to obtain the product.
NOVELTY - Method for treating goat manure, involves collecting excrement by digging and smoothing the ground and applying cement slurry as fermenting bed, performing microbial fermentation by uniformly mixing the goat dropping with microbial strain and culture bacteria solution, stacking, fermenting, after accumulating on mattress, stirring, generating organic fertilizer, placing the generated organic fertilizer into the planting pasture, feeding in goat grass, harvesting fermentation bed soil for planting grass, and then collecting goat manure.    USE - The method is useful for treating goat manure (claimed).    ADVANTAGE - The method is environmentally-friendly, saves energy and reduces emission.    DETAILED DESCRIPTION - Method for treating goat manure, involves collecting excrement by digging to the depth of 40-60 cm, smoothing the ground and applying cement slurry to 4-5 cm as fermenting bed, where the fermenting bed is set on a grid plate and the gap between the grid plate is 1-1.5 cm, and overhead placed on the top surface of the fermenting bed to collect the excrement, performing microbial fermentation by uniformly mixing the goat dropping with 100 g microbial strain and 60 kg culture bacteria solution in a ratio of 2-2.5%, stacking and fermenting at high temperature, after accumulating 7-10 days on mattress, stirring after 2-3 months, generating organic fertilizer by stirring the material in the fermentation, mixing 6 kg fermentation bed material and 1 kg natural soil, placing the generated organic fertilizer into the planting pasture, feeding in goat grass, harvesting fermentation bed soil for planting grass, and then collecting goat manure.
NOVELTY - Optimized homopolymer absorbent material comprises 2-5 wt.% of acrylamide monomer and 2-4 wt.% of methylenebisacrylamide as a cross-linking agent. The liquid fuel is selected from hydrocarbons derived from petroleum, biofuels and blends of diesel with biodiesel.    USE - Optimized homopolymer absorbent material used for removing free water from emulsified liquid fuels such as hydrocarbons derived from petroleum and biofuels such as blends of diesel and biodiesel.    ADVANTAGE - The optimized homopolymer absorbent material provides efficient removal of free water without direct contact with fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation depicting monitoring degree of swelling of hydrogel. (Drawing includes non-English language text).
NOVELTY - The method involves forming a groove (2) in an insulation portion (62), and forming a manifold is formed above the groove. The insulation portion is formed in circumference of an electroconductive portion (61) by molding a thermosetting insulation molding material. The electroconductive portion is formed by molding an electroconductive molding material containing thermosetting resin component, graphite particle, epoxy resin, and phenol type compound. A gasket is laminated on the insulation portion.    USE - Method for manufacturing fuel cell separator (claimed) such as polymer electrolyte fuel cell separator.    ADVANTAGE - The electroconductive portion and insulation portion can be precisely formed in furl cell separator, and the favorable adhesiveness between the electroconductive portion and insulation portion can be improved, such that the favorable productivity of the fuel cell separator can be maintained and the durability of the separator can be improved. The cathode side separator and anode side separator can be adhered by using the olefin resin adhesive agent, such that the elution of the impurity from an adhesive agent can be suppressed. Since the gasket is laminated on the separator, the impurity can be removed by wet blasting process even if the component derived from the material for forming a gasket adheres on the separator as an impurity, such that the adhesion amount of the impurity in the surface of the separator can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell separator.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional views of the fuel cell separator.    Groove (2)    Fuel cell separator (20)    Cathode and anode side separators (21,22)    Electroconductive portion (61)    Insulation portion (62)
NOVELTY - Microbial inoculant is obtained from thermophilic nitrogen-addicted bacteria including Bacillus mucilaginosus, B.subtilis, B.licheniformis and Micromonospora.    USE - The microbial inoculant is useful in factory for processing sewage including surface water sewage, and aquaculture sewage (all claimed).    ADVANTAGE - The inoculant maintains physical, chemical or biological property of water, improves use value of water, overcomes serious consequences of water pollution that endangers human health, industrial and agricultural production, requires minimal dosage, has no antagonistic effect, enables deodorization, causes no secondary pollution, reduces pollution rate, and is cost-effective and suitable for industrial production.
NOVELTY - Degrading carbon, nitrogen and phosphorus from sewage sludge, comprises taking the organic sludge as complementing carbon source, then denitrification and dephosphorization, increasing the organic load of a reactor, controlling anaerobic membrane bioreactor parameter to form facultative or anaerobic condition to form facultative composite, performing synchronization to sewage.    USE - The method is useful for degrading carbon, nitrogen and phosphorus from sewage sludge (claimed).    ADVANTAGE - The method is capable of simply degrading carbon, nitrogen and phosphorus from sewage sludge with less energy consumption, reduces the discharge of the carbon and organic sludge to avoid secondary pollution.
NOVELTY - The biological united photo-catalytic composite degradation liquid system comprises a micro-biodegradable agent and photo-catalyst mixed solution.    USE - The biological united photo-catalytic composite degradation liquid system is useful for degrading phenol waste water.    ADVANTAGE - The system is simple to operate and cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing biological combined photo-catalytic composite degradable liquid system.
NOVELTY - Yellow mealworm manure organic fertilizer composition, comprises 65-75 wt.% yellow mealworm manure, 8-10 wt.% loess, 8-10 wt.% tobacco straw, 4-6 wt.% vermiculite, 4-6 wt.% perlite and 1-3 wt.% effective-microorganism.    USE - Used as an organic fertilizer composition.    ADVANTAGE - The fertilizer: remains in soil fro long-term; satisfies fertility requirements for different plants; promotes growth of crops; utilizes waste and minimizes environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing organic fertilizer composition, comprising: (i) weighing total yellow mealworm manure into A and B parts in a mass ratio of 5:2, mixing yellow mealworm manure-A with loess and tobacco straw and crushing in a crusher to obtain mixed material-A; (ii) sieving the mixed material-A via screen to obtain mixed material-B; (iii) blending vermiculite and perlite with yellow mealworm manure-B and uniformly mixing to obtain mixed material-C; (iv) adding effective-microorganism and mixed material-C into a plastic barrel, sealing and fermenting under room temperature for two months to obtain fermented material-A; and (v) adding mixed material-B into fermented material-A, stirring uniformly and extruding via open extrusion granulator.
NOVELTY - Kitchen garbage is fermented and the fermentation liquid is filtered. Hydrochloric acid and calcium chloride are added to the fermentation liquid, and calcium oxalate is separated out. The fermentation liquid is filtered and oxalate is separated. Sulfuric acid is added to the oxalate and the reaction liquid is filtered using filter paper to obtain oxalic acid.    USE - Manufacture of oxalic acid (claimed).    ADVANTAGE - The method is simple, economical and enables to prepare oxalic acid with high extraction rate.
NOVELTY - Pasiniazid is prepared by p-amino salicylic acid and organic ester solvent, adding water to the solution, stirring while heating, cooling to form crystal, and filtering.    USE - Method of preparing pasiniazid (claimed).    ADVANTAGE - The method has high efficiency; can be applied to industrial production; prepares transparent product having good appearance, good stability, and a purity of higher than 99%; and is simple, short, low cost, easy to control, and environment-friendly.
NOVELTY - Glycol reduction process comprises injecting an electrolyte comprising alcohol, precipitation supplemental agent and glycol into a reactor provided with an anode (120) and a cathode (130), and electrolyzing glycol in the electrolyte (110) by applying voltage to the reactor (150).    USE - The method is useful in glycol reduction process (claimed).    ADVANTAGE - The method and the device electrochemically reduce glycol to 1,4-dioxane, which produces renewable energy sources (alkane and hydrogen), and reduces processing costs and minimizes multi-step process when compared with traditional method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for glycol reduction device comprises the reactor including the electrolyte (alcohol, the precipitation supplemental agent and glycols), the anode, which is partially or completely impregnated in the electrolyte and equipped within the reactor and the cathode, which is partially or completely impregnated in the electrolyte and equipped within the reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the cross-sectional view of the glycol reduction device.    Electrolyte (110)    Anode (120)    Cathode (130)    Reactor (150)
NOVELTY - This utility model claims one kind of biological wastewater production plant by utilizing alcohol and fulvic acid potassium sulphate concentrated solution and plant organic fertilizer's production system, wherein connecting with a cooling tower, an adjusting pool, an inclined plate sedimentation tank, a bag-type filter, zeolite adsorption device, resin absorption device, decompressing and concentrating and spray freezing and drying tower, wherein it further comprises potassium sulphate concentrated liquid production system and plant organic fertilizer production system, the utility model solves the problem of alcohol's factory's biological waste water processing, the production plant's fulvic acid the purity of the product is high, and it can be broadly applied to the field of medicine, chemical industry, agriculture, environmental protection and so on, recycling process's waste liquid, waste residue and waste the processing factory can be high quality's production plant organic fertilizer, waste resource utilization's destination, and the production system can be biological in waste water recycling alcohol's, realizes the effective recovered resource utilization.
NOVELTY - The sewage processing device is equipped with automatic control system, biological zeolite bed and sequencing batch bioreactor which are connected with each other. The sequencing batch bioreactor is provided with reaction column water inlet tank (2), water tank (1), water inlet pump (4), and aeration pump (5). The formulation microbial inoculum is composed bacteria Paracoccus sp. strain, lazoogloeo strain, quinoline degrading bacteria Pseudomonas sp. BW004 strain, and carbazole degrading bacteria Pseudomonas sp. BC046 strain.    USE - Sewage processing device.    ADVANTAGE - The sewage processing device with simple and compact structure can be provided and operated automatically. The nitrogen-containing substance can be processed effectively. The organic compound substance can be degraded easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a wastewater processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sewage processing device.    Water tank (1)    Reaction column water inlet tank (2)    Water outlet (3)    Water inlet pump (4)    Aeration pump (5)
NOVELTY - A polypeptide selected from specific amino acid sequences, is new.    USE - For preparing lipase suitable for cell culture, preferably Escherichia coli. The lipase is used in food processing, oil chemical industry, medicine, detergent and biological diesel oil.    ADVANTAGE - The lipase has higher catalytic activity in the organic solvent environment. The lipase has excellent hot stability, good stability and organic solvent tolerance.    DETAILED DESCRIPTION - A polypeptide selected from amino acid sequence of: (1) 210 amino acids (SEQ ID NO: 2) as given in the specification, or (2) SEQ ID NO: 2 represented by 29-210 amino acid sequence, or (3) upper base amino acid sequence obtained by substituting, deleting or adding of one or several amino acids and having SEQ ID NO: 2 lipase activity. INDEPENDENT CLAIMS are included for the following:    (1) new polynucleotide expression vector;    (2) new expression vector comprising the polypeptide;    (3) new cell comprising the polypeptide, where cell is a recombinant cell; and    (4) a composition comprising the lipase.
NOVELTY - Anti-epileptic, ilepcimide is prepared by mixing solvent, acetyl piperidine, piperonal, and catalyst in a reactor, slowly heating to reflux, sampling and analyzing until piperonal content is not more than 0.5%, standing to form layers, separating oil layer, water washing, removing solvent, and collecting crude product. Solvent is toluene, xylene, ethyl acetate, methylene dichloride or chloroform.    USE - Preparation of anti-epileptic medicine, ilepcimide.    ADVANTAGE - The process is simple, reagent consumed is low, and is environment-friendly.
NOVELTY - A kitchen waste decomposing microbial inoculum comprises 30-50 pts. wt. Bacillus subtilis, 10-30 pts. wt. Saccharomyces cerevisiae, 10-30 pts. wt. Trichoderma viride and 10-30 pts. wt. Aspergillus niger.    USE - The microbial inoculum is useful for decomposing kitchen waste (claimed).    ADVANTAGE - The kitchen waste can be decomposed cost-effectively and conveniently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the inoculum, which involves obtaining B.subtilis, S.cerevisiae, A.oryzae, T.viride and A.niger, culturing the strain and drying to obtain the single strain bacterial powder, and preparing the agent comprising powder of the above strains in specific concentration.
NOVELTY - Microbial inoculum comprises Bacillus cereus, Lactobacillus acidophilus, Bacillus stearothermophilus, Pseudomonas pseudoalcaligenes and Saccharomyces cerevisiae.    USE - The microbial inoculum is useful for degrading domestic garbage, preferably kitchen garbage (claimed).    ADVANTAGE - The microbial inoculum has garbage degradation rate of 80% and is environmentally-friendly.
NOVELTY - A reaction device comprises H-shaped electrolytic cell (1), sand core diaphragm (2), reference electrode (3), anode chamber (4), cathode chamber (5), electrochemical work station, light source device and hydrogen collecting device.    USE - Reaction device used for hydrogen production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of reaction device.    H-shaped electrolytic cell (1)    Sand core diaphragm (2)    Reference electrode (3)    Anode chamber (4)    Cathode chamber (5)
NOVELTY - Preparation of (S)-N-((3-(3-fluoro-4-morpholinophenyl)-2-oxo-oxazolidin-5-yl)methyl)acetamide (linezolid), comprises: reacting (R)-5-azidomethyl-3-(3-fluoro-4-morpholin-4-yl-phenyl)-oxazolidin-2-one with thioacetic acid in presence of an anionic clay as a base; and purifying the resulting linezolid.    USE - The process is useful for preparing linezolid (claimed), which is used as antibiotic for treating infections caused by Streptococcus and methicillin-resistant Staphylococcus aureus. No biological data given.    ADVANTAGE - The process utilizes the anionic clay that improves the yield of linezolid, and eliminates the problem of epimerization and also the use of hazardous solvent such as pyridine, hence it is safe and environmentally friendly.
NOVELTY - Biomass is pre-processed by stirring biomass containing cellulose in processing agent liquid mixture containing ionic liquid and peroxide, depositing cellulose from liquid mixture comprising biomass containing cellulose, ionic liquid, and peroxide, and reproducing cellulose.    USE - Pre-processing method of biomass for manufacture of monosaccharide, disaccharide, and/or oligosaccharide (claimed).    ADVANTAGE - Monosaccharide, disaccharide, and/or oligosaccharide can be manufactured with high efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacture of monosaccharide, disaccharide, and/or oligosaccharide which involves carrying out enzymatic decomposition of regenerated cellulose by cellulase; and    (2) pre-processing agent for pre-processing cellulose-containing biomass which contains ionic liquid and peroxide.
NOVELTY - Degrading lignin, comprises contacting the lignin with a layered double hydroxide catalyst in the presence of a liquid solvent.    USE - The method is useful for degrading lignin (claimed) for the production of fuel and chemical.    ADVANTAGE - The feasible method is capable of degrading lignin for the subsequent production of fuel and chemical in a cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a layered double hydroxide catalyst for lignin degradation comprising hydrotalcite impregnated with nickel at a ratio of 1-15 wt.% of nickel/ hydrotalcite.
NOVELTY - The method (100) involves measuring (104) an intensity of a reference gas such as nitrogen. The intensity of calibration gas such as methane is measured (108). The measurement of an intensity of a test gas such as natural gas is calibrated (112) using measurement of the intensity of the reference gas and measurement of the intensity of the calibration gas. The variations in intensity of the reference gas are determined from known intensities of reference gas and test gas. The measurement of the intensity of test gas is adjusted based on variation.    USE - Method for calibrating detected intensity of gas components such as natural gas (claimed) supplied from utility company to home or business.    ADVANTAGE - The detected intensity of gas components can be calibrated efficiently, for determining the quality of gas with high precision.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a gas quality assessment system.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the method for calibrating detected intensity of gas components.    Method for calibrating detected intensity of gas components (100)    Step for measuring intensity of reference gas (104)    Step for measuring intensity of calibration gas (108)    Step for calibrating measurement of intensity of test gas (112)
NOVELTY - Preparation of crystalline Form G of febuxostat involves use of a mixed solvent of methanol and water having a volume ratio of methanol to water of 5:95 to 45:55.    USE - For preparation of crystalline Form G of febuxostat, which is used as Xanthine oxidase inhibitor (claimed).    ADVANTAGE - The process is eco-friendly, cost-effective, and industrially advantageous process that involves the use of a lesser amount of methanol as compared to the amount of water, controls the formation of genotoxic impurities, and avoids the need for reducing the particle size by carrying out micronization. The crystalline Form G of febuxostat is free of the genotoxic impurities selected from 2-(3-cyano-4-hydroxyphenyl)-4-methylthiazole-5-carboxylic acid ethyl ester, 1-bromo-2-methylpropane, ethyl-2-chloroacetoacetate, methyl methane sulfonate, ethyl methane sulfonate, acetoacetic acid ethyl ester, ethyl 2,2-dichloro-3-oxobutanoate, and n-butyl bromide; febuxostat ethyl ester impurity; 2-(3-carbamoyl-4-(2-methylpropoxy)phenyl)-4-methyl-1,3-thiazole-5-carboxylic acid impurity; and methanol.
NOVELTY - Preparing a slurry of a pulverized solid in liquid or supercritical carbon dioxide comprises: making a water-pulverized solid slurry at ambient pressure; press arising the water-pulverized solid slurry; and mixing the pressurized water-pulverized solid slurry with liquid or supercritical carbon dioxide in a pressurized chamber, to form a carbon dioxide-pulverized solid slurry.    USE - The method is useful for preparing a slurry of a pulverized solid (claimed) such as coal, petcoke and biomass.    ADVANTAGE - The method economically prepares slurry of pulverized solid via a phase inversion, by which hydrophobic coal surfaces are preferentially wetted by carbon dioxide, rather than water, thus efficiently preventing the system to be brought to high process temperatures and avoiding the use of a large energy investment, high heat capacity and enthalpy of vaporization.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic illustration of a method for preparing a slurry of a pulverized solid.    Slurry mixing tank (10)    Pump (12)    Pressurized mixing vessel (14)    Carbon dioxide-rich phase (16)    Heavy aqueous phase. (18)
NOVELTY - The manufacturing method involves repeatedly performing alternately the coating of catalyst ink (2,3) on electrolytic membrane (1) and then heat drying it for couple of times to form a catalyst layer of MEA on the electrolytic membrane. A specific swelling ratio of each solvent applied to coating surface direction with respect to electrolytic membrane coated with catalyst ink is set by using 30 percent or less catalyst ink during first time coating of catalyst ink on the electrolytic membrane.    USE - Manufacturing method for fuel cell MEA.    ADVANTAGE - Suppresses swelling, wrinkling and cracking of catalyst layer of MEA during manufacture of MEA of polymer electrolyte fuel cell by performing repeated coating and heat drying of coated catalyst ink when forming the catalyst layer of MEA.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view during formation of catalyst layer on electrolytic membrane.    Electrolytic membrane (1)    Catalyst ink (2,3)    Gasket layer (4)    Mask (5)    Gasket layer with mask (6)
NOVELTY - A bark is baked at 10% or less oxygen concentration and 170-350 degrees C. The moisture content of the obtained baking material is adjusted to 10-50%, and the density of the baked material is increased more than volume density of 0.5 g/cm3 measured by bulk density test method based on JIS K 2151.    USE - Manufacture of solid fuel (claimed) used as fuel for powdered coal boiler, power generation system and incineration system.    ADVANTAGE - The method enables manufacture of solid fuel with high yield and having excellent density, grindability, and calorie amount yield.
NOVELTY - 5-30 wt.% Biomass, 50-90 wt.% coal and/or 5-20 wt.% petroleum coke are mixed, dried, and crushed. The crushed component is mixed with binder to obtain feedstock. The obtained feedstock is briquetted, cured, and torrefied, to obtain fuel briquette.    USE - Manufacture of fuel briquette used for domestic open fire and multifuel stove.    ADVANTAGE - The torrefaction process reduces the smoke producing volatile components and improves the performance of the briquettes on domestic fire. Since the torrefaction process is an in-situ process using the existing plant equipment, the operation cost is reduced. The amount of torrefied biomass incorporated into the fuel briquette is increased without reducing the yield, strength and appearance, and the amount of carbon dioxide and other pollutants emitted during combustion is reduced.
NOVELTY - A catalyst comprises shear granulated porous composition material comprising spatial heat-conductive network metallic aluminum, Raney cobalt and binding agent. The binding agent contains N-type zeolite. The particles of Raney cobalt are located in direct contact with particles of zeolite.    USE - Catalyst is used for producing carbon monoxide and hydrogen from isoparaffin-enriched synthetic oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catalyst.
NOVELTY - Fertilizer preparation involves utilizing (in wt.%): wheat straw (40-60), inoculant (0.08-0.12), chicken manure (10-14), rapeseed cake (14-20), nitrogenous fertilizer (4-6) and phosphate fertilizer (11.88-19.92).    USE - Method for preparing fertilizer used for improving growth of cabbage (claimed).
NOVELTY - Fertilizer composition preparation involves selecting raw materials (pts. wt.): animal excrement (20-35), vermiculite (15-25), grass ash (15-25), cooked pine needles (10-20), moss (10-15), calcium superphosphate (5-10), biological enzyme (1-3) and organic fertilizer fermenting agent (1-3). Animal excrement, vermiculite and pine needle are crushed by using crusher. The crushed material is put into a fermentation tank. Biological enzyme, organic fertilizer fermenting agent and water are added to the fermentation tank, and then stirred for 10-15 minutes.    USE - Method for preparing fertilizer composition for blueberry (claimed).    ADVANTAGE - The method enables to produce eco-friendly fertilizer composition that has vermiculite and grass ash, which increase content of mineral and amino acids in fertilizer.    DETAILED DESCRIPTION - Fertilizer composition preparation involves selecting raw materials (pts. wt.): animal excrement (20-35), vermiculite (15-25), grass ash (15-25), cooked pine needles (10-20), moss (10-15), calcium superphosphate (5-10), biological enzyme (1-3) and organic fertilizer fermenting agent (1-3). Animal excrement, vermiculite and pine needle are crushed by using crusher. The crushed material is put into a fermentation tank. Biological enzyme, organic fertilizer fermenting agent and water are added to the fermentation tank, and then stirred for 10-15 minutes. The fermentation tank is sealed for carrying out fermentation for 60-70 hours. Moss is added to the fermenting tank and then sealed the tank, where fermentation is carried out at 65-75 degrees C. Fermentation tank is opened after 20-30 days, and grass ash is added to the tank. The obtained fermented product is kept at cool place and dried to maintain moisture content at 8%. Calcium superphosphate is added to the obtained product, and then mixed them uniformly. The obtained product is granulated by using granulator to obtain biological organic fertilizer.
NOVELTY - Fertilizer comprises (in pts.wt.): animal excrement (20-35), vermiculite (15-25), peat soil (15-25), pine needle (10-20), moss (10-15), calcium superphosphate (5-10), biological enzyme (1-3) and organic fertilizer (1-3).    USE - Fertilizer used for growing blueberry (claimed).    ADVANTAGE - The fertilizer provides nutrients to blueberry in eco-friendly manner.
NOVELTY - Producing cresol, comprises (i) taking phenol and methanol as raw materials; (ii) reacting at 200-500 degrees C, and feeding at weight hourly space velocity of 0.5-20/hour; (iii) pre-heating the raw materials, mixing the mixture with a diluent gas, and continuously passing through a bed layer of molecular sieve catalyst, and obtaining vapor-phase cresol; and (iv) adding anisole as starting material into a reactor inlet to continuously produce cresol, mixing the molecular sieve catalyst with a binding agent, performing acid treatment, subjecting the acidic product, and performing digital modulation.    USE - The method is useful for producing cresol (claimed).    ADVANTAGE - The method has cresol selectively rate reaching up to 94% from 50%; utilizes catalyst having good stability and environmental friendly effect, and a device without causing corrosion; and is suitable in industrial application.    DETAILED DESCRIPTION - Producing cresol, comprises (i) taking phenol and methanol as raw materials; (ii) reacting at 200-500 degrees C, and feeding the raw materials at weight hourly space velocity of 0.5-20/hour under the reaction conditions; (iii) pre-heating the raw materials, mixing the mixture with a diluent gas, and continuously passing through a bed layer of molecular sieve catalyst, and obtaining vapor-phase cresol; and (iv) adding anisole as a starting raw material into a reactor inlet to continuously produce cresol, mixing the molecular sieve catalyst with a binding agent, performing acid treatment, subjecting the acidic product, and performing digital modulation.
NOVELTY - Preparing chiral sertraline hydrochloride, involves: mixing racemic sertraline and D-mandelic acid chiral ionic liquid, adding absolute ethyl alcohol and continuously stirring for 1 hour, followed by filtering to a filter cake (a), adding the filter cake (a) in an aqueous solution of sodium hydroxide and stirring for 1 hour at room temperature, and then adding methylene dichloride to obtain extracting solution; adding aqueous hydrochloric acid to the extracting solution until there is no precipitate, and filtering to obtain filter cake (b).    USE - In preparing chiral sertraline hydrochloride (claimed) for treating mental depression.    ADVANTAGE - The method is simple and convenient, produces chiral sertraline hydrochloride with high yield ( not less than 80%) and with high optical purity ( not less than 98%), shows high efficiency, less waste, reused the ionic liquid thus economical and environment-friendly.    DETAILED DESCRIPTION - A method of preparing a chiral sertraline hydrochloride, involves: mixing racemic sertraline and D-mandelic acid chiral ionic liquid at 10-100 degrees C, adding absolute ethyl alcohol and continuously stirring for 1 hour, followed by filtering to a filter cake (a), adding the filter cake (a) in an aqueous solution of sodium hydroxide and stirring for 1 hour at room temperature, and then adding methylene dichloride to obtain extracting solution; adding aqueous hydrochloric acid to the extracting solution until there is no precipitate, and filtering to obtain filter cake (b), where the filter cake (b) is cis-(1S,4S)-sertraline hydrochloride; and recovering D-mandelic acid chiral ionic liquid; where the molar ratio of sertraline and D-mandelic acid chiral ionic liquid is 1:2-3, where the absolute ethyl alcohol to volume weight of sertraline is 1-5 ml/g.
NOVELTY - (1S,3aR,6aS)-N-((S)-1-(cyclopropylamino)-1,2-dioxohexan-3-yl)octahydrocyclopenta(c)pyrrole-1-carboxamide (I) or its salt is new.    USE - As intermediate for preparation of Telaprevir (claimed) as reversible protease inhibitors.    ADVANTAGE - The compound (I) prepares telaprevir with cost effective, simple and convenient method.    DETAILED DESCRIPTION - (1S,3aR,6aS)-N-((S)-1-(cyclopropylamino)-1,2-dioxohexan-3-yl)octahydrocyclopenta(c)pyrrole-1-carboxamide compound of formula (I) or its salt is new.    R1=H, or amino protecting group selected from tert-butoxycarbonyl (Boc), benzyloxycarbonyl (Cbz), methoxycarbonyl (Fmoc), allyloxycarbonyl group (Alloc), (trimethylsilyl) ethoxycarbonyl (Teoc), methoxycarbonyl (Meoc), ethoxycarbonyl (Etoc).    INDEPENDENT CLAIMS are included for the following:    (1) preparation of the compound (I); and    (2) preparation of Telaprevir involving: condensing (1S,3aR,6aS)-N-((S)-1-(cyclopropylamino)-1,2-dioxohexan-3-yl)octahydrocyclopenta(c)pyrrole-1-carboxamide with (S)-2-(2-cyclohexyl-2-((pyrazine-2-carbonyl)-amino)-acetylamino)-3,3-dimethyl-butyric acid in presence of condensing agent selected from Disseminated intravascular coagulation (DIC), (DIC), N,N'-dicyclohexylcarbodiimide (DCC), hydroxybenzotriazole (HOBT) in 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide (EDC.HCl), benzotriazolyloxy-tris(pyrrolidino)-phosphonium hexafluorophosphate (PyBOP), bromotripyrrolidinophosphonium hexafluorophosphate (PyBroP), 1-(bis(dimethylamino)methylene)-1H-1,2,3-triazolo(4,5-b)pyridinium 3-oxid hexafluorophosphate (HATU), 1H-Benzotriazolium 1-(bis(dimethylamino)methylene) -5chloro-,hexafluorophosphate (1-),3-oxide (HCTU), 3-(diethoxy-phosphoryloxy)-3H-benzo(d)(1,2,3) triazin-4-one (DEPBT) and/or N-ethoxycarbonyl-2-ethoxy-1,2-dihydroquinoline (EEDQ) to obtain telaprevir.
NOVELTY - An argatroban intermediate is prepared by performing condensation reaction of 1st compound and 2nd compound in condensing agent and aprotic solvent in which chemical name of argatroban intermediate is (2R,4R)-ethyl-1-((S)-2-(tert.-butoxy)-5-(3-nitroguanidine)valeryl)-4-methylpiperidine-2-carboxylate and condensing agent is 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide hydrochloride, N,N-diisopropylcarbodiimide, and/or N,N'-carbonyldiimidazole.    USE - Preparation of argatroban intermediate (claimed).    ADVANTAGE - Raw material has wide source and is cheap and easy to obtain, reaction condition is mild, reaction step is short, operation is simple, and product is convenient to purify and can be synthesized in laboratory, production cost is low, product yield is high, and preparation process is environment-friendly.    DETAILED DESCRIPTION - An argatroban intermediate of formula (II) is prepared by performing condensation reaction of 1st compound of formula (I-A) and 2nd compound of formula (I-B) in condensing agent and aprotic solvent in which chemical name of argatroban intermediate of formula (II) is (2R,4R)-ethyl-1-((S)-2-(tert.-butoxy)-5-(3-nitroguanidine)valeryl)-4-methylpiperidine-2-carboxylate and condensing agent is 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide hydrochloride, N,N-diisopropylcarbodiimide, and/or N,N'-carbonyldiimidazole.
NOVELTY - A compound microorganism fertilizer comprises fermentation product of nitrogen-fixing bacteria, phosphorus bacteria, and potassium bacteria.    USE - As compound microorganism fertilizer (claimed) for improving content of nitrogen, phosphorus and potassium elements of plant and for improving quality and flavor of food and vegetables.    ADVANTAGE - The fertilizer meets the comprehensive need of nitrogen, phosphorus and potassium nutrients of plant; is low cost; is effective at low dosage; avoids wastage of components; is good for agricultural production of plants; can greatly reduce planting cost; improves yield of plant; and improves the quality and flavor of food and vegetables.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer involving selecting strain, where the selected strain is nitrogen-fixation bacteria and phosphorus bacteria capable of decomposing organic and inorganic compounds and potassium bacteria strain capable of decomposing compound of potassium, respectively culturing, and fermenting, to the fermentation product of the selected strain respectively adding grass, soybean meal, bran, corn powder, rice rear auxiliary material and fermenting, and after fermentation of the product forming fertilizer.
NOVELTY - A method of preparing enteromorpha phosphorylated oligonucleotide sugar powder fertilizer involves: preparing enteromorpha oligonucleotide by adding 10-15% of phosphorylation reagent in oligosaccharide Enteromorpha, and adjusting pH of 8-9, carrying out catalytic phosphorylation reaction for 3-6 hours, adjusted pH 7 using phosphoric acid, then spray drying to obtain enteromorpha phosphorylated oligonucleotide sugar powder fertilizer.    USE - In preparing enteromorpha phosphorylated oligonucleotide sugar powder fertilizer as seaweed fertilizer (claimed).    ADVANTAGE - The fertilizer is rich in active substance sodium, phosphorus and potassium; is non poisonous and environment-friendly; and has obvious drought resistance and anti-hot air, cold-resistant anti-freezing, anti-falling effects.
NOVELTY - Aquatic cultivation fertilizer comprises rape seed oil residues, oyster powder, carrier, sucrose, probiotics, compound sodium nitrophenolate and sodium humate, where the carrier comprises rice bran, wheat bran and bran, the mass ratio of the carrier and rape seed oil residues is 0.5-0.8:1, the mass ratio of the sucrose and rape seed oil residues is 0.06-0.08:1, the mass ratio of the compound sodium nitrophenolate and sodium humate and rape seed oil residues is 0.07-0.09:1, and the mass ratio of the oyster powder and rape seed oil residues is 0.1-0.2:1.    USE - As aquatic cultivation fertilizer.    ADVANTAGE - The aquatic cultivation fertilizer can be simply and rapidly, and long-term effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the aquatic cultivation fertilizer which involves stirring and mixing the rape seed oil residues, carrier, sucrose, probiotics, compound sodium nitrophenolate and sodium humate at a stirring speed of 25-35 revolutions/minute, adding the mixture into fermentation tank and adding edible phosphoric acid, and water, performing fermentation process at 20-28 degrees C for 10 days, filtering the fermented mixture, drying the mixture at 120-150 degrees C for 12-17 minutes, and adding the mixed oyster powder.
NOVELTY - Bioorganic fertilizer comprises 0.1-0.5 pts. wt. Bacillus licheniformis, 0.2 pts. wt. Trichoderma viride, 5-15 pts. wt. ammonium dihydrogen phosphate, 0.1-0.3 pts. wt. organic material decomposition agent, where the organic material decomposition agent comprises 50-75 pts. wt., 60-90 pts. wt. or 60-80 pts. wt. fresh tobacco leaf and 25-50 pts. wt. humus, 10-40 pts. wt. straw, or 0-20 pts. wt. poultry manure and 0-30 pts. wt. livestock manure, where the above-mentioned raw materials are in dried form.    USE - The bioorganic fertilizer is useful for providing disease resistance.    ADVANTAGE - The fertilizer has high content of organic matter, phosphorus and potassium, is prepared in large quantity easily, simply, and does not cause secondary pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the bioorganic fertilizer, which involves weighing the above-mentioned raw materials, mixing the raw materials except above-mentioned microorganisms, decomposing for 3-4 weeks, where turning once in every 2-3 days, after each 5 days turning one times, reducing the temperature to 40 degrees C and water content to 30%, adding the above-mentioned microorganisms to ferment for 7 days, when the temperature is reduced to normal temperature, the water content is 25-28%, crushing and sieving to obtain the product.
NOVELTY - Micro agricultural seedling substrate comprises mixture of garden soil or clay matrix comprising 25-45 wt.% matrix, and 55-75 wt.% garden soil or clay, substrate comprising 60-80 wt.% organic, 1-3 wt.% nitrogen, 1.5-3.5 wt.% phosphorus, 2-4 wt.% potassium, trace magnesium, calcium, iron, 0.02-0.08 wt.% manganese and boron, where pH of the matrix is 6.5-6.8.    USE - As micro agricultural seedling substrate.    ADVANTAGE - The micro agricultural seedling substrate is high in nutrient content, and environmentally-friendly, has good odor-removing function, and avoids peculiar smell.    DETAILED DESCRIPTION - Micro agricultural seedling substrate comprises mixture of garden soil or clay matrix comprising 25-45 wt.% matrix, and 55-75 wt.% garden soil or clay, substrate comprising 60-80 wt.% organic, 1-3 wt.% nitrogen, 1.5-3.5 wt.% phosphorus, 2-4 wt.% potassium, trace magnesium, calcium, iron, 0.02-0.08 wt.% manganese and boron, where pH of the matrix is 6.5-6.8. The organic matter comprises 1-4 pts. wt. vinegar, 1-3 pts. wt. starch-acrylic graft copolymer, 15-40 pts. wt. straw inoculants, 15-40 pts. wt. fermented human and animal feces, 10-18 pts. wt. mushroom fungus residue, 3-6 pts. wt. waste bamboo residues, 2-5 pts. wt. toner plant parts, 5-10 pts. wt. sludge residue, 4-6 pts. wt. bone meal, and 4-9 pts. wt. beans parker.
NOVELTY - Soil matrix comprises matrix and garden soil or clay. The matrix comprises organic matter, where the organic matter comprises potassium, nitrogen, phosphorus, copper, zinc, iron, manganese, boron, calcium and magnesium and also comprises bamboo vinegar, crystal mother liquor containing abamectin, nucleotide salt, starch-acrylic graft copolymer, straw rotten agent, fermented human and animal excreta, edible fungi residue, waste bamboo sawdust, plant charcoal powder, sludge, bone powder and soybean meal.    USE - The soil matrix is useful in agriculture for planting fruits (claimed).    ADVANTAGE - The soil matrix is rich in nutrients.    DETAILED DESCRIPTION - Soil matrix comprises 25-45 wt.% matrix and 55-75 wt.% garden soil or clay. The matrix comprises 60-80 wt.% organic matter, where the organic matter comprises 100-180 mg/kg potassium, 150-300 mg/kg nitrogen, 50-100 mg/kg phosphorus, 5-8 mg/kg copper, 10-20 mg/kg zinc, 20-40 mg/kg iron, 15-30 mg/kg manganese, 0.5-1 mg/kg boron, 3000-5000 mg/kg calcium and 300-500 mg/kg magnesium and also comprises 1-4 pts. wt. bamboo vinegar, 0.5-2 pts. wt. crystal mother liquor containing 15-25 wt.% abamectin, 4-8 pts. wt. nucleotide salt, 1-3 pts. wt. starch-acrylic graft copolymer, 15-40 pts. wt. straw rotten agent, 15-40 pts. wt. fermented human and animal excreta, 10-18 pts. wt. edible fungi residue, 3-6 pts. wt. waste bamboo sawdust, 2-5 pts. wt. plant charcoal powder, 5-10 pts. wt. sludge, 4-6 pts. wt. bone powder and 4-9 pts. wt. soybean meal. The matrix has pH of 6.5-6.8, electrical conductivity of 1.5-3.5 S and cation exchange capacity of greater than or equal to 100.
NOVELTY - Water-soluble amino acid fertilizer preparation comprises collecting neem leaves, storing, adding decomposing inoculant, and fermenting; adding water to fermented neem leaves, stirring for 0.5-2 hours, centrifuging, and collecting supernatant; adding strong acid, hydrolyzing at 40-80 degrees C for 15-22 hours to obtain amino acid mother liquor; and testing and packaging.    USE - Method for preparing water-soluble amino acid fertilizer (claimed).    ADVANTAGE - The fertilizer has insecticidal and bactericidal functions, is safe to animals, and does not leave residue on plants.
NOVELTY - A non-naturally occurring microbial organism, derived from a starting microbial organism, comprising at least one exogenous nucleic acid encoding an enzyme, or its portion, selected from ammonia lyase is new. The non-naturally occurring microbial organism has an increased resistance to biochemical stress compared to the starting microbial organism.    USE - For producing a product comprising ethanol (claimed) or other alcohols; for fermenting a carbon source obtained from a ligno-cellulosic feedstock; in the production of biochemical, such as biofuels, bio-oils, organic acids.    ADVANTAGE - The non-naturally occurring microbial organism has an increased resistance to biochemical stress compared to the starting microbial organism.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing (M1) a product involving: culturing the non-naturally occurring microbial organism in a culture medium comprising a carbon source, under conditions and for a sufficient period of time to produce the product.
NOVELTY - Manufacture of isothiazole compound (III) involves heating sulfur and a nitrile compound (I), and reacting the nitrile compound (I) and sulfur with a halogen (II).    USE - Manufacture of isothiazole compound e.g. 3,4-dichloro-5-cyanoisothiazole. Uses include but are not limited to pharmaceutical intermediate component, agrochemical intermediate component, electronic material and functional dye.    ADVANTAGE - The method enables environmentally-friendly, safe and economical manufacture of isothiazole compound with reduced waste material and without requiring aprotic polar solvent such as N,N-dimethylformamide, by a simple process.    DETAILED DESCRIPTION - Manufacture of isothiazole compound (III) involves heating sulfur and a nitrile compound of formula (I), and reacting the nitrile compound (I) and sulfur with a halogen of formula: X2 (II).    R=cyano, carboxy, or alkoxycarbonyl;and    X=chloro, fluoro, bromo, or iodo.
NOVELTY - A particulate fat-containing starting material is provided, and mixed with ethanol having concentration of 90 weight/weight%. The resulted mixture is heated, subjected to hydrocyclone treatment for forming fat reduced underflow stream and overflow stream. Then, fat-lean product is recovered from fat reduced underflow stream, and fat-rich product is recovered from overflow stream.    USE - Production of fat-rich and fat-lean product e.g. oil used in human food and animal feed product, and for producing biodiesel.    ADVANTAGE - The food grade fat-rich and fat-lean product having excellent handleability is produced at elevated pressure with high extraction rate and throughput using reduced amount of solvent without producing fire hazards by safe method.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view explaining production of fat-rich and fat-lean product.    Clarification hydrocyclone (C1,C2)    Hydrocyclone stages (Wl,W2,W3,W4,W5)
NOVELTY - Production of biodiesel involves using waste cooking oil, ethanol and magnesium silicate. The magnesium silicate absorbs pigment and residual glycerol traces in the biodiesel. The soap from the raw biodiesel is removed using ceramic filter membrane with the capillary of 0.3-2 mu m. The obtained biodiesel has purity of 99%.    USE - Production of biodiesel (claimed).    ADVANTAGE - The method enables quick, economical and environmentally-friendly production of biodiesel having high purity.
NOVELTY - Hard carbon produced by carbonizing tropical plants having high density and biomass, is claimed.    USE - The hard carbon is useful for lithium secondary battery (claimed).    ADVANTAGE - The hard carbon has excellent initial efficiency and high capacity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing hard carbon, comprising (S100) preparing charcoal from the tropical plants, (S200) crushing obtained charcoal, (S300) acid treating the crushed charcoal material, (S400) heat treating the acid treated charcoal material in presence of inert gas, (S500) surface modifying the heat treated charcoal material by coating with pyrolytic carbon, and (S600) heat treating the surface modified charcoal material in presence of vacuum.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the method for producing hard carbon (Drawing includes non-English language text).    Charcoal preparing step (S100)    Charcoal crushing step (S200)    Acid treating step (S300)    Heat treating step (S400)    Surface modifying step (S500)
NOVELTY - An apparatus for the production of biogas and a liquid fertilizer, comprises two zones arranged in series in a closed tank and is called hybrid anaerobic tank.    USE - The apparatus and the method are useful for the production of biogas and a liquid fertilizer (claimed).    ADVANTAGE - The apparatus and the method have the advantages of high biogas production, hydraulic residence time is short, and easy to operate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for generating biogas and liquid fertilizer which involves 4 stages including anaerobic microbial breeding, anaerobic microbial acclimatization, start-up of anaerobic tank, and operation of biogas and liquid fertilizer.
NOVELTY - A bacterial bioremediator indigen for reducing organic pollutants from pineapple liquid waste, comprises: Acinetobacter baumanni, Bacillus subtilis and Pseudomonas pseudomallei.    USE - For reducing organic pollutants from pineapple liquid waste (claimed).    ADVANTAGE - The bacterial bioremediator indigen has the effective time of reducing Biochemical Oxygen Demand (BOD) is 10 days, the effective time of reducing Chemical Oxygen Demand (COD) is 10 day, and the effective time od reducing Total Suspended Solid (TSS) was 9 days.
NOVELTY - Municipal domestic garbage and low-hot value coal catalyst are added, and the resulting mixture is added into roller, rotary-extrusion process is carried out, and crushed. The resulting mixture is mixed uniformly, and heated. After completing the reaction, low-hot value-coal product is removed, condensed in biological film absorbing water tank, and heavy metal lead, cadmium, mercury and arsenic are detected. 100-600 ppm Oxygen is added at normal temperature, and heavy metal lead, cadmium, mercury and arsenic are removed, to obtain smokeless coal catalyst.    USE - Synthesis of municipal domestic garbage low-hot value smokeless coal catalyst (claimed).    ADVANTAGE - The method provides municipal domestic garbage low-hot value smokeless coal catalyst without odor. Heavy metal, and food waste discharged from municipal domestic garbage is no longer landfill.    DETAILED DESCRIPTION - Municipal domestic garbage is classified as plastic package, food waste, animal manure, plant straw, paper fiber, construction waste, sludge, sediment, metal, glass, discarded electronic material, used batteries, food residue, and animal residue. Municipal domestic garbage and 10-27% low-hot value coal catalyst are added into hopper, and the resulting mixture is added into roller at normal temperature and normal pressure, rotary-extrusion process is carried out, and crushed to 10-60 meshes. The resulting mixture is introduced into stainless steel mixer, mixed uniformly, and heated at room temperature of 300 degrees C. After completing the reaction, low-hot value-coal product is removed, condensed in biological film absorbing water tank, and heavy metal lead, cadmium, mercury and arsenic are detected. 100-600 ppm Oxygen is added at normal temperature, and heavy metal lead, cadmium, mercury and arsenic are removed, to obtain smokeless coal catalyst.
NOVELTY - Biological fertilizer formulation comprises non-symbiotic nitrogen (N2) fixation bacteria Bacillus subtilis and Pseudomonas mendocina producing growth hormone IAA on test basis of 30.6-82.3 ppm, bacteria solvents phosphorus (P) and potassium (K), Flexus bacillus, and fungi Aspergillus niger for stabilizing soil aggregates.    USE - Biological fertilizer formulation.    ADVANTAGE - The fertilizer is simple and fast, with semi-aseptic methods capable of producing products free of contaminants, and utilizes easy to obtain raw materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the biological fertilizer formulation.
NOVELTY - Producing solid fuel using biomass material comprises injecting biomass raw materials including cellulose, hemicellulose and lignin in a closed panel carbonization chamber, performing semi-carbonization step to dry the biomass raw material at room temperature of 240-260 degrees C for 20-40 minutes, mixing the additives and semi-carbonized biomass raw material, and performing molding of semi-carbonized biomass raw materials and additive mixture to obtain a molded body.    USE - The method is useful for producing solid fuel using biomass material (claimed), where the fuel is useful for a boiler.    ADVANTAGE - The method ensures efficient production of solid fuel with high combustion value, improved durability and less biomass odor. The solid fuel is easy to store and handle.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a solid fuel, having a bulk density of 810-850 kg/m3, a heating value of 5300-5500 cal/g and a compression strength of 355-370 kg/cm2, obtained by the method.
NOVELTY - One method for restaurant and kitchen rubbish processing special hydrolysis acidification device composed of a tank body as the main body, wherein the lower side tank body's's said hydrolysis acidification device's bottom is provided with the slag discharging pipe and feeding pipe, the side of the tank body is provided with one's discharge pipe, tank body connecting with one's right circular of vertebra, positive cone upper table surface is provided with one of positive and negative pressure protecting device through the positive conical upper centre of the lower end face is provided with one vertical shaft's inside the tank body, orderly connecting stirring paddle vertical shaft breaking and floating slag, in turn connecting the speed reducer and variable-frequency motor outside the vertical shaft bottom's body inside the tank body's uniformly distributed vertical, vertical up welding with a heating pipe coil, the heating coil is connected with hot water inlet pipe and hot water outlet pipe. The utility model is simple in structure, adding the slag breaking system and discharging system at the bottom to ensure the hydrolysis acidification reactor for kitchen waste process operation's stability, using the heating system and improves the operation efficiency's hydrolysis acidification reactor for kitchen waste.
NOVELTY - The system has a main structure in which phenol-contained waste water is added. The phenol-contained waste water is processed under specific illumination condition. The mixed solution of micro-biodegradable agent and light catalyst is filled in main structure. The micro biodegradable agent is phanerochete chrysosporium. A light catalyst is provided with ferric oxide (Fe3O4) nanoparticles.    USE - Biological united photo-catalytic composite degradation liquid system used in degradation of phenol waste water application.    ADVANTAGE - The structure of the biological united photo-catalytic composite degradation liquid system is simplified, so that the cost reduction can be achieved. The operation of the system is carried out conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view representing the removal rate of the phenol's histogram. (Drawing includes non-English language text)
NOVELTY - The device has a coagulation reaction tank (9) whose outlet is connected to inlet of filter cloth and filtering tank (10). The outlet of ABR reactor (4), UBF reaction tank (5) and combined air floatation tank (6) are connected with the inlet of sludge concentration tank (13) whose outlet is connected to sludge dewatering machine (14). The outlet of ABR reactor and UBF reaction tank are connected with marsh gas desulfurization and burning system (16). The sump (3), ABR reactor, UBF reaction tank and combined air floatation tank are connected to tail gas outlet of tail gas system (12).    USE - High fat and oil food processing wastewater treatment device.    ADVANTAGE - The oil index reaches the standard, and the subsequent A/O biochemical processing load can be reduced. The wastewater is processed and the water quality can reach the national sewage comprehensive discharge standard. The odor produced in the wastewater processing system is greatly reduced, to ensure the quality of the surrounding air.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the High fat and oil food processing wastewater treatment device. (Drawing includes non-English language text)    Sump (3)    ABR reactor (4)    UBF reaction tank (5)    Combined air floatation tank (6)    Coagulation reaction tank (9)    Filter cloth and filtering tank (10)    Tail gas system (12)    Sludge concentration tank (13)    Sludge dewatering machine (14)    Marsh gas desulfurization and burning system (16)
NOVELTY - An efficient oil degrading bacteria Bacillus UC13, preserved in microorganism center in the China, having preservation number of CGMCC No: 7818, is new.    USE - As oil-degrading bacteria for degrading oil use in industrial refining, kitchen garbage, petroleum hydrocarbon processing, where the oil is vegetable oil including peanut oil, animal oil or mineral oil; and as fermenting agent in fermentation culture medium (claimed).    ADVANTAGE - The degrading bacteria Bacillus UC13 is prepared using simple method, and provides high activity's biological surfactant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fermentation culture medium comprising Bacillus UC13 as biological surfactant and peanut oil as unique carbon source in the mediums.
NOVELTY - Preparing ethanol fuel comprises inoculating beer yeast, Candida, Rhizopus and Bacillus subtilis into potato dextrose agar inclined plane culture medium, inoculating Bacillus subtilis into beef extract peptone culture medium, primary sorting kitchen rubbish and then placing into a crushed machine, fermenting, sealing, sterilizing and cooling, adding Rhizopus spore suspension to kitchen waste, then adding Bacillus suspension to kitchen waste and processing and adding inoculated beer yeast and Candida and fermenting.    USE - The method is useful for preparing ethanol fuel (claimed).    ADVANTAGE - The method produces ethanol fuel in an eco-friendly manner.    DETAILED DESCRIPTION - Preparing ethanol fuel comprises determining whether the ferment bacteria are beer yeast, Candida, Rhizopus and Bacillus subtilis, then respectively inoculating into potato dextrose agar inclined plane culture medium at 28-30 degrees C for 5-7 days to prepare spore suspension having a spore concentration of 107/ml, inoculating Bacillus subtilis into inclined surface of beef extract peptone culture medium at 28 degrees C for 1 day, to prepare bacteria suspension having a bacterial concentration of 107/ml, primary sorting kitchen rubbish and then placing into a crushed machine to obtain a slurry stored in the refrigerator at 4 degrees C, fermenting the raw material into a reaction container, gauze sealing, sterilizing at 121 degrees C for 30 minutes and cooling, adding 5 ml of Rhizopus spore suspension to 100 g of kitchen waste, processing at 28 degrees C for 4 days, then adding 10 ml of Bacillus suspension to 100 g of kitchen waste, processing at 28 degrees C for 1 day and adding water to saccharified liquid kitchen rubbish solution, until the moisture content is 32.86-59.36%, and adding 1-20% of inoculated beer yeast and Candida with a ratio of 1:1 and fermenting at a temperature of 30 degrees C.
NOVELTY - Denitrification reactor is filled by immobilized particle cubes of volume 27 mm3, where inner side of bottom of the reactor is seted with a blending device. The immobilized particles and water are fully mixed by blending device, the top of the reactor is provided with a grid to prevent immobilized particles and water leakage and to maintain number of immobilized particles to a fixed value. The immobilized particle cubes are filled into the reactor. Dosing pumps are connected to the reactor via feed inlet pump.    USE - Denitrification reactor used for treating sewage.    ADVANTAGE - The denitrification reactor has high nitrogen removal efficiency, and does not require backwashing.    DETAILED DESCRIPTION - Denitrification reactor is filled by immobilized particle cubes of volume 27 mm3, where inner side of bottom of the reactor is seted with a blending device. The immobilized particles and water are fully mixed by blending device, the top of the reactor is provided with a grid to prevent immobilized particles and water leakage and to maintain number of immobilized particles to a fixed value. The immobilized particle cubes are filled into the reactor. Dosing pumps are connected to the reactor via feed inlet pump. Preparing immobilized particles involve dissolving pre-polymer of polyethylene glycol and accelerator tetramethylethylenediamine in water to obtain a solution. The obtained solution is mixed with enrichment culture denitrifying sludge. Polymerization process is carried out with the obtained material after addition of initiator i.e. potassium persulphate to obtain solid gel. The obtained solid gel is cut into cubes of volume 27 mm3, where 100 ml of obtained cubes contains polyethylene glycol (10 g), accelerator (0.5 g), initiator (0.25 g) and enrichment culture denitrifying sludge (0.4 g).
NOVELTY - The biogas reactor has gas pipe (5) which is provided in reaction tank (11), and is connected with air storage tank (8). An exhaust port (6) is provided at upper side wall of air storage tank. The hot water buffer (14) connected with water pump (13) has temperature sensor (2) connected with temperature controller (3) which is connected to reaction tank. The water pump is connected with reaction tank through heating pipe (12).    USE - Solar heated biogas reactor for recycling of industrial and agricultural wastes.    ADVANTAGE - The fermentation reaction efficiency of the reactor is improved, while maintaining the temperature in the fermenting tank in constant state, so that the stable yield of reactor is ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solar heated biogas reactor.    Temperature sensor (2)    Temperature controller (3)    Gas pipe (5)    Exhaust port (6)    Air storage tank (8)    Reaction tank (11)    Heating pipe (12)    Water pump (13)    Hot water buffer (14)
NOVELTY - Co-culture method of anaerobic methane oxidation and denitrification anammox mixed microbial system, involves (a) pre-co-culturing enriched denitrifying anaerobic methane oxidation (DAMO) and ANAMMOX microflora, and (b) adding pre-microbial inoculum into co-culture system of microorganisms into liquid paraffin, adding to reactor, and adding nitrate, methane and ammonia to obtain high activity of mixed DAMO and ANAMMOX.    USE - The co-culture method is useful for anaerobic methane oxidation and denitrification anammox mixed microbial system (claimed).    ADVANTAGE - The method is cost-effective and environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) sewage processing agent comprising the mixed microbial system; and    (2) method for processing sewage, involves using the sewage processing agent.
NOVELTY - Acetic acid and butyric acid are extracted by pretreating kitchen garbage to obtain liquid residue, fermenting under anaerobic condition, adjusting pH value to less than or equal to 3, distilling, cooling, extracting, concentrating, and fractionating.    USE - Method for extraction of acetic acid and butyric acid (claimed).    ADVANTAGE - The extraction method is comprehensive and uses cheap raw materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of method for extraction of acetic acid and butyric acid from kitchen garbage. (Drawing includes non-English language text).
NOVELTY - The utility model claims a garbage processing field, specifically relates to one kind of organic anaerobic fermentation device for urban solid waste device. Comprising a feeding unit, a feeding tube, a feeding pump, a reverse back mixed mixing tank and anaerobic reactor, and output port's anaerobic reactor is cone-shaped. Operation is simple, the reliability is high, specific's tapered bottom anaerobic reactor, it can continuously and stably, which ensures higher's biological fuel gas yield, mechanical stirring way, practical and reliable, the cost is saved, the anaerobic reactor has no mechanical stirring device, such as stirrer, but the external pump taking back the material taking mixing and stirring, simple maintenance, greatly reduces the landfill garbage amount, saves the garbage landfill's occupation of land resource.
NOVELTY - This utility model claims one kind of kang stove hot smoke channel is connected marsh gas tank, belonging to the cold region season with low temperature heating auxiliary fermentation device. Feeding, comprising a tank body, a hot smoke channel, chimney, and discharging, wherein the marsh gas tank and the kang stove connecting system is connected with the kang stove flue gas waste heat is connected to the fermenting material liquid taking warming and heat-preserving to realize the stable's fermentation system, high efficiency. Building U-shaped hot smoke channel (6) on the tank body (3); hot smoke channel feeding the set at one side near the smoke inlet hole (4), the outlet flue is set 8 and the upper is connected with chimney 11, tank bottom of a feeding along the hot smoke channel wall between to the discharge. The utility model realizes the maximization's kang connecting stove system using flue gas waste heat, increasing heat preservation effect is good, hot smoke channel outer wall is rough, has good effect, brick channel time cross protruding the brick wall, and breaking function, U-shaped hot smoke channel's arrangement increases the flow path's from biogas slurry, it's good stirring to realize the main fermentation tank inlet and outlet material flows.
NOVELTY - The utility model claims one for refuse landfill's gas collecting system comprises a plurality of horizontal direction distributed's high density polyethylene perforated pipe and marsh gas collecting main pipe arranged in the vertical direction and pipe laying groove's stack body is excavated on the garbage landfill, marsh gas collecting main pipe and is connected to the bottom of the garbage landfill pile body is covered with high density polyethylene geomembrane, marsh gas collecting pipe passes through the geomembrane and the biogas utilization device's outside. The utility model's technique process is simple, the investment is small, the marsh gas collecting effect is good, the maintenance operation is simple and convenient.
NOVELTY - Producing natural fertilizer using rock phosphate and microorganisms, involves (a) crushing rock phosphate, (b) milling rice bran, (c) fermenting milled rice bran using microorganism, (d) drying fermented product using hot air, (e) mixing crushed rock phosphate and dried fermented product, and performing secondary fermentation of mixture, (f) rapidly freezing secondary fermentation product, and freeze-drying the mixture, and (g) wrapping freeze-dried product in polypropylene under vacuum condition.    USE - The method is useful for producing natural fertilizer using rock phosphate and microorganism.    ADVANTAGE - The method prepares fertilizer with excellent solubility.    DETAILED DESCRIPTION - Method for producing natural fertilizer using rock phosphate and microorganisms, involves (a) crushing 40 wt.% rock phosphate into particles of size less than 100-200 meshes, (b) milling 1.5-2.5 wt.% rice bran into particles of size 80-120 meshes, (c) fermenting milled rice bran using microorganism at 30 degrees C for 5-10 days, (d) drying fermented product at 35-45 degrees C for 20-48 hours until moisture content becomes 35-45% using hot air, (e) mixing crushed rock phosphate and dried fermented product, and performing secondary fermentation of mixture, (f) rapidly freezing secondary fermentation product at -30 degrees C to -60 degrees C for 30-60 minutes under vacuum, and freeze-drying the mixture, and (g) wrapping freeze-dried product in polypropylene under vacuum condition.
NOVELTY - Preparing 2-imino-thiazolidin-4-one compounds (I), comprises intramolecular cyclization thiourea compounds (IV) in the presence of chloroacetic acid and water at a temperature of 60-70 degrees C for 30 minutes.    USE - The process is useful for preparing (I) having antihypertensive, anti-inflammatory, antitumor, anti-alzheimer and antidepressant activities. No biological data given.    ADVANTAGE - The fast, one-pot and green process simply prepares (I) with high yield and purity in an economically and environment-friendly manner.    DETAILED DESCRIPTION - Preparing 2-imino-thiazolidin-4-one compounds of formula (I), comprises intramolecular cyclization thiourea compounds of formula (IV) in the presence of chloroacetic acid and water at a temperature of 60-70 degrees C for 30 minutes.    R1 = alkyl, aryl (both optionally substituted), or H;    R2 = five membered heteroaryl group of formula (a), or six membered aryl group of formula (b);    R1a = H, 5-NO2, 4-CH3 and/or 5-CH3;    R1b = H, 2-Cl, 3-CF3, 4-OCH3 or 4-F; and    X = S or NH.
NOVELTY - 1-(Mercaptomethyl)-cyclopropane acetic acid benzhydryl piperazine salt (II) is new.    USE - (II) is useful as intermediate for preparing (IV), montelukast or its alkali salts, preferably montelukast sodium (all claimed) for prophylaxis and chronic treatment of asthma, and reliving symptoms of seasonal allergic rhinitis and perennial allergic rhinitis in adults and pediatric patients. No biological data given.    ADVANTAGE - (II) is thermodynamically stable, and feasibly prepares (IV), the montelukast or its alkali salts, and the montelukast sodium with good physicochemical properties, reproducibility, better yield and purity in a simple, easy, convenient, cost effective and environmental friendly manner.    DETAILED DESCRIPTION - 1-(Mercaptomethyl)-cyclopropane acetic acid benzhydryl piperazine salt of formula (II), is new.    R, R1, R2 = H, halo including F, Cl, Br or I, 1-6C-alkyl, 1-6C-alkoxy, CH2F, CHF2, or CF3.    N.B. R, R1 and R2 are disclosed. INDEPENDENT CLAIMS are included for:    (1) preparation of (II);    (2) preparation of montelukast benzhydryl piperazine salt compound of formula (IV), comprising condensing (II) with methanesulfonic acid (S)-1-(3-((E)-2-(7-chloro-quinolin-2-yl)-vinyl)-phenyl)-3-(2-(1-hydroxy-1-methyl-ethyl)-phenyl)-propyl ester (III) in the presence of base and solvent; and    (3) preparation of montelukast or its alkali salt, comprising condensing (III) with 1-(mercaptomethyl)-cyclopropane acetic acid methyl ester (VII) in the presence of base, the solvent and phase transfer catalyst, and isolating montelukast or its alkali salt.
NOVELTY - Preparing biological fulvic acid from kitchen waste fermented substance comprises (i) adding water to the kitchen waste fermented product, adjusting pH using 1% sodium hydroxide solution, decocting and extracting to obtain filtrate; (ii) adjusting pH using dilute hydrochloric acid, allowing to stand, centrifuging, precipitating using acid and collecting supernatant; (iii) loading into the ion exchange resin column, collecting eluate by eluting using pure water at a specific flow speed until there is no fulvic acid; and (iv) combining the eluates, concentrating and drying.    USE - The method is useful for preparing biological fulvic acid from kitchen waste fermented substance (claimed).    ADVANTAGE - The method is simple and produces product with high purity.    DETAILED DESCRIPTION - Preparing biological fulvic acid from kitchen waste fermented substance comprises (i) adding specific amount of water to the kitchen waste fermented product, adjusting pH using 1% sodium hydroxide solution, decocting and extracting, collecting filtrate, adding specific amount of water to the filter residue, decocting and extracting, collecting the filtrate and combining the two filtrates; (ii) adjusting pH using dilute hydrochloric acid, allowing to stand, centrifuging, precipitating using acid and collecting supernatant; (iii) loading into the ion exchange resin column, collecting eluate by eluting using pure water at a specific flow speed until there is no fulvic acid; and (iv) combining the eluates, concentrating and drying.
NOVELTY - The method involves paving a bottom layer culture medium. Earthworms are inoculated in the bottom layer culture medium. An agricultural layer is paved in an upper layer culture medium. A layer of fresh farm product is paved after completing earthworm digestion process. The farm products layer is digested by a butterfly boat. The culture medium is directly collected from a cattle and naturally stacking cow.    USE - Earthworm digestion function based ecological farm product market rubbish processing method.    ADVANTAGE - The method enables processing farm products market rubbish via high efficient active microorganism containing ecological organic fertilizer and high quality humic acid liquid fertilizer, simplifying operation process and improving processing efficiency without need to install an addtional deodorizing device so as to save processing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating an earthworm digestion function based ecological farm product market rubbish processing method.
NOVELTY - Preparation method for fermented bed for pig, involves mixing grass and plant corn straw, crushing mixed material into 10-20 meshes sieve, adding leavening agent A to the mixture, fermenting mixture, turning mixture to obtain fermented liquid (A), adding fermentation agent B, adding rice flour, fermenting mixture to obtain fermented liquid (B), mixing to obtain fermented liquids (A) and (B), adding trehalose and sorbitol, stirring mixture, cooling mixture, freezing, heating, and vacuum freeze-drying mixture.    USE - The method is useful for preparing fermented bed for pig (claimed).    ADVANTAGE - The prepared fermented bed enables to prevent dysentery and promote digestion.    DETAILED DESCRIPTION - Preparation method for fermented bed for pig, involves mixing grass and plant corn straw in a weight ratio of 1:2, crushing mixed material into 10-20 meshes sieve, adding 0.002-0.004 wt.% leavening agent A to the mixture in a weight ratio of 1:1.5-2.5, fermenting mixture at 40-50 degrees C for 4-6 days, turning mixture for 2-3 days once to obtain fermented liquid (A), adding 0.001-0.003 wt.% fermentation agent B, adding rice flour, fermenting mixture at 10-20 degrees C for 5-7 days after fermentation is complete to obtain fermented liquid (B), mixing to obtain fermented liquids (A) and (B) in a ratio of 1:1-2, adding 3-5 wt.% trehalose and 2-3 wt.% sorbitol, stirring mixture for 15-20 minutes, cooling mixture at 1-2 degrees C/minutes, freezing mixture for 1-2 hours, heating mixture at 10-15 Pa and 30-35 degrees C for 10-15 hours, and vacuum freeze-drying mixture at 20-30 degrees C until the moisture content is 1-3%.
NOVELTY - Manufacturing fertilizing and pesticidal organic fertilizer comprises crushing waste tobacco powder to obtain 60-80 meshes. Sheep manure and mushroom compost are added. Bacteria are added to the material in a ratio of 1:80-120. The mixed material is stacked for 5-10 days for fermentation. Mixed material turning is performed 3-5 times to obtain fermented material. The fermented material is uniformly mixed with dry tobacco powder. Material mixing process is performed after drying a granular or powdered organic fertilizer.    USE - Method for manufacturing fertilizing and pesticidal organic fertilizer.    ADVANTAGE - The method enables effectively manufacturing fertilizer and reducing producing cost and production difficulties.
NOVELTY - Liquid fertilizer composition comprises bacterial liquid, which is produced by using fermentation. The liquid fertilizer composition comprises (in wt.%): yeast liquid waste (40-60), starch (0.1-0.135), sucrose (0.35-0.45), peptone (0.35-0.45), soybean meal (0.7-0.9), potassium dihydrogen phosphate (0.21-0.27) and water.    USE - Liquid fertilizer composition used for crops.    ADVANTAGE - The liquid fertilizer composition ensures rapid onset of action.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing liquid fertilizer composition, which involves:    (A) preparing fermentation culture medium through fermentation device by using (in wt.%): yeast liquid waste, starch, sucrose, peptone, soybean meal, potassium dihydrogen phosphate in respective ratios with water;    (B) mixing inorganic nutrient with water in a steam mixer uniformly, and then cooling to obtain cooled product;    (C) mixing cooled product with yeast waste liquid (10-40) and bacteria (1-3) to obtain product, and then uniformly stirring the product to obtain microbial bacterial liquid; and    (D) mixing microbial bacterial liquid with inorganic nutrient solution, and then cooling to obtain the desired product.
NOVELTY - Fertilizer composition comprises (in wt.%): phosphogypsum (3-30), microbial composition (1-10), water (less than 35) and nutrient (greter than 6), where nutrient comprises nitrogen, phosphorus pentoxide and potassium oxide. Microbial composition is prepared by adsorbing inoculums of Bacillus megaterium and Thiobacillus thiooxidans in fermentation medium, and then mixing obtained microbial inoculums.    USE - Fertilizer composition.    ADVANTAGE - The fertilizer composition is eco-friendly and solves problem of waste disposals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer composition, which involves:    (A) crushing phosphogypsum into powder;    (B) adsorbing Bacillus megaterium and Thiobacillus thiooxidans separately in fermentation medium, then mixing obtained microbial inoculums, and then crushing to obtain microbial composition;    (C) mixing obtained phosphogypsum and microbial composition in mass ratio of 3-30:1-10; and    (D) adding nutrient (nitrogen, phosphorus pentoxide and potassium oxide) to obtained mixture to obtain desired product.
NOVELTY - Manufacturing fertilizer involves selecting normal gas producing biogas slurry. The dry Albizzia julibrissin straw and biogas are fermented in tank containing potassium dihydrogen phosphate, bacteria and multibranched fiber at 35-45 degrees C for 30 days. Aspergillus flavus and urea is added into tank without supplying oxygen and then fermented at 45-50 degrees C for 3 days, 73 degrees C 3-5 days and 40-45 degrees C for 6-30 days. Boric acid, chromium chloride, manganese chloride and zinc sulfate is mixed at room temperature to obtain fertilizer that is bagged and packaged.    USE - Method for manufacturing fertilizer (claimed).
NOVELTY - Biological organic fertilizer preparation involves taking raw materials (wt.%): animal manure (15-20), crop straw (25-30), fly ash (15-25), rapeseed (20-25), Phellodendron leaves (3-6), biological enzyme (1-3) and organic fertilizer fermenting agent (1-3). Animal manure, crop straw, rapeseed, Phellodendron leaves and tea are crushed by using crusher. The crushed material is put into a fermentation tank. Biological enzyme, organic fertilizer fermenting agent and water are added to the fermentation tank, and then stirred for 1-15 minutes.    USE - Method for preparing biological organic fertilizer (claimed).    ADVANTAGE - The method enables to produce biological organic fertilizer that has fly ash, rapeseed meal and tea, which increase content of mineral and amino acids in fertilizer.    DETAILED DESCRIPTION - Biological organic fertilizer preparation involves taking raw materials (wt.%): animal manure (15-20), crop straw (25-30), fly ash (15-25), rapeseed (20-25), Phellodendron leaves (3-6), biological enzyme (1-3) and organic fertilizer fermenting agent (1-3). Animal manure, crop straw, rapeseed, Phellodendron leaves and tea are crushed by using crusher. The crushed material is put into a fermentation tank. Biological enzyme, organic fertilizer fermenting agent and water are added to the fermentation tank, and then stirred for 1-15 minutes. The fermentation tank is then sealed, where the product is fermented for 8-100 hours. Tea is added to the fermenting tank and sealed it, where the product is fermented at 65-75 degrees C. Fermentation tank is opened after 20-30 days and fly ash is added to the tank. The obtained fermented product is kept at cool place and dried to moisture content of 8%. The obtained product is granulated by using pelletizer to obtain biological organic fertilizer.
NOVELTY - Nutrition substrate comprises inorganic fertilizer, perlite and vermiculite, where perlite and vermiculite are present in amount of 1-10 parts and 20-40 parts, respectively.    USE - Nutrition substrate used for vegetable seedling, particularly cucumber, watermelon, melon, tomato, hot pepper and broccoli (claimed), and used in breeding and production of vegetable for research purpose.    ADVANTAGE - The nutrition substrate is simple, eco-friendly, easy to carry and suitable for large-scale industrialization.
NOVELTY - Preparing varenicline intermediate comprises reacting oxidation reaction of 1,4-dihydro-1,4-methano-naphthalene and 1,2,3,4-tetrahydro-1,4-methano-naphthalene-2,3-diol in the presence of oxidizing agent including osmium salt or hydrate and solvent including water, 1-6C alcohol solvent, ketone solvent, ether solvent and nitrile solvent. The volume ratio of water and organic solvent is 1:0.1:9.    USE - The method is useful for preparing varenicline intermediate (claimed).    ADVANTAGE - The method is capable of simply and economically preparing the varenicline intermediate in an eco-friendly manner with high purity of more than 99% and yield.
NOVELTY - Preparing 2-(4-(4-chlorophenyl)cyclohexyl)-3-hydroxy-naphthalene-1,4-dione (I) comprises reacting naphthalen-1-ol (VII) with 4-(4-chlorophenyl)cyclohexanol (VI) and solvent to obtain 2-(4-(4-chlorophenyl)cyclohexyl)naphthalen-1-ol (V), carrying out oxidation reaction of (V) to obtain 2-(4-(4-chlorophenyl)cyclohexyl)naphthalene-1,4-dione (IV), carrying out bromine reaction of (IV) to obtain 2,3-dibromo-2-(4-(4-chlorophenyl)cyclohexyl)tetralin-1,4-dione (III), and carrying out bromine elimination of (III) to obtain 2-bromo-3-(4-(4-chlorophenyl)cyclohexyl)naphthalene-1,4-dione (II).    USE - The method is useful for preparing (I) (claimed).    ADVANTAGE - The method is capable of preparing (I) in a simple manner without pollution.    DETAILED DESCRIPTION - Preparing 2-(4-(4-chlorophenyl)cyclohexyl)-3-hydroxy-naphthalene-1,4-dione of formula (I) comprises (1) reacting naphthalen-1-ol (VII) with 4-(4-chlorophenyl)cyclohexanol (VI) in the presence of catalyst to obtain 2-(4-(4-chlorophenyl)cyclohexyl)naphthalen-1-ol (V), (2) carrying out oxidation reaction of (V) using solvent and catalyst at 120-150 degrees C to obtain 2-(4-(4-chlorophenyl)cyclohexyl)naphthalene-1,4-dione (IV), (3) carrying out bromine reaction of (IV) at 60-90 degrees C to obtain 2,3-dibromo-2-(4-(4-chlorophenyl)cyclohexyl)tetralin-1,4-dione (III), (4) carrying out bromine elimination of (III) at 60-90 degrees C to obtain 2-bromo-3-(4-(4-chlorophenyl)cyclohexyl)naphthalene-1,4-dione (II) and (5) carrying out hydroxyl reaction using alcohol in the presence of base.
NOVELTY - Preparing star anise acid comprises oxidizing anise camphor with hydrogen peroxide solution in the presence of alkaline solution.    USE - The star anise acid is useful in medicine, food and cosmetic industry.    ADVANTAGE - The method is capable of preparing star anise acid with high purity, simple operation, mild reaction condition, reduced toxic and harmful solvent residue in an eco-friendly and cost-effective manner.
NOVELTY - Synthesizing 3-nitro methyl salicylate comprises adding methyl salicylate, stirring with concentrated sulfuric acid and heating, cooling, mixing with nitric- and sulfuric-acid solution, stirring and reacting, pouring into water, adjusting pH, filtering and drying to obtain 3-nitro-5-methyl salicylate, adding the sulfuric acid solution, heating to reflux, stirring, cooling and filtering to obtain 3-nitrosalicylic acid crude product, dissolving in methanol solution, dropping sulfuric acid, heating to reflux, stirring, cooling, filtering, and drying.    USE - The method is useful for synthesizing 3-nitro methyl salicylate (claimed).    ADVANTAGE - The method is capable of synthesizing 3-nitro methyl salicylate with high yield, economic benefit in an eco-friendly manner.    DETAILED DESCRIPTION - Synthesizing 3-nitro methyl salicylate comprises (1) adding methyl salicylate as raw material, stirring with concentrated sulfuric acid and heating the stirred solution, (2) cooling the heated solution, mixing with nitric- and sulfuric-acid solution, stirring and reacting, pouring the reaction solution into a water, adjusting the pH value, filtering and drying the filter cake to obtain 3-nitro-5-methyl salicylate, (3) adding the 3-nitro-5-methyl salicylate into the sulfuric acid solution, heating to reflux, stirring, cooling and filtering to obtain 3-nitrosalicylic acid crude product, (4) dissolving the 3-nitrosalicylic acid crude product in methanol solution, dropping sulfuric acid, heating to reflux, stirring, cooling, filtering, and drying.
NOVELTY - Preparing 2,6-dibromo-4-(trifluoromethoxy) aniline, comprises adding water, metal bromide and ammonium sulfate in a reaction bottle, stirring to dissolve, adding solvent into 4-tri-fluorin methoxyl group benzene amine, stirring for 30 minutes, dripping 30% of hydrogen peroxide at 20-50 degrees C, refluxing and reacting at 40-85 degrees C for 0.5-3 hours, cooling to room temperature, adding reducing agent, stirring for 30 minutes, standing to divide into layers, drying the organic phase and removing water phase. The metal bromide is sodium bromide or potassium bromide.    USE - The 2,6-dibromo-4-(trifluoromethoxy) aniline is useful for preparing thifluzamide as pesticide or bactericide.    ADVANTAGE - The method is capable of preparing 2,6-dibromo-4-(trifluoromethoxy) aniline with corrosion phenomenon, in an eco-friendly manner.
NOVELTY - Preparation of roflumilast particles, involves: 1) dissolving the roflumilast in mixed solvent of ketone and alcohol to prepare solution; 2) reverse adding the solution of step 1) into water to separate desired particle size of roflumilast; where the ketone is one or two of straight-chain or branched chain ketone having less than 6 carbon atoms; the alcohol is one or two of straight-chain or branched-chain fatty alcohol; a volume ratio of the ketone and alcohol is 1:1-20.    USE - For preparation of roflumilast particles (claimed) useful as phosphodiesterase 4 (PDE4) inhibitor, for treating chronic obstructive pulmonary disease.    ADVANTAGE - The method compared with the traditional method, provides high yield, which can reach more than 90%; has low production cost; prepares the product using conventional device and non-polluting solvents; does not pollute the environment; and avoids the mechanical grinding dust and noise pollution.
NOVELTY - Preparation of puerarin, involves: adding root of kudzu vine raw material into container, adding n-butanol solvent in container, extracting three times, first time by adding n-butanol 5-9 times as amount of raw material, heating to 35 to -100 degrees C, extracting for 4.5-8 hours, second time by adding n-butanol 3-5 times as amount of raw material, extracting for 2.5-4 hours, each time separating extraction liquid, concentrating combined extraction liquid after three times leaching, recycling n-butyl alcohol to obtain paste extract, then acid crystallizing, re-crystallizing to obtain puerarin.    USE - For preparation of puerarin (claimed).    ADVANTAGE - The puerarin prepared by this method has a high content of active ingredients, and less impurities. The preparation method provides less environmental pollution; is less health hazardous to the operator; and has low production cost, and short cycle.    DETAILED DESCRIPTION - Preparation of puerarin, involves: adding root of kudzu vine raw material into container, adding n-butanol solvent in the container, taking three times, first time leaching by adding n-butanol 5-9 times as amount of raw material, heating to 35 to -100 degrees C, extracting for 4.5-8 hours, second time leaching by adding n-butanol 3-5 times as amount of raw material, extracting for 2.5-4 hours, each time separating extraction liquid after leaching, after finishing leaching, concentrating combined extraction liquid after three times leaching, recycling n-butyl alcohol to obtain paste extract, then acid crystallizing, re-crystallizing to obtain puerarin.
NOVELTY - 1-(ferrocenyl)ethanol is synthesized by mixing aqueous methanol solution and acetyl ferrocene, adding sodium borohydride, reacting at - 5-5 degrees C, removing solvent, concentrating, adding aqueous ammonium chloride solution to remove excess sodium borohydride, adding dichloromethane to extract water layer, and removing solvent from organic layer.    USE - Synthesis of 1-(ferrocenyl)ethanol for herbicides.    ADVANTAGE - The process improves reaction speed, reduces complexity of reaction, improves product yield, and reduces wastewater discharge, energy production, and production costs.
NOVELTY - An erbium-doped tungstate upconversion luminescent material is prepared by weighing magnesium ion-containing compound, lanthanum ion-containing compound, ytterbium ion-containing compound, erbium ion-containing compound, and tungsten ion-containing compound, grinding, mixing, pelletizing to obtain flaky preform, pre-sintering preform in air atmosphere for 1-2 times, sintering at 300-700 degrees C for 1-12 hours, naturally cooling, grinding, mixing, pelletizing to obtain sheet, calcining in air atmosphere at 700-1300 degrees C for 2-15 hours, naturally cooling to room temperature, grinding, and mixing.    USE - Preparation of erbium-doped tungstate upconversion luminescent material for anti-fake label, fluorescent label, and biological molecule 3-dimensional display (all claimed).    ADVANTAGE - Process is simple and environment-friendly, and has low cost raw materials. Luminescent material has stable structural performance and good purity.    DETAILED DESCRIPTION - An erbium-doped tungstate upconversion luminescent material of formula MgLa2-2(x+y)Er2xYb2y(WO4)4 is prepared by weighing magnesium ion (Mg2+)-containing compound, lanthanum ion (La3+)-containing compound, ytterbium ion (Yb3+)-containing compound, erbium ion (Er3+)-containing compound, and tungsten ion (W6+)-containing compound, grinding, mixing, pelletizing to obtain flaky preform, pre-sintering preform in air atmosphere for 1-2 times at 300-700 degrees C for 1-12 hours, naturally cooling, grinding, mixing, pelletizing to obtain sheet, calcining in air atmosphere at 700-1300 degrees C for 2-15 hours, naturally cooling to room temperature, grinding, and mixing to obtain powder in which x is mole percent of doped Er3+.    x=0.0001-0.4;    y=0.1-0.9; and    x+y=0.09-0.9.    DESCRIPTION OF DRAWING(S) - The drawing shows an emission spectrum of erbium-doped tungstate upconversion luminescent material at wavelength of 975 nm and intensity of 2.24 W. (Drawing includes non-English language text).
NOVELTY - Soil bacterial Bacillus liquid, is claimed. The soil bacterium Bacillus liquid is produced by the fermentation of Bacillus edaphicus in a fermentation device by using a fermentation culture medium comprising 40-60 wt.% yeast waste liquid, 1.4-1.8 wt.% silkworm pupa powder, 1.4-1.8 wt.% peptone, 0.35-0.45 wt.% gelatinized corn powder, 0.21-0.27 wt.% sodium chloride, 0.14-0.18 wt.% potassium dihydrogen phosphate, 0.07-0.09 wt.% magnesium sulfate and water.    USE - The fertilizer is useful as a foliar spray on plants (claimed).    ADVANTAGE - The soil bacterial Bacillus liquid can improve the utilization rate of the fertilizer by reducing the amount of fertilizer used, and saves the production cost. The fertilizer has combined effect of foliar fertilizer and microbial fertilizer, not only has rapid onset effect, but also rapid replenishing effect of crops growth period by providing the required nutrient elements.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (I) a liquid microbial foliar fertilizer comprising 15-30 wt.% soil bacterial Bacillus liquid, 0.5-1 wt.% surfactant, 1-15 wt.% protective agent, and an inorganic nutrient and water (suitable amount), where the inorganic nutrient has total nutrient content of nitrogen, phosphorus pentoxide and potassium oxide in an amount of greater than or equal to 4%; and (II) producing liquid microbial foliar fertilizer, comprising (i) preparing the fermentation culture medium, (ii) fermenting Bacillus edaphicus in fermentation device by using the fermentation culture medium, to obtain the soil bacterial Bacillus liquid, (iii) uniformly mixing inorganic nutrient with water in a steam mixer, and cooling, (iv) uniformly stirring by adding 15-30% protective agent into the soil bacterial Bacillus liquid, and then adding inorganic nutrients, and (v) completely dissolving the surfactant, and uniformly mixing, to obtain the product.
NOVELTY - An absorbing liquid contains hindered amine, alcohol amine, N-dimethylacetamide, and salt catalyst with de-ionized water in which concentration of alcohol amine is 15-40 wt.%, concentration of hindered amine is 10-60 wt.%, hindered amine is non-linear alcohol with sterically hindered amine compound structure with nitrogen atom, concentration of N-dimethylacetamide is 5-30 wt.%, and concentration of salt catalyst is 0.1-5 wt.%.    USE - An absorbing liquid for removing sulfur compound and carbon dioxide from natural gas component (all claimed).    ADVANTAGE - Product is low-cost and has high desulfurizing rate, low energy consumption, and good stability.
NOVELTY - A pig waste fermentation bed composting method involves fermenting bed pad material and collecting waste, mixing the waste pad material and straw and adding calcium cyanamide, paving one layer of straw at the bottom then paving one layer of waste pad material mixture, spraying on the waste pad material mixture proper amount of lime water by mud cover and waiting for 10 days.    USE - As pig waste fermentation bed composting method (claimed).    ADVANTAGE - The method allows fermentation at good fermenting speed, causes no pollution, has high insect ovum and weed seed killing rate, has improved compost product recovery, and has important popularization value in modern agriculture field.
NOVELTY - A fertilizer for improving outer cover of sugar kiwi fruit, comprise: 40 pts.wt. of bran cake fertilizer, 50 pts.wt. of sucrose and trace element fertilizer.    USE - As fertilizer for improving outer cover of sugar kiwi fruit (claimed).    ADVANTAGE - The fertilizer increases 5-6% of bright color, provides sugar kiwi fruit with good mouth feel and more nutrition, and improves selling price.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing the fertilizer involves: preparing trace element fertilizer by mixing zinc fertilizer, magnesium fertilizer, iron fertilizer and calcium fertilizer with ratio of 1:1:1:1; measuring and weighing each component; crushing the cake fertilizer and frying to becomes golden yellow; and then mixing each component, stirring uniformly and cleaning using water; fermenting at 30 degrees C; and packaging the product.
NOVELTY - Producing fertilizer for tobacco, involves: using raw material including: 30-32 wt.% pig manure, 21-23 wt.% dairy manure, 8 wt.% peanut cake, 6 wt.% rape seed cake, 3 wt.% plant ash, 5 wt.% lees, 10 wt.% canola straw, 1 wt.% organic fertilizer fermenting agent, 10 wt.% urea, 0.5 wt.% monoammonium phosphate, 2.5 wt.% of potassium sulfate, 0.2 wt.% of amino acid chelate manganese, 0.5 wt.% amino acid chelated boron, 0.1 wt.% humic acid chelate zinc, and 0.2 wt.% humic acid zinc amino acid chelate.    USE - For producing fertilizer for tobacco (claimed).    ADVANTAGE - The fertilizer production process is simple, provides fertilizer with stable and durable nutrient efficacy.    DETAILED DESCRIPTION - A fertilizer for tobacco, comprises raw material including: 30-32 wt.% pig manure, 21-23 wt.% dairy manure, 8 wt.% peanut cake, 6 wt.% rape seed cake, 3 wt.% plant ash, 5 wt.% lees, 10 wt.% canola straw, 1 wt.% organic fertilizer fermenting agent, 10 wt.% urea, 0.5 wt.% monoammonium phosphate, 2.5 wt.% of potassium sulfate, 0.2 wt.% of amino acid chelate manganese, 0.5 wt.% amino acid chelated boron, 0.1 wt.% humic acid chelate zinc, and 0.2 wt.% humic acid zinc amino acid chelate; where the fertilizer is produce by: (1) crushing and mixing the pig manure, dairy manure, peanut cake, rape seed cake, plant ash, lees and canola straw; and adding the organic fertilizer fermenting agent and water, and fermenting in summer for at 35-40 days and in winter for 65-70 days to obtain organic fertilizer; and (2) crushing urea, monoammonium phosphate, potassium sulfate, amino acid chelate manganese, amino acid chelated boron, humic acid chelate zinc, and humic acid zinc amino acid chelate into powder; mixing the powder with the organic fertilizer to obtain the finished product.
NOVELTY - Composite microbial fertilizer comprises 30-50 pts. wt. beer residue, 30-80 pts. wt. calcium hydrophosphate, 5-30 pts. wt. cassava dregs and 1-5 pts. wt. honey.    USE - The fertilizer is useful in the fertilization of grains, vegetables, fruits and various crops (claimed); and improving soil structure, and loose soil; increasing soil permeability; and promoting growth in crops.    ADVANTAGE - The fertilizer meets the national ministry of agriculture and NY/T798-2004 standards (claimed), and coverts waste into useful substance, reduces environment pollution, and has improved efficiency. The method has low production cost, and simple production procedure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the fertilizer, comprising (i) taking all the above mentioned raw materials; (ii) mixing beer residue wit honey, and fermenting for 5 days under sealed conditions; and (iii) compactly filling the mixture, and fermenting at 45 degrees C for 7 days under sealed conditions.
NOVELTY - American ginseng special organic fertilizer comprises fully fermented including 150-300 parts by weight (pts. wt.) straw of livestock and poultry excrement, 1-2 pts. Wt. fertilizer of ginseng, mixing them uniformly, where the American ginseng fertilizer, according to weight proportion: 5.5-7.5 of ammonium sulfate, 15-20 pts. Wt. urea, 17-21 pts. wt. agricultural ammonium nitrate, 1-2 pts. wt. monoammonium phosphate, 3-5 pts. wt. calcium superphosphate, 20-30 pts. wt. potassium chloride, 2-3 pts. wt. nitro humic acid, 8-12 pts. wt. amino acid.    USE - As American ginseng special organic fertilizer (claimed).    ADVANTAGE - The organic fertilizer ginseng improves the soil environment, improves soil fertility, increases production and product quality ginseng cultivation purposes, and has important significance.    DETAILED DESCRIPTION - American ginseng special organic fertilizer comprises fully fermented including 150-300 parts by weight (pts. wt.) straw of livestock and poultry excrement, 1-2 pts. wt. fertilizer of ginseng, mixing them uniformly, where the American ginseng formula fertilizer, according to weight proportion:5.5-7.5 of ammonium sulfate, 15-20 pts. wt. urea, 17-21 pts. wt. agricultural ammonium nitrate, 1-2 pts. wt. monoammonium phosphate, 3-5 pts. wt. calcium superphosphate, 20-30 pts. wt. potassium chloride, 2-3 pts. wt. nitro humic acid, 8-12 pts. wt. amino acid, where the production process is as follows: firstly comprises a manure straw at a temperature of more than 60 degrees C to ferment for 7-10 days, the fermentation process in turning for three times, then adding American ginseng formula fertilizer rear fully fermented, mixing rear taking granulating and packaging the finished product.
NOVELTY - A fertilizer comprises raw material of 68-70% pig manure, 1% organic fertilizer fermenting agent, 9-11% urea, 6% monoammonium phosphate, 6% potassium chloride, 4% ammonium hydroxide, 0.5% zinc-iron composite soil conditioner, 1% fertilizer powder, 0.5% root stimulating agent, 0.3% amino acid chelated boron, 0.4% amino acid chelated calcium, 0.3% humic acid chelate magnesium, 0.5% slow release agent, and 0.5% synergistic agent.    USE - As fertilizer useful for the production of cotton (claimed).    ADVANTAGE - The fertilizer can adjust permeability and moisture retention of soil, increase cotton drought, cold, cropping of abiligy, promote ecological balance, quickly develop the cotton seedling, improve immunity of cotton and increase the yield and quality of cotton, and also greatly improve the rate of cotton.    DETAILED DESCRIPTION - A fertilizer comprises raw material components: 68-70% pig manure, 1% organic fertilizer fermenting agent, 9-11% urea, 6% monoammonium phosphate, 6% potassium chloride, 4% ammonium hydroxide, 0.5% zinc-iron composite soil conditioner, 1% fertilizer powder, 0.5% root stimulating agent, 0.3% amino acid chelated boron, 0.4% amino acid chelated calcium, 0.3% humic acid chelate magnesium, 0.5% slow release agent, and 0.5% synergistic agent. The preparation of fertilizer, involves: (1) adding organic fertilizer fermenting agent, pig manure in a prescription amount to water, sealing in plastic film, fermenting in summer for 30-35 days and in winter for 60-65 days to prepare product; and (2) Putting urea, mono-ammonium phosphate, potassium chloride, potassium hydroxide, zinc-iron composite soil conditioner, fertilizer powder, root stimulating agent, zinc amino acid chelated boron, amino acid chelated calcium, humic acid chelate magnesium, slow release formulation, synergistic agent into the crusher, crushing into powder and mixing pig manure fermenting product uniformly to obtain the special fertilizer for cotton production.
NOVELTY - Indolo(2,1-b)quinazoline-6,12-dione derivative (I), is new.    USE - For treating cancer, Alzheimer's disease, autoimmune disease, depression, and anxiety.    ADVANTAGE - The compound is prepared by method which is simple, has mild reaction condition, saves solvent, reduces pollution and is convenient for industrial production.    DETAILED DESCRIPTION - Indolo(2,1-b)quinazoline-6,12-dione derivative of formula (I), is new.    R1=H or F;    R2=piperazin-1-yl, piperazine-1-carboxylic acid tert-butyl ester, piperazine, morpholine, or -NH-.    An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - Preparing honeycomb coal briquette comprises adding corn cob, livestock manure and anthracite as raw materials with additives and then uniformly mixing with water, and preparing briquette according to a conventional method.    USE - The method is useful for preparing honeycomb coal briquette (claimed).    ADVANTAGE - The method enables economical preparation of the honeycomb coal briquette with strong flames and low pollution gas emissions and without peculiar smell.
NOVELTY - Sodium hydroxide is weighed in micro amount and dissolved in methanol. The mixture is transesterified with castor oil under sealed conditions in a 300-mL reactor, while increasing the temperature and stirring. Stirring is stopped and the reaction solution is quickly water-cooled to room temperature. The reaction mixture is decompressed and rotary-evaporated at 60 degrees C for 30 minutes, and methanol is removed. The product is then layered to obtain an upper layer of fatty acid methyl ester, and lower layer of glycerol.    USE - Micro-alkali-catalytic preparation of biodiesel (claimed).    ADVANTAGE - The method reduces transesterification catalyst, which enables homogeneous elimination of catalyst during washing and drying, uses mild conditions, and is energy-saving and easy.
NOVELTY - Seedling growth additive is prepared by weighing components comprising 8-15 pts. wt. flora Escherichia coli A01, 10-20 pts. wt. sawdust, 40-55 pts. wt. dried sewage sludge, 5-10 pts. wt. gravel, 1-4 pts. wt. bamboo leaves, 0.5-2 pts. wt.; 15-25% abamectin crystallized mother liquor and 15-60 pts. wt. water, mixing weighed components with water, allowing obtained mixture to get wet, and incubating the mixture at 25-35 degrees C for 4-8 days to obtain final product.    USE - The seedling growth additive is useful for maintaining fertility of soil (claimed).    ADVANTAGE - The additive is prepared using natural raw materials, and hence is non-toxic and causes no pollution. The additive improves plant growth environment, increases efficiency of fertilizer, effectively maintains fertility of the soil and prolongs fertilization period, and hence required to be added in less quantity.
NOVELTY - Method for preparing culture additive for maintaining soil fertility, involves weighing 8-15 pts. wt. Escherichia coli strain A01, 10-20 pts. wt. sawdust, 40-55 pts. wt. dry sewage sludge, and 5-10 pts. wt. processed deciduous leaves, adding 15-60 pts. wt. water to the above-mentioned components for wetting the components, and maintaining the temperature at 25-35 degrees C for 4-8 days to obtain product.    USE - The method is useful for preparing culture additive for maintaining soil fertility (claimed).    ADVANTAGE - The method prepares culture additive which is nontoxic. The culture additive causes no pollution, improves plant growth environment, increases efficiency of fertilizer, and prolongs fertilizer effect for a long period of time.
NOVELTY - Long-acting compound fertilizer is prepared by using 15-20 wt.% crop straw, 5-10 wt.% amino acid, 6-10 wt.% chitin, 5-10 wt.% chicken manure, 6-10 wt.% ammonium sulfate, 10-18 wt.% humic acid, and plant ash (suitable quantity), mixing the crop straw, amino acid, and chitin with chicken manure, performing fermentation process, and adding raw materials (remainder), and mixing and granulating the obtained product.    USE - As long-acting compound fertilizer.    ADVANTAGE - The long-acting compound fertilizer provides nutrient elements to promote growth of crops.
NOVELTY - Organic biofertilizer comprises 3-5 wt.% Azotobacter, 5-10 wt.% diammonium phosphate, 8-12 wt.% potassium chloride, 5-15 wt.% powdered rock phosphate, 3-10 wt.% straw powder, 6-8 wt.% Bacillus mucilaginosus, 10-20 wt.% chicken manure and fly ash (remainder).    USE - As organic biofertilizer for crops.    ADVANTAGE - The biofertilizer effectively improves soil environment and soil compaction, provides maximum amount of nutrients to crops required for proper growth of crops, enriches crops, suitable for all kinds of soil including acid and alkaline soil, contains reasonable proportion of nutrient elements and increases yield of the crops.
NOVELTY - Soil matrix is formed by mixing 25-45 wt.% substrate comprising 60-80% organic substance and 55-75 wt.% garden soil or clay. The matrix comprises 1-3 wt.% nitrogen, 1.5-3.5 wt.% phosphorus, 2-4 wt.% potassium, and 0.02-0.08 wt.% magnesium, calcium, iron, manganese and boron and has pH 6.5-6.8, 1.5-3.5 S electric conductivity and more than 100 cationic exchange capacity.    USE - As soil matrix for vegetables.    ADVANTAGE - The soil matrix has 55-70% total porosity, 0.5-0.7 g/cm3 density, high nutrient content, and good odor-removing function, and is environmentally-friendly.    DETAILED DESCRIPTION - Soil matrix is formed by mixing 25-45 wt.% substrate comprising 60-80% organic substance and 55-75 wt.% garden soil or clay. The matrix comprises 1-3 wt.% nitrogen, 1.5-3.5 wt.% phosphorus, 2-4 wt.% potassium, and 0.02-0.08 wt.% magnesium, calcium, iron, manganese and boron and has pH 6.5-6.8, 1.5-3.5 S electric conductivity and more than 100 cationic exchange capacity. The organic substance comprises 1-4 pts. wt. bamboo vinegar, 0.5-2 pts. wt. 15-25% abamectin crystallization mother liquor, 1-3 pts. wt. starch-acrylic acid graft copolymer, 15-40 pts. wt. decomposed straw inoculant, 15-40 pts. wt. fermented human and animal excreta, 10-18 pts. wt. edible mushroom fungus residue, 3-6 pts. wt. waste bamboo sawdust, 2-5 pts. wt. plant-treated carbon powder, 5-10 pts. wt. silt sludge, 4-6 pts. wt. bone powder, 4-9 pts. wt. soybean meal.
NOVELTY - Soil matrix is formed by mixing 25-45 wt.% substrate comprising 60-80% organic substance and 55-75 wt.% garden soil or clay. The matrix comprises 1-3 wt.% nitrogen, 1.5-3.5 wt.% phosphorus, 2-4 wt.% potassium, and 0.02-0.08 wt.% magnesium, calcium, iron, manganese and boron and has pH 6.5-6.8, 1.5-3.5 S electric conductivity and more than 100 cationic exchange capacity.    USE - As soil matrix for leafy vegetables.    ADVANTAGE - The soil matrix has 55-70% total porosity, 0.5-0.7 g/cm3 density, high nutrient content, and good odor-removing function, and is environmentally-friendly.    DETAILED DESCRIPTION - Soil matrix is formed by mixing 25-45 wt.% substrate comprising 60-80% organic substance and 55-75 wt.% garden soil or clay. The matrix comprises 1-3 wt.% nitrogen, 1.5-3.5 wt.% phosphorus, 2-4 wt.% potassium, and 0.02-0.08 wt.% magnesium, calcium, iron, manganese and boron and has pH 6.5-6.8, 1.5-3.5 S electric conductivity and more than 100 cationic exchange capacity. The organic substance comprises 1-4 pts. wt. bamboo vinegar, 0.5-2 pts. wt. 15-25% abamectin crystallization mother liquor, 1-3 pts. wt. starch-acrylic acid graft copolymer, 15-40 pts. wt. decomposed straw inoculant, 15-40 pts. wt. fermented human and animal excreta, 10-18 pts. wt. edible mushroom fungus residue, 3-6 pts. wt. waste bamboo sawdust, 2-5 pts. wt. plant-treated carbon powder, 5-10 pts. wt. silt sludge, 4-6 pts. wt. bone powder, 4-9 pts. wt. soybean meal.
NOVELTY - Agricultural soil micro-substrate comprises substrate and soil or clay. The substrate comprises organic matter, nitrogen, phosphorus, potassium and magnesium, calcium, iron, manganese and boron. The organic matter comprises wood vinegar, 15-25% avermectin crystallization mother liquor, nucleotide salt, chitooligosaccharide, starch-acrylic graft copolymers, straw inoculants, fermented human and animal feces, edible fungi residue, waste bamboo shavings, plant charcoal, sludge residue, bone meal, and soybean meal.    USE - As agricultural soil micro-substrate.    ADVANTAGE - The agricultural soil micro-substrate is clean and environmentally-friendly, and has excellent odor removing property.    DETAILED DESCRIPTION - Agricultural soil micro-substrate comprises 25-45 wt.% substrate and 55-75 wt.% soil or clay. The substrate comprises 60-80 wt.% organic matter, 1-3 wt.% nitrogen, 1.5-3.5 wt.% phosphorus, 2-4 wt.% potassium and 0.02-0.08 wt.% magnesium, calcium, iron, manganese and boron, where pH of the substrate is 6.5-6.8, electric conductivity is 1.5-3.5S, and cation exchange capacity is greater than or equal to 100. The organic matter comprises 2-5 pts. wt. wood vinegar, 0.5-2 pts. wt. 15-25% avermectin crystallization mother liquor, 4-8 pts. wt. nucleotide salt, 3-8 pts. wt. chitooligosaccharide, 1-3 pts. wt. starch-acrylic graft copolymers, 15-40 pts. wt. straw inoculants, 15-40 pts. wt. fermented human and animal feces, 10-18 pts. wt. edible fungi residue, 3-6 pts. wt. waste bamboo shavings, 2-5 pts. wt. plant charcoal, 5-10 pts. wt. sludge residue, 4-6 pts. wt. bone meal, and 4-9 pts. wt. soybean meal.
NOVELTY - Special fertilizer comprises solid raw materials comprising 40-60 wt.% rabbit manure, 30-50 wt.% starch, 3-6 wt.% nitrogenous fertilizer, 1.5-2 wt.% phosphate fertilizer, 1.5-2 wt.% potassium fertilizer.    USE - The special fertilizer is useful for blueberry (claimed).    ADVANTAGE - The fertilizer has excellent uniformity and stability, and is prepared simply and cost-effectively using easily available raw materials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned special fertilizer, which involves (a) crushing the above-mentioned rabbit manure to 10 mm and mixing the above-mentioned straw with the crushed product in a ratio of 1-1.5:1, (b) inoculating microorganisms to the obtained mixture, where organic content of the mixture is 30-35%, moisture content of the mixture is 35-40%, and the inoculation amount is 0.001-0.01%, (c) adding the above-mentioned nitrogenous fertilizer, phosphate fertilizer, and potassium fertilizer to the obtained mixture (solid raw materials), (d) adding sucrose to the rabbit manure in a mass ratio of 1:5, adding 20 times water to the obtained product, adding 1% urea and 1.5% peptone to the product and culturing the above-mentioned mycorrhizal fungus in the product at 25 degrees C, fermenting the product for 3 days, stopping fermentation, and storing the product at 4 degrees C to obtain mycorrhizal fungal liquid, and (e) mixing the solid raw materials and the mycorrhizal fungal liquid in a mass ratio of 100:1-2.
NOVELTY - Composting poultry and livestock excrements, by stacking organic carbon source material in container, forming padding layer, inoculating bacteria, adding the excrements and organic carbon source material, forming covering layer, inoculating bacteria, composting mixture, mixing and stirring compost material including the padding layer and covering layer, adding mixed compost material to secondary fermentation tank, fermenting compost material and drying fermented material to obtain fertilizer.    USE - The method is useful for composting poultry and livestock excrements and obtaining compost used as fertilizer (claimed).    ADVANTAGE - The method is performed using simple equipments and easy to operate, enables safe disposal and effective utilization of waste livestock and poultry excrements and has high safety with respect to humans, as environmental pollution is reduced.    DETAILED DESCRIPTION - Method for composting poultry and livestock excrements, involves (a) stacking organic carbon source material in bottom portion of a container having opened top portion, forming padding layer, inoculating bacteria on the padding layer, adding the poultry and livestock excrements on upper padding layer, adding the organic carbon source material on the added excrements, forming covering layer and inoculating bacteria on the covering layer, (b) subjecting obtained mixture to first stage composting process at 65-75 degrees C, maintaining water content of the mixture at 50-60% and pH value at 6.5-7.5, and performing composting process for 360-480 hours under the above-mentioned conditions, (c) mixing and stirring obtained compost material including the padding layer and covering layer, (d) adding mixed compost material to secondary fermentation tank and fermenting the compost material for 7-10 days, and (e) drying obtained fermented material to obtain fertilizer.
NOVELTY - Preparation of culture substrate comprises crushing mature sugarcane stem, leaves, seed, or bagasse, watering, piling, fermenting, adding fine soil, where ratio of substrate to soil is 1:3-5, uniformly mixing, disinfecting, and sterilizing.    USE - Method for preparing culture substrate (claimed) used for seedlings, root system, and robust plants.    ADVANTAGE - The culture substrate supplies nutrients, has double growing effect on seedlings, and fertilizing effect, and reduces fertilizer amount to 1/3-1/2.
NOVELTY - Preparation of microsuspension (MS) bioorganic fertilizer comprises testing heavy metal content in animal manure; dehydrating until water content is reduced to 40-50%, removing fecal stones and other impurities, and ultrafine crushing to 70-80 meshes; stirring, adding MS, mixing, and soaking; piling and decomposing for 1-3 days; detecting organic matter, moisture, nutrient, and heavy metal content of fermented mixture; dry granulating, wet granulating until water content is 25-35%, condensing, sieving, and regranulating unqualified product; weighing in fertilizer bag; and storing.    USE - Method for preparing microsuspension bioorganic fertilizer (claimed) used for killing bacteria and nematodes and increasing crop growth.    ADVANTAGE - The fertilizer does not need to add microbial inoculum, protects environment, has high efficiency, and increases soil nutrient. The method has low production cost and is short.
NOVELTY - An aminated granulated fertilizer production system comprises potassium hydrogen conversion tank (1), sulfuric acid and potassium chloride reaction device, preneutralizing tank (2), reactor (3), ammoniation neutralizing device, pelleting device and tail gas processing device. The system further comprises storage tank, granulating machine, where the tail gas treatment device, venturi scrubber (6), and washing tower (7).    USE - Aminated granulated fertilizer production system.    ADVANTAGE - The system reduces tail gas discharge and saves production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer comprising introducing 98% sulfuric acid and potassium chloride into potassium hydrogen conversion tank to produce potassium bisulfate and hydrogen chloride, flowing to preneutralization overflow storage tank, adding phosphoric acid washing liquid mixed acid, transferring to reactor, reacting under 0.5 MPa ammonia gas, entering in granulating, adding auxiliary material through lifting machine, mixing and granulating, entering produced tail gas into venturi scrubber, acid washing tower and water tower.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of the aminated granulated fertilizer production system.    Potassium hydrogen conversion tank (1)    Pre-neutralizing tank (2)    Reactor (3)    Venturi scrubber (6)    Washing tower (7)
NOVELTY - Preparation of Agaricus blazei cultivation material comprises taking sawdust, lees, fish scale particle, bran, powdered phosphate rock, charcoal, weathered coal, calcium superphosphate, lime powder, ferrous sulfate, vinegar dregs, flour, montmorillonite powder, and humus, mixing with water; piling and fermenting, adjusting water content, filling in bags, and sterilizing.    USE - Method for preparing Agaricus blazei cultivation material (claimed).    ADVANTAGE - The cultivation material is simple, has high nutrient content and promotes high growth rate of Agaricus blazei.    DETAILED DESCRIPTION - Preparation of Agaricus blazei cultivation material comprises taking 30-40 pts. wt. sawdust, 10-20 pts. wt. lees, 5-8 pts. wt. fish scale particle, 20-30 pts. wt. bran, 2.5-3.5 pts. wt. powdered phosphate rock, 5-7 pts. wt. charcoal, 3-5 pts. wt. weathered coal, 1-2 pts. wt. calcium superphosphate, 4-5 pts. wt. lime powder, 1-3 pts. wt. ferrous sulfate, 10-15 pts. wt. vinegar dregs, 2-3 pts. wt. flour, 25-30 pts. wt. montmorillonite powder, and 30-40 pts. wt. humus, mixing with water at a ratio of 1:2.5-3.0; piling and fermenting for 20-30 days, adjusting water content to 40-50%, filling 650-800 g per bag, and sterilizing at 110-120 degrees C for 5-6 hours.
NOVELTY - Fruit and vegetable special compound fertilizer comprises 35-40 pts. wt. rotten chicken manure, 40-45 pts. wt. decomposed clover, 5-8 pts. wt. urea, 5-8 pts. wt. diamine, 2-3 pts. wt. alpha -naphthylacetic acid, and 3-5 pts. wt. potash fertilizer.    USE - The special compound fertilizer is useful for fruit and vegetable (claimed).    ADVANTAGE - The special compound fertilizer is cost-effective, and rich in necessary growth element including calcium, phosphorus, sodium, chlorine, magnesium, sulfur, iron, copper and zinc, prevents hardening of soil, promotes absorption of crops, and improves soil granule structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the special compound fertilizer which involves drying rotten chicken manure until the water content is 50-70%, adding composting agent to the dried chicken manure, uniformly mixing the mixture, and performing fermentation for 10-15 days, where the ratio of the chicken and composting agent is 1:10000 kg, and the composting agent is prepared by using rice chaff, drying the fermented mixture until the water content is 10-15%, and sieving and removing impurity, and adding the other raw materials, fermenting the mixture for 7 days, and drying, crushing, granulating, sieving, and packing the obtained product.
NOVELTY - Culture material for Stropharia mushroom comprises raw materials comprising 55-65 wt.% sugarcane leaves, 15-25 wt.% cottonseed hulls, 10 wt.% pond mud, 6 wt.% wheat bran, 2 wt.% lime powder, and 2 wt.% gypsum powder, where the ratio of raw materials is 100%.    USE - The culture material is useful for Stropharia mushroom (claimed).    ADVANTAGE - The culture material provides good absorption, high yield and biological efficiency of 110.3-125.6%, and promotes growth of mushroom mycelium.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the culture material, which involves pre-wetting sugarcane, cutting into 2-3 cm, spraying lime water, stacking for 2 days, drying, crushing, uniformly mixing materials, placing sugarcane with thickness of 15-20 cm, adding pond mud, sealing, stacking, turning mixture with interval time of 6, 5, 4, 3 or 2 days, turning for 4 times for 20 days, adding gypsum powder, cotton seed hull and bran, adding water, and fermenting mixture until the water content is 63-65%.
NOVELTY - Preparing 1,3-diamino guanidine hydrochloride, comprises dissolving sodium thiocyanate material in water and then adding dimethyl sulfate, heating the reaction mixture at a room temperature for 5-6 hours, collecting water and oil layers from the reaction mixture, mixing hydrazine hydrochloride and water to the reaction mixture and then heating to a temperature of 30-40 degrees C, adding methyl thiocyanate to the heated mixture, heating the reaction mixture for 5-10 degrees C for 4-5 hours, filtering, and washing with cold water to obtain desired product as a white solid.    USE - The method is useful for preparing 1,3-diamino guanidine hydrochloride (claimed).    ADVANTAGE - The method allows the simple and economical preparation of the 1,3-diamino guanidine hydrochloride with high yield and purity in an environmentally-friendly manner.    DETAILED DESCRIPTION - Preparing 1,3-diamino guanidine hydrochloride, comprises dissolving sodium thiocyanate material in water and then adding dimethyl sulfate, heating the reaction mixture at a room temperature for 5-6 hours, collecting water and oil layers from the reaction mixture, where a mass ratio of sodium thiocyanate and water is 1:1-1.5, and a mass ratio of sodium thiocyanate and dimethyl sulfate is 2-2.5:1, mixing hydrazine hydrochloride and water to the reaction mixture and then heating to a temperature of 30-40 degrees C, adding methyl thiocyanate to the heated mixture, heating the reaction mixture to 5-10 degrees C for 4-5 hours, filtering, and washing with cold water to obtain desired product as a white solid. The mass ratio of the hydrazine hydrochloride and the water is 1:4-5, and the mass ratio of hydrazine hydrochloride and the methyl thiocyanate is 1.9-2.1:1.
NOVELTY - Chromatographic technique involves mixing chloroform, methanol and 0.1 moles per liter hydrochloric acid solution to form mixed solvent. The obtained solvent is divided into lower layer and upper layer, where the lower layer is dissolved in serotonin derivate extract. The lower layer is considered as stationary phase and upper layer is considered as mobile phase. The obtained mixed solvent is injected into chromatographic column to obtain desired product. The obtained product is isolated and then concentrated.    USE - Chromatographic technique used for isolating serotonin derivatives (claimed).    ADVANTAGE - The method enables to prepare serotonin derivatives in an efficient, eco-friendly and a cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing serotonin derivative extract, which involves:    (A) weighing safflower seed and liquid material in a ratio of 1-5:1-20;    (B) crushing safflower seed and mixing it in liquid material to obtain a mixture;    (C) refluxing the mixture for 0.5-2 hours;    (D) extracting refluxed mixture for 1-3 times to obtain extracting;    (E) concentrating the extract until dryness;    (F) dissolving the concentrated extract with methanol to obtain solution;    (G) extracting the solution with n-hexane to obtain extract; and    (H) dissolving the extract in ethyl acetate to obtain the desired product.
NOVELTY - Producing acesulfame potassium crystal involves neutralization reaction, separating and hydrolysis reaction step, where the neutralization reaction of using the front process of water washing organic phase, into the neutralizing kettle, adding raw alkali, adjusting PH value to 9.5-10.5, standing, depositing for half an hour the rear the acesulfame honey; (2) acesulfame potassium crystal into the coarse steaming kettle, heating potassium crystal, recycling the solvent dichloromethane; (3) potassium crystal by freezing, centrifuging to obtain acesulfame potassium crystal.    USE - For producing acesulfame potassium crystal (claimed).    ADVANTAGE - Using neutralizing directly crystallizing process, simplify operation, reduces the labor intensity of the worker, and the original production process, directly crystallizing and removing the caustic soda concentration operation and simplifies the operation, reduces the labor intensity, saves water and steam.
NOVELTY - Preparing 11 beta , 17 alpha -hydroxy-1,4-prognene-3,20-dione-21-acid ester (I) comprises: (1) performing Mitsunobu reaction of 11 alpha -hydroxy-1,4-diene-16,17-epoxyprogesterone methyl ester with p-toluenesulfonic acid; (2) reacting 11 beta -toluenesulfonyl-16,17-epoxy-1,4-diene-progesterone with hydrobromic acid; (3) reacting 11 beta ,17 alpha -hydroxy-16 beta -bromo-1,4-pregnene with reducing agent; (4) reacting 11 beta , 17 alpha -dihydroxy-1,4-pregnene-3,20-dione with iodine; and (5) reacting 11 beta , 17 alpha -hydroxy-1,4-pregnene-3,20-one-21-iodine with potassium acetate in presence of an organic solvent to obtain (I).    USE - The method is useful for preparing (I).    ADVANTAGE - The method avoids the tedious job strain selection, and is capable of simply preparing (I) with high yield and without environmental pollution.    DETAILED DESCRIPTION - Preparing 11 beta , 17 alpha -hydroxy-1,4-prognene-3,20-dione-21-acid ester (I) comprises: (1) performing Mitsunobu reaction of 11 alpha -hydroxy-1,4-diene-16,17-epoxyprogesterone methyl ester with p-toluenesulfonic acid in the presence of an organic solvent and a catalyst to obtain 11 beta -toluenesulfonyl-16,17-epoxy-1,4-diene-progesterone (a); (2) reacting (a) with hydrobromic acid to obtain 11 beta ,17 alpha -hydroxy-16 beta -bromo-1,4-pregnene (b); (3) reacting (b) with a reducing agent in the presence of a catalyst to obtain 11 beta , 17 alpha -dihydroxy-1,4-pregnene-3,20-dione (c); (4) reacting (c) with iodine in the presence of organic solvent to obtain 11 beta , 17 alpha -hydroxy-1,4-pregnene-3,20-one-21-iodine (d); and (5) reacting (d) with potassium acetate in presence of an organic solvent to obtain (I).
NOVELTY - Preparing fluticasone propionate particles with particle size D98 of less than 5 mu m, comprises dissolving fluticasone propionate in a solvent to form a solution, mixing the solution with an anti-solvent to precipitate a desired particle size of fluticasone propionate. The anti-solvent is a mixture of a surfactant and water. The mass ratio of surfactant to water is 0.01-1:500. The solvent includes dimethyl sulfoxide, N,N-dimethylformamide and/or polyethylene glycol. The surfactant is anionic surfactant, cationic surfactant, zwitterionic surfactant or nonionic surfactant.    USE - The method is useful for preparing fluticasone propionate particles (claimed), which is useful for preventing and treating rhinitis or asthma.    ADVANTAGE - The method is capable of simply and economically preparing fluticasone propionate particles with high yield, small granularity, narrow granularity distribution, high sphericity, good liquidity and reduced energy consumption and toxicity and without using a special device in an environmentally-friendly manner.
NOVELTY - Preparing 9,11 beta-epoxy steroid compounds (I), comprises reacting (2-((10S,13S,17R)-16-R1-17-hydroxy-10,13-dimethyl-3-oxo-7,8,12,14,15,16-hexahydro-6H-cyclopenta(a)phenanthren-17-yl)-2-oxo-ethyl) R2formate (I) with halogenating agent in a solvent in the presence of perchloric acid to a give ((9S,10S,11S,13S,17R)-16-R1-17-(2-R2carbonyloxyacetyl)-17-hydroxy-10,13-dimethyl-3-oxo-11-R3oxy-6,7,8,11,12,14,15,16-octahydrocyclopenta(a)phenanthren-9-yl) (II), and reacting (II) with a strong base, methylene chloride and methanol under heating at 45-65 degrees C for 20-30 times.    USE - The method is useful for preparing (I) (claimed).    ADVANTAGE - The method allows the economical preparation of (I) in an efficient and environmentally-friendly manner.    DETAILED DESCRIPTION - Preparing 9,11 beta-epoxy steroid compounds of formula (I), comprises reacting (2-((10S,13S,17R)-16-R1-17-hydroxy-10,13-dimethyl-3-oxo-7,8,12,14,15,16-hexahydro-6H-cyclopenta(a)phenanthren-17-yl)-2-oxo-ethyl) R2formate compound of formula (I) with halogenating agent in a solvent in the presence of perchloric acid to a give ((9S,10S,11S,13S,17R)-16-R1-17-(2-R2carbonyloxyacetyl)-17-hydroxy-10,13-dimethyl-3-oxo-11-R3oxy-6,7,8,11,12,14,15,16-octahydrocyclopenta(a)phenanthren-9-yl) compound of formula (II), reacting (II) with a strong base, methylene chloride and methanol under heating at 45-65 degrees C for 20-30 times, followed by filtration and distillation at atmospheric pressure, cooling to below 5 degrees C, and drying to obtain 9,11 beta-epoxy-steroidal compounds of formula (I).    R1, R2 = H or 1-6C lower alkyl, preferably CH3; and    R3 = -COH (preferred) or -COCH3.
NOVELTY - This utility new type relates to one energy-saving device, namely one surface of bio-gas conversion device, wherein said device is of kettle by wall of upper cover, the lower bottom and the form of (1), is provided with a gas collection pipe (9), gas pipe (9) upper is provided with a valve. The beneficial effects are as follows: the coal, methane micro-organism nutrient fluid, the methane microorganism, and in a large amount of volatile substances such as coal is divided into the combustible gas to be used, and the hot value of coal and is not reduced, so as to improve the utilization rate of coal and greatly reduces the burning of coal for environment of pollution, and the device is simple, the cost is low, convenient to implement and process is controllable, it can be popularized fast speed, wide application range of coal by using new way in the breeding process.
NOVELTY - A highly stable methanol gasoline comprises: 70-89% of gasoline, 10-28% of methanol and 1-2% of additive; where the additive is dimethyl carbonate, dioctyl azelate, diethylene glycol monomethyl ether, sorbitol monooleate, lecithin, sodium petroleum sulfonate, dimethyl sulfate, fatty alcohol-polyoxyethylene ether.    USE - As gasoline (claimed) for automobile engine.    ADVANTAGE - The methanol gasoline can be prepared using low manufacturing cost, shows high stability and can be stored more than two years and will not delaminate; promotes the fuel burn fully, to save energy and reduce emission of target.
NOVELTY - Production of copper chrome arsenic (CCA) wood dangerous waste derived fuel involves carrying out pre-crushing, magnetic separation and secondary crushing of CCA wood dangerous waste to obtain 2-3 mm long wood chips; soaking wood chips in 0.1-0.2% oxalic acid solution, where the soaking time is not less than 1 day; and then drying until moisture content becomes reduced to 5-20%; and then based on the principle of stable fuel heat value, after drying the wood chips, adding into the calorific value waste organic solvent, evenly stirring, shaping by extrusion molding equipment into shaped derived fuel.    USE - For the production of copper chrome arsenic wood dangerous waste derived fuel (claimed).    ADVANTAGE - The method makes full use of the CCA wood dangerous waste having the characteristics of stable heat value, and waste oxalic acid and waste organic solvent to obtain harmless treatment; and realizes the purpose of treating waste by waste.
NOVELTY - A morel culture medium material comprises 100 kg dry feed containing 60 wt.% cottonseed hulls, 10 wt.% wheat bran, 10 wt.% 0.2-0.5 cm corn cob, 10 wt.% 0.2-0.5 cm peony root, 5 wt.% 0.2-0.5 cmrear apple tree peony, 1 wt.% glucose, 2 wt.% gypsum, and 2 wt.% calcium carbonate.    USE - Morel culture medium material.    ADVANTAGE - The method timely diffuses water immersion which provides clean water to morsel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cultivation of morel by:    (A) building arch shed with 7 m roof span and 2.5 m high, and digging ground at 3 m width, 5 m long, and 20 cm deep; adding with loose soil, leveling, layering with 1 cm thick ash and 5 cm thick sand, and irrigating until water is submerged into sand at 1 cm deep for 7 days; and feeding and inoculating while keeping level of surface and water, stopping irrigation after 5 days, and covering with plastic when water naturally decreases;    (B) preparing culture medium material by crushing corn cob, apple tree branches, and peony root, mixing with glucose, gypsum, and calcium carbonate, bagging into polyethylene bag, sealing, and sterilizing; and    (C) cultivating fruiting body in late February, spraying 1 L/m2 every 2-3 days when weather is dry, culturing for 13 days until part of sclerotia starts to mature, and soaking in 300-600 ml saline water while maintaining culture medium and water temperature to 10-22 degrees C to form fruiting body for 5 days; and harvesting after 4-6 days.
NOVELTY - Controlling plant diseases and insect pests of fruit tree branches comprises crushing fresh seaweed, adding to 5-9 times water, stirring, adding 2-5 wt.% alkali substance, stirring once every 30 minutes for 1-2 hours; and filtering, collecting filtrate, coating into branches of fruit trees, and spraying with 2-5 wt.% calcium chloride aqueous solution biological protective film.    USE - Method for controlling plant diseases and insect pests of fruit tree branches (claimed).    ADVANTAGE - The method is environment-friendly, prevents rainwater erosion, prolongs drug residence time on branches, turns waste into treasure, and has good control effect on dried apples rot, ring rot and spider mites.
NOVELTY - A water emulsion insecticidal composition comprises cypermethrin and nitenpyram at weight ratio of 1:5-1:20.    USE - Water emulsion insecticidal composition used for preventing and treating vegetable, fruit tree, and melon crop from insects, particularly Trialeurodes vaporariorum, aphid, Psylla chinensis, leafhopper, and thrips, preferably melon thrips, onion thrips, rice thrips, and western flower thrips (all claimed).    ADVANTAGE - The composition is environment-friendly, relieves drug resistance of pests, reduces dosage of agrochemicals, and has best crop protection effect.
NOVELTY - The system has a control unit controlling cooling of synthetic gas generated by gasification reaction of biogas with pulverized coal. A fuel inlet supplies pulverized coal to a coal gasifier unit. The control unit supplies biogas to the fuel inlet. An agent refusal part is connected with the gasifier unit to remove slag. A refrigerator is connected with the gasifier unit to cool generated synthetic gas, and maintains temperature of the synthetic gas at 200-300 degree Celsius. Another agent refusal part is connected with the refrigerator to remove the fly ash.    USE - Coal gasifier system.    ADVANTAGE - The system allows supply of biogas to the gasifier unit in an improved manner, so that synthetic gas with low temperature can be easily generated.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a synthetic gas production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an coal gasifier system.'(Drawing includes non-English language text)'
NOVELTY - Extracting carbohydrates from biomass comprises preparing the biomass for extraction of carbohydrates; forming a first biomass solution comprising the prepared biomass, water, and acid or an alkali; and subjecting the first biomass solution to a first hydrodynamic cavitation treatment, where acid or alkali hydrolysis of the biomass occurs.    USE - The methods are used for extracting carbohydrates from biomass, and for creating bioalcohol from carbohydrates extracted from biomass (all claimed).    ADVANTAGE - Methods to carry out heterogeneous reactions that do not require a large amount of energy input, and avoid potentially dangerous, high-pressure operation are provided. The method of producing alcohol from biomass is improved, more efficient and more cost effective. The method simply requires a minimum input fluid velocity and pressure to create cavitation in the flow towards the goal of creating new products.    DETAILED DESCRIPTION - Extracting carbohydrates from biomass comprises preparing the biomass for extraction of carbohydrates; forming a first biomass solution comprising the prepared biomass, water, and acid or an alkali; subjecting the first biomass solution to a first hydrodynamic cavitation treatment, where acid or alkali hydrolysis of the biomass occurs; filtering the first biomass solution into a first filtrate and an intermediate biomass, where the first filtrate contains extracted carbohydrates; creating a second biomass solution comprising the intermediate biomass, water and an enzyme source; exposing the second biomass solution to a second hydrodynamic cavitation treatment, where enzymatic hydrolysis of the biomass occurs; and filtering the second biomass solution into a second filtrate and a filtered biomass, where the second filtrate contains extracted carbohydrates. An INDEPENDENT CLAIM is a process for creating bioalcohol from carbohydrates extracted from biomass according to the method above.
NOVELTY - The gasifier has a reaction chamber (3) that is divided into an upper portion (3a) and a lower exhaustion portion (3b) that is provided with a mobile grid (21) for withdrawing charcoal and supporting a solid bed. The reaction chamber is provided with first upper end equipped with opening (5) for introducing substances to be gasified inside the chamber internally equipped with a rotary stirring shaft (13). The shaft is equipped with openings (15) for delivering comburent fluid pre-heated at a temperature sufficient to guarantee triggering oxidation reactions, inside chamber.    USE - Continuous-type gasifier of downdraft type for biomasses and urban and industrial wastes.    ADVANTAGE - The adequate temperature is kept for guaranteeing the cracking of gas and of tars produced by the pyrolysis which cross axial area of the reaction chamber. The gasifier guarantees the complete exhaustion of the carbon residual due to eso-thermal combustion reactions, reaching, in the hottest bed areas, temperatures much greater than 1000 degrees C.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of the gasifier.    Reaction chamber (3)    Upper portion (3a)    Lower exhaustion portion (3b)    Opening (5)    Shaft (13)    Openings (15)    Mobile grid (21)
NOVELTY - Yeast microorganism comprising a pyruvate utilizing biosynthetic pathway, reduced pyruvate decarboxylase (PDC) activity and modified adenylate cyclase activity, is new.    USE - The microorganism is useful for producing a fermentation product that is 3-6C alcohol that is propanol, butanol, pentanol or hexanol, where the produced alcohol is useful in a bio-based fuel (all claimed).    ADVANTAGE - The microorganism has an increased biomass yield as compared to a corresponding microorganism that does not have modified adenylate cyclase activity, where carbon flow through the pyruvate utilizing pathway is not reduced compared to a corresponding microorganism that does not have modified adenylate cyclase activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing a fermentation product from pyruvate comprising providing the microorganism and growing the microorganism under conditions where the fermentation product is produced from pyruvate.
NOVELTY - Generating energy involves co-firing in a reactor an engineered fuel feedstock, comprising at least two sorbents and at least two components derived from municipal solid waste (MSW), and at least one fossil fuel, where the emission of at least one pollutant is less than the emission of the pollutant, when the fossil fuel is fired in the absence of the engineered fuel feedstock feed stock.    USE - The method is useful for generating energy, preferably electricity or steam (all claimed).    ADVANTAGE - The method is capable of efficiently and easily generating energy in an economical and cost-effective manner.    DETAILED DESCRIPTION - An INDPENDENT CLAIM is included for a method-I of making an engineered fuel feedstock, comprising processing plastic, a sodium-based sorbent, and a calcium-based sorbent to form a plastic-sorbent composition, and processing the plastic-sorbent composition with fiber to form a fiber-plastic-sorbent-composition.
NOVELTY - A biocoke (5) manufacturing apparatus comprises reaction tube (1) which has heating unit (6) in outer peripheral part and makes biomass feedstock react by heating and under-pressurization, cooling pipe (2) which has cooling unit (7) in greater than or equal to 1 part of outer peripheral part and cools biomass reaction product after reaction, and receiving pressure part (4) which receives an applied pressure during pressurization in which exit of the cooling pipe (3) is opened and is spacing apart from receiving pressure part.    USE - An apparatus for manufacturing biocoke (claimed).    ADVANTAGE - Installation cost is reduced. Apparatus is easy to convey.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biocoke (5) manufacturing process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biocoke manufacturing apparatus. (Drawing includes non-English language text).    Reaction tube (1)    Cooling pipe (2)    Exit of the cooling pipe (3)    Receiving pressure part (4)    Biocoke (5)    Heating unit (6)    Cooling unit (7)    Heat insulation material (8)    Material input part (9)    Flange of reaction tube (10)
NOVELTY - A to-be-processed water containing chemical oxygen demand component and ammonia is introduced to biological treatment tank accommodating activated sludge having bacteria capable of decomposing chemical oxygen demand component, biologically treated and processed. The number of ammonium oxidizing bacteria in activated sludge accommodated in the biological treatment tank is 1x 107 (cells/mL-MLSS) or more.    USE - Processing of water discharged during carbonization in coke oven.    ADVANTAGE - The quality of water is effectively improved by processing method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing apparatus of to-be-processed water (100).    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of processing apparatus of to-be-processed water. (Drawing includes non-English language text)    Processing apparatus (100)    Denitrifying tank (111)    Nitrification tank (112)    Oxygen supply unit (130)    Sedimentation tank (150)
NOVELTY - A container (10) consisting of an inner wall face containing iron alloy is prepared. A gas containing oxygen is then introduced into the container, and the inside of the container is maintained under reduced pressure. Ethylene gas and hydrogen gas are filled into the container, to obtain combustible gas.    USE - Manufacture of combustible gas (claimed).    ADVANTAGE - The ethanization of the ethylene in the combustible gas containing ethylene and hydrogen is suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of manufacturing equipment of combustible gas.    Container (10)    Container valve (12)    Piping system (20)    Non-return valve (31)    Pressure gauge (51)
NOVELTY - Preparing a humin fertilizer, comprises performing a hydrothermal carbonization of biomass, preferably sewage sludge (1), which is obtained from a filtrate of a carbonization product, and packing or filling into a closed container.    USE - The method is useful for preparing a humin fertilizer (claimed). No biological data given.    ADVANTAGE - The method is capable of energy-efficiently and economically preparing the humin fertilizer with less effort in an environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for performing the method.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a device for performing the method.    Sewage sludge (1)    Sulfuric acid (3)    Coal Slurry (4)    Solid fuel (6)    Washer. (13)
NOVELTY - The pot has a chemical tank (6) that accommodates hydrogen-producing agent (5) comprised in lower layer of container main portion (1), and reacts with water and generates hydrogen. A gas channel (4) is provided with non return valve (3). A discharge opening portion (7) is comprised to the upper layer of container main portion. A cover portion (9) is detachably externally equipped to discharge opening portion. The cover portion is provided to reduce pressure inside of container main portion before removing from discharge opening portion.    USE - Pot for portable hydrogen water generator for generating water used as drinking water, coffee, black tea, or green tea.    ADVANTAGE - Since the chemical tank is comprised to the inner surface of lower cover detachably screwed together in the lower upper layer of container main portion, the insertion into chemical tank of hydrogen-producing agent can be performed by very simple operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the pot for portable hydrogen water generator.    Container main portion (1)    Non return valve (3)    Gas channel (4)    Hydrogen-producing agent (5)    Chemical tank (6)    Discharge opening portion (7)    Cover portion (9)
NOVELTY - The hydrogen combustion domestic equipment comprises a water electrolysis unit (15) with a water inlet, an oxygen outlet and a hydrogen outlet. A power input is provided for providing electrical power to the electrolysis unit. A storage tank (10) is provided for hydrogen to accumulate hydrogen produced in the electrolysis unit with inlet and outlet hydrogen. A hydrogen burner (13) is connected to the hydrogen storage tank. The power input includes a direct current power supply input.    USE - Hydrogen combustion domestic equipment used as household cooking system or water heating system.    ADVANTAGE - The hydrogen combustion domestic equipment comprises a water electrolysis unit with a water inlet, an oxygen outlet and a hydrogen outlet, and thus precisely regulates flow and pressure of water supplied to the electrolysis unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen combustion domestic equipment.    Tank (6)    Water level sensor (7)    Storage tank (10)    Hydrogen burner (13)    Water electrolysis unit (15)
NOVELTY - Isolation of propane-1,3-diol from the post-fermentation broth, comprises extracting propane-1,3-diol with a mixture of organic solvents, where the propane-1,3-diol is isolated, after previous biomass removal from post-fermentation broth, with 2-butanone that is present in the organic solvent mixture.    USE - The method is useful for isolation of propane-1,3-diol from a post-fermentation broth (claimed), where the propane-1,3-diol is used as monomer to build polymer polytrimethylene terephthalate, which is used for the production of fibers, carpets, textiles, for sanitary and medical applications, and as a packaging and/or structural material.    ADVANTAGE - The method allows simple and economical isolation of the propane-1,3-diol from a post-fermentation broth with high purity, yield and efficiency and reduced energy consumption.
NOVELTY - Producing sewage sludge pellet comprises: mixing a polymer and sludge from a sewage treatment plant for coagulation of the polymer with the sludge; removing the residual polymer remaining after electro-osmotic decomposition dehydration of the sludge in which 5% of the moisture is absorbed into sawdust; pressing the polymer to a diameter of 10 mm and thickness of 4-6 mm into shape of pellets; irradiating far infrared ray in the pellets transferred by a conveyor; and drying the pellets.    USE - The method is useful for producing sewage sludge pellet for substitute fuel (claimed) such as petroleum or coal.    ADVANTAGE - The method is capable of conveniently removing the moisture contained in the sludge, reducing waste of energy, and enhancing drying efficiency of the sludge.    DETAILED DESCRIPTION - Producing sewage sludge pellet comprises: mixing a polymer and sludge from sewage treatment plant for coagulation of the polymer with the sewage sludge; removing the residual polymer remaining after electro-osmotic decomposition dehydration of the sludge in which 5% of the moisture is absorbed into sawdust, where the residual polymer is removed by injecting 5% of the sludge with the sawdust to regain moisture content of the sludge to 65%; pressing the polymer to a diameter of 10 mm and thickness of 4-6 mm into shape of pellets; irradiating far infrared ray in the pellets transferred by a conveyor; and drying the sludge pellets till 10% of moisture is removed using a heater. An INDEPENDENT CLAIM is included for a sewage sludge pellet produced by the method.
NOVELTY - Preparation of ioforminol (I) from 5-formylamino-2,4,6-triiodo-N,N'-dipropyl-isophthalamide derivative (II), comprises in situ hydrolysis of the protecting groups of (II), where (II) is suspended in water only.    USE - The process is useful for preparing (I) (claimed), which is useful as a contrast agent for X-ray imaging.    ADVANTAGE - The process is economical, environmentally and provides (I) with an yield of greater than 95% which is 20% higher and saves one day in production time when compared to conventional processes.    DETAILED DESCRIPTION - Preparation of ioforminol of formula (I) from 5-formylamino-2,4,6-triiodo-N,N'-dipropyl-isophthalamide derivative of formula (II), comprises in situ hydrolysis of the protecting groups of (II), where (II) is suspended in water only.    X = H, formyl or acetyl.    An INDEPENDENT CLAIM is also included for (I) prepared by the process.
NOVELTY - Producing a fatty acid methyl ester from a lipid source, involves: (a) extracting at least one lipid from a lipid source; and (b) transesterifying the lipid into a fatty acid methyl ester, where the steps (a) and (b) occur within a system comprised of a first solvent and a second solvent, and at least one catalyst.    USE - The method is useful for producing a fatty acid methyl ester from a lipid source, where the lipid source comprises biomass, preferably algae, dry biomass or wet biomass (all claimed), where the fatty acid methyl ester is useful in the production of lipid-based products, such as biodiesel.    ADVANTAGE - The method is capable of selectively transesterifying a lipid into a fatty acid methyl ester.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for producing a fatty acid methyl ester from a lipid source, comprising a reaction vessel for extracting at least one lipid from the lipid source and for transesterifying the lipid into the fatty acid methyl ester and having at least one inlet passage and at least one outlet passage, where a reaction component enters the reaction vessel through the inlet passage and exits the reaction vessel through the outlet passage.
NOVELTY - An isolated polynucleotide having at least 75% homology to SEQ ID NO: 1, sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication, is new.    USE - The isolated polynucleotide, host cells and methods are useful for obtaining triacylglycerols (TAGs) used as a biofuel or as a starting material for the production of biofuel (all claimed).    ADVANTAGE - The isolated polynucleotide, host cells and methods allow high production of TAGs, and allow using various substrates to obtain oil in E. coli in a short time.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) an isolated polypeptide which has at least 75% homology to SEQ ID NO: 2, sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication, with triacylglycerol synthase activity, encoded by the polynucleotide; (2) a vector comprising the polynucleotide; (3) host cell transformed with the vector; (4) Escherichia coli transformed with the pET29 vector comprising the polynucleotide of SEQ ID NO: 1; (5) a method for obtaining triacylglycerols (TAGs) comprising: (a) obtaining the transformed host cell; (b) culturing the transformed host cell obtained in (a) in a culture medium comprising waste or industrial waste as a carbon source; and (c) recovering TAGs accumulated in the host cell or culture medium in (b); and (6) TAGs or a fraction obtained employing the latter method, used as a biofuel or as a starting material for the production of biofuel.
NOVELTY - A method involves injecting microalgae solution containing contaminants to modular electrolytic system containing electrolytic reactor (252) with electrically connected anode and cathode to perform electrolysis of algae solution to form flocs. The anode and cathode are concentric to each other and are parallel to the flow of micro algal solution in the reactor. The turbulence is created in the solution by controlling the flow rate of micro algal solution.    USE - Method of separating, harvesting and primary dewatering microalgae biomass from microalgae solution (claimed).    ADVANTAGE - The method performs separation, harvesting and primary dewatering economically and efficiently, by an environmentally-friendly process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) system for separating, harvesting and primary dewatering of microalgae biomass; and    (2) electrolysis reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of modular skid of electrolysis reactors.    Electrolysis reactor (252)
NOVELTY - Producing butanol comprises: providing a recombinant host cell comprising a butanol biosynthetic pathway; and contacting the recombinant host cell with a fermentation medium comprising a fermentable carbon substrate, and magnesium. The butanol is produced via the engineered butanol biosynthetic pathway.    USE - The method is useful for producing butanol which is isobutanol (claimed), 1-butanol, 2-butanol or 2-butanone, where the butanol is useful as a fuel additive, a feedstock chemical in the plastics industry, or as a food-grade extractant in food and flavor industry.    ADVANTAGE - The method provides higher yields of butanol in a cost effective and environmental friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a composition comprising a recombinant host cell comprising a butanol biosynthetic pathway, a fermentable carbon substrate, and 5-200 mM magnesium.
NOVELTY - Manufacture of solid fuel involves adjusting moisture content of wood-type biomass ground material to 8-50% and increasing volume density to 0.55 g/cm3 and baking at oxygen concentration of 10% or less and temperature of 170-350 degrees C.    USE - Manufacture of solid fuel used as fuel for pulverized coal for power generation equipment e.g. boiler and incineration system.    ADVANTAGE - The method efficiently enables manufacture of solid fuel having high calorific value with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid fuel.
NOVELTY - The system (10) has a carbon layer support (32) positioned upstream of a syngas collection chamber (114), and a syngas heater (34) provided with an inlet (44) that is fixed and in fluid communication with the syngas collection chamber, where the heater is positioned in a pyrolysis reaction zone (20). A vacuum source (204) e.g. diesel engine, is positioned downstream from a reactor vessel (16), and is communicated with a syngas outlet (206). Syngas in the reactor vessel is drawn through a combustion reaction zone, the syngas collection chamber, the syngas heater and the syngas outlet.    USE - Plasma assisted gasification system for generating power by converting carbonaceous material into a charcoal, wood-oils, and tars. Uses include but are not limited to coal, biomass, biofuel, carbon dioxide, hydrogen and petroleum.    ADVANTAGE - The system includes an agitator drive assembly that prevents formation of burn channels within fuel, produces electricity from biomass by producing syngas to replace need for petroleum based fuels to engine, facilitates easy shipment over land, sea, rail, or air, and transportation of the system from manufacturing site to on-site location. The heater increases efficiency of the engine without negatively impacting a reactor vessel, and reduces contaminates in syngas without requiring extensive filtering. The system includes the reactor vessel with distinct reaction zones that facilitates greater control and a more efficient system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a plasma assisted gasification system.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a reactor vessel of a plasma assisted gasification system.    Plasma assisted gasification system (10)    Reactor vessel (16)    Pyrolysis reaction zone (20)    Carbon layer support (32)    Syngas heater (34)    Inlet (44)    Syngas collection chamber (114)    Vacuum source (204)    Syngas outlet (206)
NOVELTY - Machine composter comprises a tube processor, a geared motor, a stirrer shaft, an air injector, a vacuum gas fermenter, and a biofilter.    USE - The machine composter is useful for composting organic waste (such as straw, vegetable scraps and fruit dumped in cultivated area) into organic fertilizer or compost used in agriculture, plantations, golf courses, mine reclamation and urban parks to fertilize fish ponds.    ADVANTAGE - The machine composter economically prepares the organic fertilizer without any odor to enrich effects on plants and soil fertility in an environmental friendly manner.
NOVELTY - A bacterial bioremediator for neutralizing pH and reducing organic pollutants from pineapple liquid waste, comprises: Bacillus cereus, Acinetobacter baumanni, Bacillus subtilis and Pseudomonas pseudomallei.    USE - For neutralizing pH and reducing organic pollutants from pineapple liquid waste (claimed) for degrade the waste.    ADVANTAGE - The bacterial bioremediator has the effective time to neutralize the pH by bacterial starter is 6 days.
NOVELTY - The tool has shaped arrows which are provided with arrowheads that are larger in diameter than the rod or pipe arrows. The driving pipe is provided with trash. The tip of the arrows is provided with protective porous holes. The extraction pipe is provided with pore holes. The rocks are directly inserted into the holes.    USE - Tool for making holes in rubbish dump and garbage piles.    ADVANTAGE - The rock can be directly loaded to the layer immediately outside the pipe extraction in efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the tool for making holes in rubbish dump and garbage piles.    Cone (1)    Arrow (2)    Segment connection (3)    Plate (7)
NOVELTY - Making fiber-degrading agent (microfungi composition) with superior enzymatic activity, involves: (a) preparing sugarcane bagasse with humidity around 70%; (b) storing bagasse in an incubator at 37 degrees C; (c) isolating microfungi grown on sugarcane bagasse medium; (d) identifying isolates obtained from microfungi; (e) selecting microfungi based on enzymatic activity to degrade lignocellulose; and (f) determining the composition of the selected microfungi.    USE - The method is useful for making fiber-degrading agent used in decomposing lignocellulose (claimed).    ADVANTAGE - The method produces fiber-degrading agent with superior enzymatic activity in a short period.
NOVELTY - Preparing intermediate chemicals from the breakdown of glycerol using aqueous media under subcritical and supercritical conditions, involves forming a reactant mixture comprising glycerol and water, degassing by boiling the mixture for 2-3 minutes, introducing the mixture into a 10 ml batch reactor and then flowing nitrogen gas to maintain the reactor at a pressure of 250 bar, conducting the reaction at a temperature of 200-350 degrees C for subcritical and 400 degrees C for supercritical conditions, and immediately cooling the reactor to halt the reaction process.    USE - The process is useful for preparing intermediate chemicals such as methanol, ethanol and acetaldehyde (all claimed), which is useful in the manufacture of plastics and resins, and methanol and ethanol are useful as solvents and liquid fuels.    ADVANTAGE - The process prepares intermediate chemicals with high yield and selectivity and reduced usage of catalysts.
NOVELTY - A bio-fertilizer comprises microbial consortium of arbuskular mycorrhizal fungi (AMF) and non-symbiotic bacteria. An INDEPENDENT CLAIM is included for preparation of the bio-fertilizer involving mixing 30 g of arbuskular mycorrhizal fungi with 10 ml of non-symbiotic bacteria.    USE - As bio-fertilizers for legume crops such as soybeans, green beans, peanuts, and lentils preferably Canavalia ensiformis (L.) (claimed).    ADVANTAGE - The bio-fertilizer is environment friendly and safe; and can increase the productivity of crops.
NOVELTY - Composition of biological agents comprises Paenibacillus polymyxa BG25, Pseudomonas fluorescens PG01, and Serratia liquefaciens SG01.    USE - The composition of biological agents is useful as biological fertilizer and biological control commodity crops, and in horticulture, plantation and forestry (claimed) for promoting plant growth, and controlling disease.    ADVANTAGE - The composition improves quality and yield of crop, and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of the composition of biological agents on seeds by incorporating bio-matriconditioning seed, medium (formulation of biological agents) and water in containers in a ratio of 10:7.5:5, covering the container with a perforated plastic sheet, incubating the seeds at room temperature for 12 hours (for the seeds rather soft textured like nuts seeds, spinach, kale and fruits) or 24 hours (for hard textured seeds such as rice, maize, peppers and tomatoes) or (for the seeds are very hard textured like cashew, teak and pecan), drying the incubated seeds, and packaging and storing, or directly sown or planted in the field.
NOVELTY - Making water weed extract of Azolla pinnata comprises: cleaning and blending water weeds of Azolla pinnata weighing 1 kg and mixing with starter consisting of 3 cc M-Bio (sic) fertilizers and 5 g sugar with 1 l water and leaving for 2x 24 hours, covering weeds that have been blended with the mixed starter, with a black plastic sheet; and after 7 days, filtering the extract using a filter cloth and keeping in a bottle for ready to use.    USE - The method is useful for making water weed extract Azolla pinnata where the extract is useful as fertilizer for the growth of Spirulina platensis (all claimed). No biological data given.    ADVANTAGE - The method utilizes Azolla pinnata to provide the extract for Spirulina platensis microalgae growth medium so that it can be used as a natural food that does not harm predators (fish and shrimp larvae), with excellent growth.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) A. pinnata weed fertilizer containing a concentration of 1000 ppm in the culture medium; (2) using culture media for the growth of Spirulina platensis comprising 11% salinity brackish water with 300 g salt (1 piece box of salt) in each media volume of 10 l; and a potential aquatic weed as fertilizer for culturing microalgae production by fermentation using M-Bio (sic) comprising weed of Pistia stratiotes, A. pinnata, Eichhornia crassipes, Marsilea crenata and Salvinia molesta.
NOVELTY - The apparatus comprises an anaerobic two-phase bioreactor including an asidogenesis bioreactor unit and a methanogenesis bioreactor unit (12). Each bioreactor unit includes chambers and an outflow channel for liquid and biogas. A first chamber serves as a zone for suspended microbial growth. The second chamber is divided into first and second volumes, and serves as a zone for immobilized microbial growth. The second volume is 2 times greater than the first volume room. The bioreactor includes an aerobic microbial breeding stage.    USE - The apparatus is useful for treating wastewater (claimed).    ADVANTAGE - The apparatus exhibits compact size and high performance, and efficiently removes chemical oxygen demand from the wastewater in an environmentally friendly manner.    DETAILED DESCRIPTION - The apparatus comprises an anaerobic two-phase bioreactor including an asidogenesis bioreactor unit and a methanogenesis bioreactor unit (12). Each bioreactor unit includes chambers and an outflow channel for liquid and biogas. A first chamber serves as a zone for suspended microbial growth. The second chamber is divided into first and second volumes, and serves as a zone for immobilized microbial growth. The second volume is 2 times greater than the first volume room. The bioreactor includes an aerobic microbial breeding stage, an anaerobic microbial acclimation, asidogenesis and methanogenesis stages, start-up stage of anaerobic bioreactor and operation stage of anaerobic bioreactor for treating wastewater. The wastewater is treated at room temperature to reduce concentration of chemical oxygen to 10%, and has pH of 7 plus minus 0.2. The bioreactor is operated at hydraulic residence time of 1 day.    DESCRIPTION OF DRAWING(S) - The figures show schematic side views of anaerobic bioreactor and suspended microbial growth zone.    Methanogenesis bioreactor unit (12)    Chamber (14)    Valve (22)    Lid (26)    Baffle. (32)
NOVELTY - A chemical system for reducing C-O, C-N, and C-S bonds, comprises a mixture of at least one organosilane and at least one strong base; and optionally at least one molecular hydrogen donor compound and/or molecular hydrogen.    USE - For reductively cleaving aromatic and aliphatic C-O, C-N, and C-S bonds in organic substrate comprising a biomass (e.g. lignin, sugar), biomass liquifaction, biopyrolysis oil, black liquor, coal, coal liquifaction, natural gas, petroleum process stream (claimed); for decomposition of biomass-based feedstreams into aromatic feedstocks and fuels; and for desulfurization of sulfur-containing contaminants in crude oil streams.    ADVANTAGE - The system is free of a transition-metal compound (i.e. less than 10 ppm); is free of water and/or oxygen; reduces 40-100% C-X bonds in the substrate; activates C-O, C-N, and C-S bonds in the liquid phase, without the necessary presence of transition metal catalysts, UV radiation or electrical discharges; and produces only environmentally benign silicates as the byproduct and avoids toxic metal waste streams.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for reducing C-X bonds comprising C-O, C-N, and C-S bonds in a an organic substrate, involving contacting a quantity of the substrate comprising at least one C-O, C-N, or C-S bond with the chemical system.
NOVELTY - An alkyl ethoxylate sulfate (AES) electrostatic demisting liquid is prepared by electrostatically demisting AES sulfonated tail gas, dissolving in water, adding pH regulator, and stirring to pH value of 7-8.    USE - Preparation of alkyl ethoxylate sulfate electrostatic demisting liquid used for preparing pesticide additive, particularly herbicide (claimed).    ADVANTAGE - The liquid can be recycled into high-value products. The process reduces environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pesticide additive comprising 30-40 wt.% AES electrostatic demisting liquid, 6-15 wt.% pH regulator, 1-2 wt.% surfactant and balance water.
NOVELTY - Manufacture of single superphosphate involves adding lime water to gypsum waste containing phosphorus pentoxide and fluorine, reacting, stirring, adjusting pH, performing solid-liquid separation, removing impurities precipitate, adding lime to resulting purified solution, reacting, stirring, adjusting pH, performing solid-liquid separation, filtering, obtaining phosphorus-containing filter cake, recycling filtrate process water for production of phosphoric acid, mixing obtained filter cake and sulfuric acid, mixing and curing.    USE - Manufacture of single superphosphate (claimed).    ADVANTAGE - The method efficiently provides single superphosphate by simple, economical and environmentally-friendly process.    DETAILED DESCRIPTION - Manufacture of single superphosphate involves adding lime water to gypsum waste containing 1.5-6% phosphorus pentoxide and 0.3-1.8% fluorine such that mass ratio of calcium oxide and fluorine is 1-1.4:1, reacting at 15-50 degrees C, stirring for 0.5-2 hours, adjusting pH to 1.5-2.2, performing solid-liquid separation, removing impurities precipitate, adding lime to resulting purified solution such that mass ratio of calcium oxide and phosphorus pentoxide is 0.8-1:1, reacting at 15-50 degrees C, stirring for 0.5-2 hours, adjusting pH to 6.2-7.2, performing solid-liquid separation, filtering, obtaining phosphorus-containing filter cake, recycling filtrate process water for production of phosphoric acid, mixing obtained filter cake and sulfuric acid, mixing and curing. The addition amount of sulfuric acid is 0.2-0.4 times of phosphorus-containing filter cake.
NOVELTY - A fruit swelling agent contains active ingredient containing 18-25 pts. wt., preferably 21 pts. wt. magnesium sulfate, 4-7 pts. wt., preferably 5.5 pts. wt. powdered rock phosphate, and 0.04-0.06 pts. wt., preferably 0.05 pts. wt. phosphorus and potassium solubilizing bacteria.    USE - Fruit swelling agent for melon (claimed).    ADVANTAGE - The fruit swelling agent is convenient to use, increases yield by promoting chlorophyll synthesis and enhancing photosynthesis, reduces use of nitrogenous fertilizer, and has good swelling agent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of fruit swelling agent on melon which involves basal application, diluting, spraying or dipping in which dilution solvent is 800-1500 ml/g.
NOVELTY - A fertilizer composition comprises 45-55 wt.% wild rice leaves, 25-35 wt.% sawdust, 15 wt.% wheat bran, 2 wt.% lime powder, 1 wt.% urea, 1 wt.% calcium superphosphate and 1 wt.% gypsum powder.    USE - Fertilizer composition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer composition comprising drying wild rice leaves, cutting to length of 0.5-1 cm, soaking in 2 vol.% lime solution for 20-24 hours, standing, peeling wheat bran, piling at height of 1.4-1.5 m and width of 2 m, dissolving urea in water, pouring on, fermenting for 8-10 days, adding gypsum powder, calcium superphosphate, sawdust and wheat bran to obtain mixture with moisture content of 63-65%, packaging in polypropylene bags with width of 17 cm, length of 35 cm and thickness of 0.005 cm, putting 1100-1200 g mixture per polypropylene bag, sterilizing at 100 degrees C under atmospheric pressure, standing for 10-12 hours, and cooling at less than or equal to 25 degrees C.
NOVELTY - Nutritional material comprises 20-30 pts. wt. soil, 20-30 pts. wt. peat, 5-10 pts. wt. Azotobacter, 3-56 pts. wt. bacterial decomposition of organic matter, 5-10 pts. wt. fiber mixture, 10-30 pts. wt. perlite, 10-30 pts. wt. vermiculite, and 3-5 pts. wt. green mold.    USE - The nutritional material is useful in municipal engineering for greening and gardening, and as plant growth medium (claimed).    ADVANTAGE - The nutritional material improves nutritional capability of greening soil, and gardening.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the nutrient material, involves (a) incubating bacteria using a suitable medium for microbial flora, adjusting incubation time if required, concentrating culture after decomposition of organic matter bacterial flora, and obtaining nitrogen-fixing bacteria and Trichoderma cell, (b) mixing remainder above-mentioned raw materials, adding suitable amount of organic matter decomposition bacterial flora, nitrogen-fixing bacteria and Trichoderma group, and obtaining product.
NOVELTY - A fertilizer comprises 47-50 pts. wt. fish meal, 45-60 pts. wt. sweet potato powder, 20-40 pts. wt. sludge, 30-48 pts. wt. manure, 4-6 pts. wt. microorganisms, 3-6 pts. wt. molasses, 4-5 pts. wt. wheat bran, 20-35 pts. wt. nitrogen/phosphorus/potassium mixture, 3-5 pts. wt. fertilizer containing zinc, iron, calcium and magnesium and sulfur, 5-10 bentonite and 20-25 pts. wt. nano-release carrier.    USE - Fertilizer composition.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) preparation of fertilizer composition comprising mixing fish meal, sweet potato powder, sludge, manure and nano-release carrier at 30-35 degrees C at water content of 60-70%, adjusting pH to 5-6, stirring for 0.5-1 hour, adding microorganisms, fermenting at 50-60 degrees C for 3-4 days, adding molasses, wheat bran, nitrogen/phosphorus/potassium mixture, fertilizer containing zinc, iron, calcium and magnesium and sulfur and bentonite, mixing at 25-28 degrees C to moisture content of 20-32%, stirring for 1-2 hours, drying, granulating, and packaging; and (2) preparation of nano-release carrier comprising mixing silicon hydroxyapatite, attapulgite, hydrotalcite, montmorillonite, titanium dioxide, calcite, kaolin at mass ratio of 35-45:10-15:10-15:8-10:8-10:7-8:5-7, adding 230 pts. wt. dimethyl sulfoxide and 50 pts. wt. methanol, stirring at 65 degrees C for 60 hours, filtering, washing thrice to remove excess dimethyl sulfoxide, drying at 60 degrees C under vacuum pressure for 24 hours, grinding, sieving to obtain modified compound, mixing 1 pt. wt. modified compound, 15 pts. wt. potassium acetate and 25 pts. wt. distilled water, stirring at 50 degrees C for greater than or equal to 10 hours, dispersing ultrasonically at 30 degrees C for 2.5 hours at power of 350 W and for 4 hours at power of 250 W, heating at 90 degrees C, and stirring mechanically for 60 minutes at speed of 1200 revolutions/minute.
NOVELTY - A fertilizer composition comprises 55-65 wt.% dried sugarcane leaves, 25-35 wt.% manure, 5 wt.% rapeseed cake, 2 wt.% lime powder, 1.5 wt.% calcium superphosphate and 1.5 wt.% gypsum powder.    USE - Fertilizer composition used for mushrooms.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer composition comprising drying sugarcane leaves, cutting to length of 30-40 cm, standing for 2-3 days, spray-drying, crushing, piling on concrete floor at length of 15-20 cm and width of 2 meters, covering at width of 2.3-2.5 cm, length of less than or equal to 5 m and thickness of 1.5 m for 23-25 days, adding gypsum powder, crushing calcium superphosphate, mixing, adding rapeseed cake, fermenting, adjusting pH to 7.2-7.5, and drying to water content of 63-65%.
NOVELTY - Straw mushroom cultivation material comprises 53-63 %mass sugarcane leaves, 15-25 %mass pond mud, 15 %mass bacterial residue, 5 %mass lime powder, and 2 %mass gypsum powder with respect to 100 %mass material.    USE - The cultivation material is useful for cultivating straw mushroom (claimed).    ADVANTAGE - The cultivation material promotes growth of mushroom mycelium, is prepared simply, has reasonable and balanced nutrition, enables vigorous straw mushroom growth, and exhibits efficiency rate to 26.4-28.5%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing straw mushroom cultivation material, which involves (a) taking sugar cane leaves and pond mud, pre-wetting the sugarcane leaves, crushing the leaves to size of 3-5 cm, pouring 5% lime on the leaves, accumulating the leaves for 2 days, stacking the accumulated leaves before 2 days, pre-wetting the dried pond mud, mashing the mixture and uniformly mixing the above-mentioned components to obtain pre-stack, (b) building heap by crushing and uniformly mixing 15-20 cm sugarcane leaves, covering the layer of the leaves using pond mud, stacking and sealing the mixture, fermenting the sealed mixture, where the stack has height of 1.5-1.8 m, width of 2.3-2.5 m and length of not less than 5 m, stacking, setting water outlet at bottom of he stack, turning bottom of bamboo cylinder and inserting crabstick in the cylinder to a diameter of 15 cm, and (c) turning the container for 2-6 days for 4 times, sacking side portion of sugarcane leaves, adding gypsum powder and remaining materials, adjusting pH of the mixture, stopping fermentation, maintaining pH value of the culture to 7.5-8, and maintaining water content to 60-62%.
NOVELTY - Flat mushroom culture material comprises raw materials comprising 52-62 wt.% sugarcane, 15-25 wt.% cotton seed hull, 10 wt.% pond mud, 8 wt.% rice bran, 2 wt.% lime powder, 2 wt.% gypsum powder and 1 wt.% calcium superphosphate, where the mass ratio of dry substance is 100%.    USE - As flat mushroom culture material.    ADVANTAGE - The culture material promotes growth of white fungus mycelium, provides biological efficiency of 135.3-152.8%, and is harmless.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the culture material, which involves cutting sugarcane leaves, pre-wetting sugarcane, cutting sugarcane into 2-3 cm, spraying 2% using lime water, stacking sugarcane for 2 days, drying pond mud, crushing, uniformly mixing, paving sugarcane on cement ground, paving layer of pond mud, stacking at height of 1.5-1.8 m, width of 2.3-2.5 m and length of 5 m, turning mixture for 6, 5, 4, 3 or 2 days, turning for 4 times, adding gypsum powder, calcium superphosphate, cotton seed hull and rice bran, and fermenting mixture until water content of the culture material is 63-65%.
NOVELTY - A vegetable seedling substrate is prepared by taking corn cob as raw material, adding 5-20 wt.% manure and 10-25 wt.% inorganic modifiers, inoculating, drying to obtain powder with powder to water mass ratio of 10000-20000:1, fermenting to moisture content of 50-65%, heating at 50 degrees C to obtain brownish mixture, cooling to 35 degrees C, sieving binder to particle size of 12 mesh, adding 10-15 wt.% horticultural vermiculite and 3-8 wt.% perlite, and mixing.    USE - Method for preparing vegetable seedling substrate (claimed).
NOVELTY - White fungus culture material comprises raw materials comprising 25-35 wt.% fresh tea meal, 38-48 wt.% tea seed meal, 20 wt.% wheat bran, 3 wt.% soybean powder, 1 wt.% calcium superphosphate, 1 wt.% gypsum powder, 1.2 wt.% sucrose, 0.5 wt.% monopotassium phosphate and 0.3 wt.% magnesium sulfate, where the proportion of dry substance is 100%.    USE - As white fungus culture material.    ADVANTAGE - The culture material promotes growth of white fungus mycelium, provides balanced nutrition and biological efficiency of 11-12.1% and high yield, and is harmless.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the culture material, which involves exposing the raw material to UV for 2-3 days, killing bacteria in raw material, pre-wetting the raw materials, drying raw materials, piling for 2 hours until the moisture content is 50-55%, mixing wheat bran, soybean powder, calcium superphosphate, gypsum powder, fresh tea, tea seed meal, pre-wet material, sucrose, monopotassium phosphate and magnesium sulfate, uniformly stirring mixture, adding mixture into polyethylene bag, sterilizing and cooling bag at 100 degrees C, maintaining bag for 10-12 hours, and naturally cooling to lower than 25 degrees C.
NOVELTY - Method for preparing carbapenem antibiotic intermediate, involves (a) reacting azetidin-2-one compound (II) with 2-methylene-3-oxo-pentanal compound (III) to obtain intermediate (1R,5R)-4-((R)-3-ethyl-4-oxo-azetid in-2-yl)-2-methylene-3-oxo-pentanal compound (XVI), and (b) synthesizing the (1R,5R)-4-((S)-3-((R)-1-hydroxy-ethyl)-4-oxo-azetidin-2-yl)-2-methylene-3-oxo-pentanal compound (I) from the intermediate compound.    USE - The method is useful for preparing carbapenem antibiotic intermediate (claimed).    ADVANTAGE - The method is simple, rapid, cost-effective, environmentally-friendly and less labor intensive, reduces type and dosage of the solvent, and utilizes easily available raw materials as compared to existing method.    DETAILED DESCRIPTION - Method for preparing carbapenem antibiotic intermediate, involves (a) reacting azetidin-2-one compound of formula (II) with 2-methylene-3-oxo-pentanal compound of formula (III) to obtain intermediate (1R,5R)-4-((R)-3-ethyl-4-oxo-azetid in-2-yl)-2-methylene-3-oxo-pentanal compound of formula (XVI), and (b) synthesizing the (1R,5R)-4-((S)-3-((R)-1-hydroxy-ethyl)-4-oxo-azetidin-2-yl)-2-methylene-3-oxo-pentanal compound of formula (I) from the intermediate compound.    R1=methyl, ethyl, P-nitrobenzyl, benzyl, allyl, 4-chlorobenzyl, 2-nitrobenzyl, 3-nitrobenzyl or 4-methoxybenzyl;    R2=acetyl or benzoyl;and    R3=trimethylsilyl or t-butyldimethylsilyl.
NOVELTY - 2-(3-(S)-(3-(2-(7-Chloro-2-quinolinyl)ethenyl)phenyl)-(3-hydroxy)propyl)benzoate (I) is obtained by using 2-(3-(3-(2-(7-chloro-2-quinolinyl)ethenyl)phenyl)-(3-carbonyl)propyl)benzoate(II), ketoreductase, trolamine buffer, isopropyl alcohol, and toluene as raw materials, adding a co-factor solution to the reaction solution, and recrystallizing the reaction solution with water and ethanol.    USE - Preparation of 2-(3-(S)-(3-(2-(7-chloro-2-quinolinyl)ethenyl)phenyl)-(3-hydroxy)propyl)benzoate useful as non-steroid antiinflammatory drug intermediate.    ADVANTAGE - The method enables simple, environmentally-friendly and economical preparation of 2-(3-(S)-(3-(2-(7-chloro-2-quinolinyl)ethenyl)phenyl)-(3-hydroxy)propyl)benzoate with high product purity.    DETAILED DESCRIPTION - 2-(3-(S)-(3-(2-(7-Chloro-2-quinolinyl)ethenyl)phenyl)-(3-hydroxy)propyl)benzoate of formula (I) is obtained by using 2-(3-(3-(2-(7-chloro-2-quinolinyl)ethenyl)phenyl)-(3-carbonyl)propyl)benzoate of formula (II), ketoreductase, trolamine buffer, isopropyl alcohol, and toluene as raw materials, adding a co-factor solution to the reaction solution, and recrystallizing the reaction solution with water and ethanol.
NOVELTY - Preparation of tetrahydrofuran derivative (I) involves reacting isatin diazonium compound (II), ortho-substituted benzaldehyde compound (III) and nitro group-containing compound (IV) in presence of 1-2 mol% rhodium(II) acetate as catalyst and 20-30 mol% 2,3,4,6,7,8,9,10-octahydropyrimido(1,2-a)azepine.    USE - Preparation of tetrahydrofuran derivative (claimed).    ADVANTAGE - The method economically and efficiently provides tetrahydrofuran derivative with high yield, by a simple and environmentally-friendly process in a short period of time, under mild reaction condition.    DETAILED DESCRIPTION - Preparation of tetrahydrofuran derivative of formula (I) involves reacting isatin diazonium compound of formula (II), ortho-substituted benzaldehyde compound of formula (III) and nitro group-containing compound of formula (IV) in presence of 1-2 mol% rhodium(II) acetate as catalyst and 20-30 mol% 2,3,4,6,7,8,9,10-octahydropyrimido(1,2-a)azepine.    R1=H, 5-methyl, 5-fluoro, 6-fluoro or 6-chloro;    R2=methyl, acetyl or benzyl;    R3=5-fluoro, 5-chloro, 4-diethylamino, 5-bromo, 5-tert-butyl, 5-methoxy, 3-methoxy or phenyl;and    R4=phenyl, 2-methoxyphenyl, 4-methoxyphenyl, 3-chlorophenyl, 4-bromophenyl or 4-nitrophenyl.
NOVELTY - Preparation of 3,3-spiro(2-tetrahydrofuranyl)oxindole polycyclic compound (I) involves reacting isatin diazonium compound (II), ortho-substituted phenyl nitroalkene compound (III) and aldehyde compound (IV) in presence of rhodium(II) acetate as catalyst and 2,3,4,6,7,8,9,10-octahydropyrimido(1,2-a)azepine.    USE - Preparation of 3,3-spiro(2-tetrahydrofuranyl)oxindole polycyclic compound (claimed).    ADVANTAGE - The method economically and efficiently provides 3,3-spiro(2-tetrahydrofuranyl)oxindole polycyclic compound with high yield, by a simple and environmentally-friendly process in a short period of time, under mild reaction condition.    DETAILED DESCRIPTION - Preparation of 3,3-spiro(2-tetrahydrofuranyl)oxindole polycyclic compound of formula (I) involves reacting isatin diazonium compound of formula (II), ortho-substituted phenyl nitroalkene compound of formula (III) and aldehyde compound of formula: R3-CHO (IV) in presence of rhodium(II) acetate as catalyst and 2,3,4,6,7,8,9,10-octahydropyrimido(1,2-a)azepine.    R1=H, 5-methyl, 5-fluoro, 6-fluoro or 6-chloro;    R2=methyl, acetyl or benzyl;    R3=phenyl, m-bromophenyl, p-bromophenyl, p-methoxyphenyl, o-fluorophenyl, styryl, 2-thiophene or 2-furyl;and    R4=5-chloro or 5-bromo.
NOVELTY - 3-(N-methyl-n-pentylamine)propionic hydrochloride, phosphorous acid and 1,3-dimethyl-2-imidazolidinone are mixed. Phosphorus trichloride is dropped to resulting mixture, and cooled. The resulting product is subjected to thin-layer chromatography and dried, to obtain crystalline ibandronate monohydrate crude product. The crude product and deionized water are added into reactor, heated, activated carbon and methanol are added, stirred, filtered, solid is washed with methanol, decompressed, and dried to obtain white crystalline ibandronate sodium monohydrate.    USE - Preparation of crystalline ibandronate sodium monohydrate (claimed).    ADVANTAGE - The method environmentally-friendly provides crystalline ibandronate sodium monohydrate with high yield and high purity.    DETAILED DESCRIPTION - 3-(N-methyl-n-pentylamine)propionic hydrochloride, phosphorous acid and 1,3-dimethyl-2-imidazolidinone are mixed, added into glass reactor and hydrogen chloride gas absorption device at 25-30 degrees C, and stirred for 10 minutes. Phosphorus trichloride is dropped at 60-70 degrees C, reacted at 80 degrees C for 6 hours, and cooled to 30 degrees C. 20 l Deionized water is added, reacted at 45 degrees C, heated, and stirred at 110 degrees C for 7 hours. The resulting product is subjected to thin-layer chromatography, cooled at 40 degrees C, sodium hydroxide solution is added to adjust pH to 4.1-4.3, 30% methanol solution is added, stirred for 2 hours, centrifuged, filtered, and dried at 55-60 degrees C, to obtain white solid crystalline ibandronate monohydrate crude product. The crystalline ibandronate monohydrate crude product and deionized water are added into reactor, heated to 50 degrees C, dissolved, activated carbon is added, stirred for 30 minutes, methanol is added, stirred for 2 hours, centrifuged and filtered. The resulting solid is washed with methanol, decompressed, and dried at 55-60 degrees C, to obtain white crystalline ibandronate sodium monohydrate.
NOVELTY - Preparation of glyphosate involves reacting methyl phosphonic acid sodium salt and glycine as raw material, in presence of sodium iodide or polyethyleneimine as catalyst and water.    USE - Preparation of glyphosate (claimed).    ADVANTAGE - The method economically and environmentally-friendly provides glyphosate having improved quality with high yield and efficiency.
NOVELTY - Preparing wood fiber biomass thin film comprises (i) crushing wood fiber biomass, and passing through a 160 mesh sieve; (iii) dissolving the crushed wood fiber biomass in dimethyl sulfoxide/lithium chloride (DMSO/LiCl) to obtain wood fiber film liquid, the content of DMSO/LiCl in the solvent system is 2-10%, and controlling the wood fiber biomass film liquid concentration to 1-20 wt.%; and (iii) placing the film liquid film on an upper flat plate film-forming film, soaking in a coagulation bath, removing the solvent, and drying to obtain the regenerated wood fiber biomass thin film.    USE - The method is useful for preparing wood fiber biomass thin film (claimed).    ADVANTAGE - The method: is simple; has high efficiency; and can directly use the existing high molecular film-forming device. The thin film has surface roughness and simple structure.
NOVELTY - Soil conditioning agent comprises raw materials comprising 6-14 pts. wt. lactein, 86-94 pts. wt. physical and chemical factors, 18x 108 colony forming unit (cfu)/g Rhodopseudomonas palustris, where the physical and chemical factors are crushed to obtain particles of size 200 meshes, 40-72 pts. wt. white clay powder, 20-40 pts. wt. zinc sulfate heptahydrate, and 3-7 pts. wt. magnesium oxide.    USE - The soil conditioning agent is useful for reducing cadmium content in crop during production, where the crop is rice (all claimed).    ADVANTAGE - The agent improves pH value of soil, and reduces cadmium ion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing soil conditioning agent, which involves culturing R.palustris in slant culture under aseptic condition, performing fermentatio, obtained fermentation liquid, concentrating and drying the liquid to obtain spore powder.
NOVELTY - Method for removing heavy metal-containing soil from chemical eluant containing disodium ethylenediaminetatraacetci acid and saponin as an active ingredient, is claimed.    USE - Method for removing heavy metal-containing soil from chemical eluant for processing polluted soil e.g. lead and/or zinc polluted soil (all claimed).    ADVANTAGE - The heavy metal-containing soil is removed from chemical eluant by a simple and environmentally-friendly process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for processing polluted soil, which involves digging and transferring polluted soil to a stirring tank, adding chemical eluant, fully stirring, then stopping stirring until the solution is clear, adding water, and drying.
NOVELTY - Preparation of water-retaining and sand-fixing agent involves adding 20-45 %mass high-water-absorbent resin to water, heating to 60-90 degrees C, stirring to dissolve, adding remaining water, then adding crushed plant straw, fermentated furfural residue and fixing agent, and stirring uniformly. The water-retaining and sand-fixing agent contains 5-25 %mass furfural residue, 5-20 %mass fixing agent, 0.5-5 %mass crushed plant straw, 1-10 %mass high-water-absorbing resin and 50-85 %mass water.    USE - Preparation of water-retaining and sand-fixing agent is used as liquid mulching film planting lawn.    ADVANTAGE - The method enables preparation of environmentally-friendly and degradable water-retaining and sand-fixing agent.
NOVELTY - A high speed and cost-efficient treatment system has main reaction tanks (A, B) used for performing biochemical reactions which are connected to nutrient solution storage tank, liquid supply unit (2), liquid discharge unit (3), gas collection and detection unit (10, 16), heating temperature control unit (17), and time control unit (18) connected to run-time control system.    USE - A high speed and cost-efficient treatment system for urban organic solid waste (claimed).    ADVANTAGE - The method reduces municipal solid wastes, consumes less processing time, produces clean biological energy source, has no greenhouse gas emission, is low cost, and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for treatment method of urban organic solid waste which involves separating, crushing, loading in main reaction tank, preparing nutrient solution in nutrient solution storage tank, pre-heating in heating temperature control device at not less than 35 degrees C, injecting to main reaction tank until liquid surface contains less solid, standing overnight, draining nutrient solution through discharge device leading back to nutrient solution storage tank, repeating procedure depending on frequency of detected methane gas content, and recovering residual solid waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a treatment system for urban organic solid waste. (Drawing includes non-English language text).    Liquid supply unit (2)    Liquid discharge unit (3)    Gas collection and detection unit (10, 16)    Heating and temperature control unit (17)    Time control unit (18)    Reaction tank (A, B)
NOVELTY - Tetracycline bacteria residue is processed by mixing 75-90% tetracycline bacteria residue, 0.1-0.3% glucose, and balance water to obtain fermentation culture medium, fermentation culturing using beer yeast and Candida tropicalis, adding yeast extract, and performing enzyme extraction to obtain organic nitrogen source.    USE - Processing of tetracycline bacteria residue for preparing organic nitrogen source (claimed) used for feed and fertilizer.    ADVANTAGE - Processing of tetracycline bacteria residue reduces cost and bacteria residue discharge, and produced organic nitrogen source has rich amino acid content.