NOVELTY - Method of producing liquid hydrocarbon mixtures is carried out via hydroconversion of lignocellulose biomass in a solvent medium in the presence of a dispersed catalyst precursor. The method includes drying the biomass; grinding the biomass; preparing a paste from the ground biomass, solvent and dispersed catalyst precursor; hydroconversion of the prepared paste; separating the obtained products in a system of separators; the method is characterised by that the solvent used is an organic solvent having viscosity of 0.5-2.5 Pa.s at 60-90 degrees C, which contains 2-5.5 wt % sulphur and 5-25 wt % polycyclic aromatic hydrocarbons and/or derivatives thereof, and grinding of the biomass and preparation of said paste is carried out via dispersion with mechanical activation of the biomass in a solvent medium containing a catalyst precursor, wherein the prepared paste is first heated in an inert atmosphere to temperature of 330-380 degrees C and pressure of 0.2-0.5 MPa until removal of the basic amount of oxygen in the biomass in the form of CO, CO2 and H2O, followed by hydroconversion.    USE - Chemistry.    ADVANTAGE - High output of liquid products of hydroconversion of the biomass, higher conversion of the biomass and simpler process.10 cl, 10 tbl, 2 dwg, 7 ex
NOVELTY - Method of disrupting biomass, involves fermenting biomass with microorganism or consortium of microorganisms producing gas in vessel, where the gas increases pressure in the vessel, and disrupting the biomass by abruptly releasing the increased pressure.    USE - The method is useful for disrupting biomass (claimed).
NOVELTY - Method for preparing bark compost, involves (a) cleaning bark using water, draining water, separating radioactive substance from the bark, adding water to radioactive substance and adding organic polymer flocculant to the mixture, (b) sedimenting the mixture and obtaining flocculated precipitate, (c) inoculating microbial bacteria in the precipitate, adding the mixture to bark compost raw material and fermenting the mixture, (d) homogenizing the fermented mixture, and (f) adding the agglomerated precipitate to the bark compost raw material and fermenting the mixture.    USE - The method is useful for preparing bark compost (claimed).    ADVANTAGE - - The method prepares bark compost which has radiation dose of 200 Bq/kg, and is environmentally-friendly.    DETAILED DESCRIPTION - Method for preparing bark compost, involves (a) cleaning bark using water, draining water, separating radioactive substance from the bark, adding water to radioactive substance and adding organic polymer flocculant to the mixture, (b) sedimenting the mixture, obtaining flocculated precipitate and discarding supernatant comprising water, (c) inoculating microbial bacteria in the above-mentioned precipitate, adding the mixture to bark compost raw material and fermenting the mixture, (d) homogenizing and stirring the fermented mixture, and (f) adding the agglomerated precipitate to the bark compost raw material and again fermenting the mixture.
NOVELTY - Enzyme composition comprises one or more endoglucanases, one or more cellobiohydrolases, one or more beta -glucosidases, at least one beta -mannosidase, and at least one mannanase, where the mannanase is chosen from Aspergillus niger mannanase, Trichoderma reesei mannanase, Corollospora maritima mannanase or Talaromyces leycettanus mannanase.    USE - The enzyme composition is useful for hydrolyzing a mannan-containing cellulosic material, degrading a mannan-containing cellulosic material, and producing a fermentation product. The fermentation product is alcohol, alkane, cycloalkane, alkene, amino acid, gas, isoprene, ketone, organic acid, or polyketide (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) process (P1) for degrading a mannan-containing cellulosic material, involves treating the cellulosic material with an enzyme composition; and    (2) process (P2) for producing a fermentation product, involves (a) saccharifying a mannan-containing cellulosic material with an enzyme composition, fermenting the saccharified cellulosic material with a fermenting microorganism to produce the fermentation product and recovering the fermentation product from the fermentation, or (b) contacting an aqueous slurry of a mannan-containing cellulosic material with an enzyme composition of the present invention to produce a soluble hydrolyzate, and contacting the soluble hydrolyzate with a fermenting organism to produce a fermentation product.
NOVELTY - Preparation of water-soluble fertilizer comprises crushing low-value fish into fish slurry and removing impurities; adding purified water at mass ratio of 0.8-1.2:1 and adding into fermentation tank; adding 7-15 wt.% strain and 15-25 wt.% enzyme, and stirring; fermenting at 40-45 degrees C for 11-13 hours and stirring; aerating for 40-80 minutes and stirring for 10-20 minutes; and fermenting for 3-8 days.    USE - Method for preparing water-soluble fertilizer used for Paris polyphylla (claimed).    ADVANTAGE - The method is simple, has short processing time, and reduces loss of nutrient substance.
NOVELTY - Artificial ecological circulation system comprises biogas treatment system containing biogas, biogas power generation unit, power supply line, lamp, air circulation system, filtration system and water supply pipes. The biogas is used for anaerobic fermentation of plant residues, animal feces, kitchen garbage and brewing waste to obtain biogas and biogas slurry used as animal feed and fertilizer. The carbon dioxide produced from the power generation process is delivered to plants for photosynthesis. The filtration system is wound on natural fibers to obtain clean water throughout the system.    USE - Artificial ecological circulation system used for organic waste and urban wastewater treatment.    ADVANTAGE - The system is energy efficient.
NOVELTY - Production of biological carbon comprises drying food waste to moisture content of less than 10%, crushing into 4-6 mm, placing in carbonization furnace, purging with nitrogen, successively heating at 200-300 degrees C for 30-60 minutes with heating rate of 2-10 degrees C/minute and at 350-500 degrees C for 1-4 hours with heating rate of 5-20 degrees C/minute, cooling to 80 degrees C, crushing into 100 mesh, soaking in deionized water for 8-12 minutes, filtering and drying.    USE - Method for producing biological carbon for soil improvement (claimed).    ADVANTAGE - The method is simple, cost-saving and environment-friendly. The product increases soil pH value to 0.15-0.45 and total porosity to 4-12% and decreases soil bulk density to 4-10%.    DETAILED DESCRIPTION - Production of biological carbon comprises drying food waste to moisture content of less than 10%, crushing into 4-6 mm, placing in carbonization furnace, purging with nitrogen, successively heating at 200-300 degrees C for 30-60 minutes with heating rate of 2-10 degrees C/minute and at 350-500 degrees C for 1-4 hours with heating rate of 5-20 degrees C/minute, cooling to 80 degrees C, crushing into 100 mesh, soaking in deionized water for 8-12 minutes, filtering and drying to obtain biological carbon with pH value to 8.0-10.5, organic matter content of 50-70%, nutrient content of 5-15%, porosity of 0.25-0.35 cm3/g, aperture of 10-40 nm and average specific surface area of 120-220 m3/g.
NOVELTY - Preparation of composite fertilizer comprises mixing straw decomposition agent and mixed culture material, decomposing to prepare compost cultivation material, mixing with straw powder and straw fiber and granulating.    USE - Method for preparing composite fertilizer (claimed).    ADVANTAGE - The method is environment-friendly.
NOVELTY - Preparation of banana special fertilizer involves mixing carbamide and phosphoric acid, adding into reaction kettle, heating, reacting while stirring, cooling and centrifugally separating to obtain intermediate; mixing intermediate and alkaline potassium salt, adding into reaction kettle, stirring, reacting while stirring and adjusting pH to obtain material slurry; circulating material slurry in cooling crystallizer, detecting filtrate, stopping crystallizing and filtering to obtain filter cake comprising potassium dihydrogen phosphate product; and drying and adjusting water content.    USE - Method for preparing banana special fertilizer (claimed).    ADVANTAGE - The fertilizer has low production cost, and no environment-polluting waste liquid discharge.    DETAILED DESCRIPTION - Preparation of banana special fertilizer comprises:    (A) mixing carbamide and phosphoric acid at mol ratio of (1.2-1.4):1, adding into reaction kettle, heating to 100-130 degrees C at speed of 3 degrees C/minute, reacting while stirring for 150-180 minutes, cooling to 20-30 degrees C and centrifugally separating to obtain intermediate;    (B) mixing intermediate and alkaline potassium salt at mol ratio of 1:(1.8-2), adding into reaction kettle, stirring at speed of 220-240 revolutions/minute, reacting while stirring for 60-80 minutes and adjusting pH to 10-11 to obtain material slurry;    (C) circulating material slurry in cooling crystallizer, detecting filtrate if nitrogen content is 3-5%, phosphorus content is 0.5-1.5% and potassium content is 9-11%, stopping crystallizing and filtering to obtain filter cake comprising potassium dihydrogen phosphate product; and    (D) adding potassium dihydrogen phosphate product, filtrate and trace elements, drying at 20-30 degrees C for 40-60 minutes and adjusting water content to 3-5%.
NOVELTY - A mushroom culture medium comprises high-order peat soil and corn core as raw materials.    USE - Mushroom culture medium.    ADVANTAGE - The culture medium reduces material cost and changes waste into treasure, thus increasing economic benefit.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) pre-processing high-order peat soil comprising adding 1% alum and 1% activated coal and drying; and    (2) production of mushroom culture medium comprising mixing corn core and high-order peat soil at ratio of 1:1-2:1 and adding 1.5% gypsum, 1% potassium dihydrogen phosphate, 0.5% calcium superphosphate and 1% corn powder.
NOVELTY - Preparation of sugarcane organic fertilizer comprises uniformly mixing water, cow manure, chicken manure, rice bran, flashed brick powder, filter mud, cypress, silicon dioxide powder, bactericide and metal passivating agent, standing for 1-24 hours, adding fermentation microbial inoculum and brown sugar, mixing with sterile water to water content of 50-60 wt.%, stacking, aerobically fermenting for 15-20 days while turning every 2 days, fermenting for 25-30 days while turning every 3-4 days, anaerobically fermenting for 5-9 days, regulating water content to 20-30 wt.%, crushing and sieving.    USE - Method for preparing sugarcane organic fertilizer (claimed).    ADVANTAGE - The fertilizer eliminates odor and increases quick-acting nutrient content.    DETAILED DESCRIPTION - Preparation of sugarcane organic fertilizer comprises uniformly mixing 20-50% water, 30-50 pts. wt. cow manure, 30-50 pts. wt. chicken manure, 60-70 pts. wt. rice bran, 10-15 pts. wt. flashed brick powder, 10-15 pts. wt. filter mud, 2-5 pts. wt. tea cypress, 2-5 pts. wt. silicon dioxide powder, bactericide and metal passivating agent, standing for 1-24 hours, adding fermentation microbial inoculum and 1-2 pts. wt. brown sugar, mixing with sterile water to water content of 50-60 wt.%, stacking, aerobically fermenting for 15-20 days while turning every 2 days, fermenting for 25-30 days while turning every 3-4 days, anaerobically fermenting for 5-9 days, regulating water content to 20-30 wt.%, crushing and sieving.
NOVELTY - Isolation of purified caffeic acid, ferulic acid and isoferulic acid from Chinese propolis aqueous extract, involves freezing Chinese propolis, crushing, heating, extracting, cooling, removing upper solidified beeswax, concentrating, adding ethanol, removing supernatant, eluting, purifying, collecting fractions and then concentrating to obtain sample, subjecting sample to high performance liquid chromatography, and collecting fractions and then concentrating to obtain monomer compound containing caffeic acid, ferulic acid and isoferulic acid.    USE - Isolation of purified caffeic acid, ferulic acid and isoferulic acid from Chinese propolis aqueous extract (claimed).    ADVANTAGE - The method enables easy and safe isolation of caffeic acid, ferulic acid and isoferulic acid from Chinese propolis aqueous extract in an economical and environmentally-friendly manner.    DETAILED DESCRIPTION - Isolating purified caffeic acid, ferulic acid and isoferulic acid from Chinese propolis aqueous extract, involves freezing Chinese propolis, crushing, heating and then extracting using distilled water, cooling to room temperature, removing upper solidified beeswax, concentrating under reduced pressure to a relative density of 1.2, adding 95% ethanol to the concentrate and then allowing to react overnight, removing supernatant, eluting, purifying using macroporous resin, collecting fractions and then concentrating to obtain sample, subjecting sample to high performance liquid chromatography, collecting fractions and then concentrating under reduced pressure to obtain monomer compound containing caffeic acid, ferulic acid and isoferulic acid.
NOVELTY - Bacillus thuringiensis Bt-1 strain with the preservation number CCTCC No: M2013680, is new.    USE - The Bacillus thuringiensis is useful for degrading pesticides, preferably azoxystrobin, kresoxim, pyraclostrobin, cyhalothrin, deltamethrin, cyhalothrin and/or fenpropathrin, in crops, soil or water (all claimed).    ADVANTAGE - The strain has high environmental adaptability, high degradation efficiency, is easy to use, solves agricultural production problems and environmental problems, produces pollution-free green agricultural products, and protects the ecological environment and human health.
NOVELTY - A heat shock protein (Hsp)23 gene of gypsy moth, comprising a 750 base pair sequence (SEQ ID NO: 1) fully defined in the specification, is new.    USE - The Hsp23 gene is useful in prevention of growth and development of gypsy moth, preferably Asian gypsy moth (claimed) in forest plantation region.    ADVANTAGE - The Hsp23 gene enables environmentally-friendly insect control technique.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for double-stranded (ds)RNA of the Hsp23 gene, which comprises a 516 base pair sequence (SEQ ID NO: 2) fully defined in the specification.
NOVELTY - Utilizing agricultural straw involves pretreating crop straw by steam explosion. The cellulase and yeasts are added to obtained product for hydrolysis and fermentation to obtain mash. The activated yeast Saccharomyces cerevisiae is cultured in mixture of corn mash and sugar. The ratio of corn mash and sugar is 80-90:10-20. The large yeasts are obtained by multi-generation expanded culture. The ratio of corn mash and sugar is 60-70:30-40. The sugar concentration is increased until digested sugar becomes more than 70%. The obtained material is distilled to obtain ethanol.    USE - Method for utilizing agricultural straw used for preparing thermoplastic wood, cellulosic ethanol and compressed natural gas for vehicles (claimed).    ADVANTAGE - The method enables complete utilization of agricultural straw.
NOVELTY - Method of preparing biocompost from organic wastes lies in the fact that two modes of ventilation are carried out in it. In the first mode, with the variable flow rate, the air from the exhaust system of the fermenter is fed to air-air heat exchanger through which the fresh air is passed. In the second mode, with the constant maximum flow rate, the exhaust air is discharged directly into the environment, and the outdoor air through the secondary circuit of the heat exchanger and the inflow system is fed into the fermentable biomass. The transition from the first mode to the second is carried out after reaching the temperature of the fermented biomass of 65-70 degrees C. The temperature, humidity and oxygen content in the fresh air and the exhaust window of the ventilation system are periodically measured. According to the measured information the state of the fermented biomass is assessed, and the optimal programs of changing the air flow rate are formed, which ensures a minimum heating time of the fermented biomass. The device comprises a fermenter with a perforated bottom, a ventilation system equipped with a air-air heat exchanger with a bypass tee at the inlet and the controlled valve changing the direction of flow, sensors of temperature, humidity and oxygen content, mounted at the inlet and outlet of the ventilation system, and an automatic control device which inlet is connected to the sensors of temperature, humidity and oxygen content, and which outlet is connected to the controlled drive of the forced fan and the drive of the controlled valve.    USE - Agriculture.    ADVANTAGE - Invention provides improvement of biocompost quality and reduction of time of its preparation.6 cl, 4 dwg
NOVELTY - Method includes anaerobic fermentation of organic substances in a methane tank with electrical activation of the medium with dc voltage of 0.2-36 V while stirring and bubbling the mass with the released biogas. The organic substances are fed into the methane tank with moisture content of 40-95%. Monitoring is carried out by measuring the value of current in the electrical circuit, calculating conductivity of the system, measuring the volume flow rate of the formed biogas and determining the current content of carbon dioxide gas in the biogas in the upper part of the methane tank.    USE - Chemistry.    ADVANTAGE - High content of methane in biogas, intensification of the process of producing biogas, high process stability and obtaining an end product with accurately defined parameters.    DETAILED DESCRIPTION - Electrical activation of methanogenesis is controlled by controlling current by setting a new value of current at the level of the sum of the present and calculated maximum current.
NOVELTY - Method of production of organic fertiliser from biodegradable wastes comprises mixing bird dropping, livestock manure and biodegradable wastes, stacking the shoulder with the height of 2.4-3 m, the width of 4.5-5 m, of arbitrary length, its moisture, crushing, settling the substrate with rain worms Eisenia foetida in an amount of 500 zooids per 1 m3 of the mixture at an ambient temperature not lower than 0 degrees C, at that the main component of the substrate is taken as scraps of trees, bushes, lawn grass and weeds, corn cores, food waste in an amount of 75%, and bird dropping and manure - 25%, the shoulder is moistened three times to moisture content of 60-70%, preliminary mixed, immediately after the stacking, and a half month and one month it is crushed with a hammer mill and moistened the 3rd time, the earthworms are placed, the shoulder is not covered, the process of biochemical degradation of compost and simultaneous propagation of earthworms is carried out without stirring, without fertilising and selection for 7.5 months.    USE - Agriculture.    ADVANTAGE - Invention enables to recycle wastes, to reduce the time of decomposition of compost, to obtain the quality fertiliser for any crop.1 dwg, 1 ex
NOVELTY - An organic waste is cut to 3-5 mm, and optionally dried. The dried waste is added to a reactor, and processed at 200-450 degrees C and 6.5 mbar. An oxidation additive is added to a section (A) of the reactor, and obtained final product is separated into liquid and gas phases. The gas phase is cleaned, and neutralized. Water, low-melting point hydrocarbon and solid contaminants are extracted from the gas phase and collected. The solid product remained at the end of the thermal cracking is removed from the reactor, cooled and collected.    USE - Production of recyclable base material e.g. gaseous, steam and solid base material (claimed).    DETAILED DESCRIPTION - An organic waste is cut to 3-5 mm, and optionally dried to moisture content of 7-8% using waste heat of the process. The dried waste is added to a conical inner shell tiltable axis reactor provided with a heating sheath, and processed at 200-450 degrees C and 6.5 mbar. Reactor blades are mounted on a section (A) of the reactor and a reactor screw is provided on a section (B) of the reactor. An oxidation additive is added to the section (A) of the reactor, and obtained final product is separated into liquid and gas phases in a condenser. The gas phase is cleaned in a gas processor, neutralized and forwarded through a vacuum pump for further processing. Water, low-melting point hydrocarbon and solid contaminants are extracted from the gas phase in an oil separator and collected in an oil tank. The solid product remained at the end of the thermal cracking is removed from the reactor, cooled and collected in a slag storage unit provided with a lever sensor.
NOVELTY - A farmyard manure retting method comprises taking wheat straw, rice straw and/or corn straw, cutting, taking 5 pts. wt. straw stick, 2 pts. wt. soil, 1 pt. wt. human and livestock manure, and 2 pts. wt. human and livestock urine, soil paving at thickness of 10-15 cm, taking straw stick, soaking in human and livestock urine, spreading straw at thickness of 25-30 cm, spreading human and livestock manure, soil paving, and retting for 30-35 days.    USE - Farmyard manure retting method (claimed).    ADVANTAGE - The method improves fertility of farm fertilizer.
NOVELTY - Preparation of livestock manure flower fertilizer comprises taking 30-45 pts. wt. dairy manure, 10-15 pts. wt. plant ash, 5-10 pts. wt. golden cypress and 5-15 pts. wt. persimmon, mixing, sending into plastic greenhouse fermentation device, adding effective microorganism strain, fermenting at 40-55 degrees C, adding 5-10 pts. wt. urea, adding quicklime, regulating pH to 7-7.5, drying to water content of 12%, mixing, cooling, crushing into 60-80 mesh, adding adhesive, granulating, cooling and packaging.    USE - Method for preparing livestock manure flower fertilizer (claimed).    ADVANTAGE - The fertilizer is easy to use and transport.
NOVELTY - Preparation of ceftiofur sodium comprises taking 2-furoyl chloride and sodium hydrosulfide as raw material, preparing into water phase solution at 20-30 degrees C and pH of 6-8 to obtain 2-furan-methylthio hydroxy acid; reacting with 7-aminocephalosporanic acid in the presence of catalyst in organic solvent at 0-15 degrees C; reacting with active ester, treating with 2-ethylhexanoate and sodium exchange reagent, adding activated charcoal to decolor, filtering, adding crystallization solvent to filter liquid, crystallizing, and vacuum drying.    USE - Method for preparing ceftiofur sodium (claimed).    ADVANTAGE - The method is simple, environment-friendly, and suitable for industrial production, has high yield, low cost, and inexpensive raw materials, and shortens synthesis steps.
NOVELTY - Preparation of (R)-9-(2-phosphate methoxy propyl)adenine (I) comprises reacting adenine and propylene carbonate, adding p-toluenesulfonyloxy diethyl phosphite and alkyl derivative (II), adding protonic acid and carrying out hydrolysis reaction.    USE - Method for preparing (R)-9-(2-phosphate methoxy propyl)adenine (claimed).    ADVANTAGE - The method is environment-friendly and cost-saving and has low energy consumption.    DETAILED DESCRIPTION - Preparation of (R)-9-(2-phosphate methoxy propyl)adenine of formula (I) comprises reacting adenine and propylene carbonate adding p-toluenesulfonyloxy diethyl phosphite and alkyl derivative of formula (RO)2Mg (II), adding protonic acid and carrying out hydrolysis reaction.    R=1-6C aliphatic alkyl.
NOVELTY - Improved and environmentally-friendly preparation of xanthenes-1,8(2H)-dione derivative (I) involves reacting cyclocondensed aldehyde (II) with 1,3-diketone (III) in absence of catalyst.    USE - Improved and environmentally-friendly preparation of xanthenes-1,8(2H)-dione derivative used as antibiotics, and antibacterial, antiviral, and antiinflammatory agents.    ADVANTAGE - The method enables economical and environmentally-friendly preparation of xanthenes-1,8(2H)-dione derivative with improved yield by catalyst-free synthetic transformation, using raw materials having simple handleability, within short period of time.    DETAILED DESCRIPTION - Improved and environmentally-friendly preparation of xanthenes-1,8(2H)-dione derivative or its analog of formula (I) involves reacting cyclocondensed aldehyde of formula (II) with 1,3-diketone of formula (III) in absence of catalyst.    R1,R2=aryl or heteroaryl (both optionally substituted by H or electron-donating and electron-withdrawing substituent);and    n=1 or 2.
NOVELTY - Pollution-free organic fertilizer comprises chicken manure (20-35 pts. wt.), rapeseed cypress (8-15 pts. wt.), zeolite (10-18 pts. wt.), weathered coal powder (18-35 pts. wt.), humic acid (20-25 pts. wt.), grass carbon powder (5-15 pts. wt.), magnesium chloride (3-7 pts. wt.), bean cake (8-15 pts. wt.) and microbial agent (1-2 pts. wt.).    USE - Pollution-free organic fertilizer.    ADVANTAGE - The pollution-free organic fertilizer has simple production method, low cost, can be used for long term, increases soil organic matter, improves soil quality and improves yield and quality of agricultural products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing pollution-free organic fertilizer, which involves:    (A) crushing chicken manure, zeolite and rapeseed to 30-50 mesh;    (B) mixing the crushed materials to perform pretreatment of raw materials;    (C) carrying out aerobic fermentation for 5-8 days by mixing the obtained mixture with microbial inoculum (1-2 pts. wt.);    (D) fermenting the mixture for 2-3 days until the temperature rises to 60-65 degrees C;    (E) turning the fermenter and maintaining the temperature to 30-40 degrees C;    (F) performing stacked aging of the fermented material in indoor yard;    (G) stacking the fermented material in piles to facilitate aging process without turning;    (H) aging the fermented material till the white hypha disappears;    (I) sterilizing the aged material for 3-5 hours at 100 degrees C;    (J) adding weathered coal, humic acid, grass carbon powder, magnesium chloride, bean cake and proper amount of water;    (K) mixing and steam pelleting the obtained material; and    (L) mixing the obtained granules with soil-modifying agent to obtain the final product.
NOVELTY - Preparation of pantoprazole sodium enteric-coated composition comprises taking pantoprazole sodium, conventionally processing into granule, tablet or capsule, and applying three-layer coating i.e. alkaline protective layer, isolating layer and enteric layer respectively.    USE - Method for preparing pantoprazole sodium enteric-coated composition (claimed).    ADVANTAGE - The method is short, environment-friendly, and has less dust pollution.    DETAILED DESCRIPTION - Preparation of pantoprazole sodium enteric-coated composition comprises taking pantoprazole sodium, conventionally processing into granule, tablet or capsule, and applying three-layer coating alkaline protective layer, isolating layer and enteric layer respectively. The protective layer comprises basic film former, lubricant, opacifier, alkaline stabilizer, and solvent, where pH of the coating liquid is 8-13, preferably 10-12. The isolation layer comprises film former, lubricant, plasticizer, and opacifier, where the coating liquid pH is 7-8. The enteric layer comprises film former, plasticizer, lubricant, opacifier, stabilizer, and solvent, where the pH value of coating liquid is 5-6.
NOVELTY - Soybean or leguminous forage rhizosphere biological-bacterial fertilizer comprises rhizosphere biological bacteria separated from soybeans comprising at least three indole acetic acid (IAA) secreting soluble phosphorus bacterial strains, at least one plant hormones secretion bacterial strain with phosphorus solubilizing capability, and at least two strains of Rhizobium.    USE - The fertilizer is useful for promoting soybean pods, promoting the growth of white clover and improving nutritional content of the white clover, and promoting the growth of lotus root and improving nutritional content of the lotus root (all claimed).    ADVANTAGE - The fertilizer: activates insoluble phosphorus in the soil and can fix nitrogen in the air after applying the fertilizer; increases nitrogen and phosphorus nutrients in the soil of soybean and leguminous forage; can secrete plant growth hormone; promotes the nutrient absorption of the plants; promotes the growth of the plants; improves the nutrition structure of the plants; and increases the yield of soybean and improves the nutritional quality of the forage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the soybean or leguminous forage rhizosphere biological-bacterial fertilizer, comprising inoculating active DR19, DR9, DR24, DR4, D2, D4 bacterial strains in super optimal broth (SOC) culture medium, culturing at 26-28 degrees C under 180-200 rotations/minute under shaking condition, stopping fermentation when optical density at 600 reaches 0.5-0.8, obtaining liquid viable preparation, using a humus soil as carrier, taking active preparation through a sterile carrier absorbing culture, and packaging to obtain solid viable preparation.
NOVELTY - An F52-6 protein comprising sequence of 351 amino acids (SEQ ID NO: 2), given in the specification, is new.    USE - F52-6 protein for expression cassette, recombinant carrier, recombinant bacteria, transgenic cell line, and recombinant bacteria used for preparing xylanase, xylosidase, beta-glucosidase, and cellulase, degrading biomass e.g. corn cob (all claimed), and hydrolyzing xylan.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) F52-6 protein encoded DNA molecules;    (2) expression cassette, recombinant carrier, recombinant bacteria, transgenic cell line, or recombinant bacteria containing DNA molecule;    (3) use of F52-6 protein for xylanase, xylosidase, beta -glucosidase, or cellulase in which xylanase has optimum pH of 5 and optimum temperature of 75 degrees C; and    (4) preparation of xylanase, xylosidase, beta -glucosidase, or cellulase which involves fermenting recombinant bacteria.
NOVELTY - Preparation of carbon foam involves placing coal tar pitch into a reactor, heating at 200-300 degrees C for 0.5-10 hours, performing air oxidation process in 100-300 rpm and air flow rate of 100-1000 mL/minute, obtaining high-softening point pitch, crushing the resultant material to particle size of 5-1000 mu m, adding 1-5000 g/L organic solvent, magnetically stirring at 25-100 degrees C for 2-10 hours, filtering, drying, adding foaming agent and reinforcing agent, mixing, adding 10-500 g resultant mixture into a 0.5-5 L reactor, sealing the reactor and reacting at 300-500 degrees C for 0.5-10 hours.    USE - Preparation of carbon foam used as thermal-insulation material for building.    ADVANTAGE - The method provides carbon foam by economical process with reduced energy consumption.    DETAILED DESCRIPTION - Preparation of carbon foam involves placing coal tar pitch into a reactor, heating at 200-300 degrees C for 0.5-10 hours in rate of 5-10 degrees C/minute, performing air oxidation process in 100-300 rpm and air flow rate of 100-1000 mL/minute, obtaining high-softening point pitch, crushing the resultant material to particle size of 5-1000 mu m, adding 1-5000 g/L organic solvent, magnetically stirring at 25-100 degrees C for 2-10 hours, filtering, drying, adding foaming agent and reinforcing agent, mixing, adding 10-500 g resultant mixture into a 0.5-5 L reactor, sealing the reactor and reacting at 300-500 degrees C for 0.5-10 hours in 1-20 degrees C/minute. The weight ratio of foaming agent and high-softening point pitch is 1-20:100. The weight ratio of reinforcing agent and high-softening point pitch is 2-20:100.
NOVELTY - Aquatic ecosystem nutrient fertilizer comprises potato residue having not greater than 25% water content, protein biological fermentation agent, composite carbon source, protein nutrition water, sodium humate, nitrogen phosphorus potassium fertilizer, calcium salt and sodium salt.    USE - Aquatic ecosystem nutrient fertilizer used for sea or fresh water aquaculture (claimed).    ADVANTAGE - The fertilizer is efficient and environment-friendly, has lasting effect, no pollution, and no toxic side effect, and improves water quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer comprising pumping potato residue from starch plant through suction pipeline to organic fertilizer plant, passing through first and second pressure filter machine to a water content of not greater than 25%, entering into fermentation pool, adding protein biological fermentation agent, composite carbon source, protein nutrition water, sodium humate, nitrogen phosphorus fertilizer, calcium salt, and sodium salt, fermenting at 75 degrees C for 7 days, turning once every 24 hours, conveying to crushing machine, crushing, weighing and packaging.
NOVELTY - A diethyl ((1E,4E)-3-methyl-5-(2,6,6-trimethylcyclohex-2-en-1-yl)penta-1,4-dien-1-yl)phosphonate (I), is new.    USE - New diethyl ((1E,4E)-3-methyl-5-(2,6,6-trimethylcyclohex-2-en-1-yl)penta-1,4-dien-1-yl)phosphonate (claimed).    ADVANTAGE - The diethyl ((1E,4E)-3-methyl-5-(2,6,6-trimethylcyclohex-2-en-1-yl)penta-1,4-dien-1-yl)phosphonate is manufactured with high yield, by simple, economical and environmentally-friendly process.    DETAILED DESCRIPTION - A diethyl ((1E,4E)-3-methyl-5-(2,6,6-trimethylcyclohex-2-en-1-yl)penta-1,4-dien-1-yl)phosphonate of formula (I), is new.    An INDEPENDENT CLAIM is included for preparation of diethyl ((1E,4E)-3-methyl-5-(2,6,6-trimethylcyclohex-2-en-1-yl)penta-1,4-dien-1-yl)phosphonate (I), which involves reacting (3E)-2-methyl-4-(2,6,6-trimethylcyclohex-2-en-1-yl)but-3-enal and methylene diphosphonic acid tetraethyl ester in dipolar aprotic solvent or non-dipolar aprotic solvent and organic base at 0-30 degrees C and performing Wittig-Horner reaction.
NOVELTY - Preparing imatinib intermediate N-(5-amino-2-methylphenyl) -4-(3-pyridyl)-2-pyrimidinamine (II), comprises carrying out catalytic reduction of N-(2-methyl-5-nitrophenyl)-4-(3-pyridyl)-2-pyrimidinamine (I) in presence of a catalyst in an organic solvent to obtain final product, where the catalyst is palladium/carbon, reducing agent used for the catalytic reduction is ammonium formate, and the organic solvent is methanol or ethanol.    USE - The method is useful for preparing imatinib intermediate N-(5-amino-2-methylphenyl) -4-(3-pyridyl)-2-pyrimidinamine.    ADVANTAGE - The method: has simple operation and short reaction time; avoids use of dangerous chemical reagents when compared to existing method; and is suitable for industrial production.    DETAILED DESCRIPTION - Preparing imatinib intermediate N-(5-amino-2-methylphenyl) -4-(3-pyridyl)-2-pyrimidinamine of formula (II), comprises carrying out catalytic reduction of N-(2-methyl-5-nitrophenyl)-4-(3-pyridyl)-2-pyrimidinamine of formula (I) in presence of a catalyst in an organic solvent to obtain final product, where the catalyst is palladium/carbon, reducing agent used for the catalytic reduction is ammonium formate, and the organic solvent is methanol or ethanol.
NOVELTY - A 2-(6-hydroxy-2,3-dihydrobenzofuran-3-yl)acetonitrile compound (I) is new.    USE - 2-(6-Hydroxy-2,3-dihydrobenzofuran-3-yl)acetonitrile compound used for preparing TAK-875 (claimed).    ADVANTAGE - The method has higher yield and purity of TAK-875, and is suitable for industrial production.    DETAILED DESCRIPTION - A 2-(6-hydroxy-2,3-dihydrobenzofuran-3-yl)acetonitrile compound of formula (I) is new. INDEPENDENT CLAIMS are included for:    (1) preparation of 2-(6-hydroxy-2,3-dihydrobenzofuran-3-yl)acetonitrile compound; and    (2) preparation of fasiglifam (TAK-875) comprising taking benzyl chloride derivative of formula (i), adding aprotic solvent A, alkali A and 2-(6-hydroxy-2,3-dihydrobenzofuran-3-yl)acetonitrile compound, reacting at 50-90 degrees C to obtain 2,6-dimethylbiphenyl derivative of formula (ii), adding aprotic solvent B and alkali B and reacting at 60-100 degrees C.
NOVELTY - The utility model is new type aiming at the existing biomass gasification furnace fuel gas output carry end splitting tar in fuel gas combustion rate and low problem, have one kind environment-friendly and energy saving biomass gasification furnace, gasification furnace category field. Storage box, comprising body, a liner, tar, tar relux pipe, gas pipe, an ash room. Wherein: the storage box set on the top of the gasification furnace, the liner is located in the internal furnace body, the storage box and connected with bottom, the tar absorbing room is set with outlet on the inner container, the fuel gas pipe and tar absorbing room connecting, removing gasification process generating the tar and output the purified gas for user use. The tar relux pipe and tar absorbing room and connected with the inner container. The ash falling room equipped with bottom in the gasification furnace, the ash after collecting the biomass burning. The utility model is new type by absorbing gas output end of the tar splitting, increase fuel gas purity, so as to increase gas combustion rate. At the same time will not tar and splitting relux to circulation gasification furnace of continuous gasification combustion, increase use rate of resource, reach energy saving and environment-friendly goal.
NOVELTY - Purifying a hydrocarbon stream comprising: (a) sending the hydrocarbon stream through a lean gas absorber; (b) sending a vapor stream out a top of the lean gas absorber; (c) sending a heavier hydrocarbon portion out a bottom of the lean gas absorber; and (d) sending the heavier hydrocarbon portion to a column (16) to be separated into a light hydrocarbon portion comprising methane and ethane exiting a top of the column, a heavy hydrocarbon portion exiting a bottom of the column comprising pentanes and heavier hydrocarbons and a middle portion comprising butanes and propanes.    USE - The method is useful for purifying a hydrocarbon stream including natural gas streams of propanes, butanes, pentanes and higher hydrocarbons (claimed).    ADVANTAGE - The method: is not sensitive to carbon dioxide or water content in the feed; and is capable of processing all liquids that are formed from gas processing plants, and utilizes them as absorbing liquids to decrease the gas richness and increase overall capacity of natural gas plants and cryogenic services.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for purifying a hydrocarbon stream comprising: lean oil absorber (6) for separating a stream (24) into a vapor stream and a heavier hydrocarbon stream; a column for separating the heavier hydrocarbon stream into a vapor stream, a heavy hydrocarbon stream and a butane/propane stream; and the stripper with a side stripper reboiler (36) for removing lighter hydrocarbons from the butane/propane stream and a stabilizer reboiler (62) for stabilizing the heavy hydrocarbon stream.    DESCRIPTION OF DRAWING(S) - The figure illustrates a system for purifying a hydrocarbon stream.    Lean oil absorber (6)    Column (16)    Stream (24)    Side stripper reboiler (36)    Stabilizer reboiler (62)
NOVELTY - A fuel cell apparatus (1) has modifier (3) which modifies hydrogen-containing fuel and produces hydrogen enrichment fuel, several fuel cells (6) which produce electric power using the hydrogen enrichment fuel and an oxidizing agent, offgas combustion unit (7) which burns off gas emitted from upper end portion of the fuel cell and maintains the modifier in high temperature state, and burner (8) which burns portion of hydrogen enrichment fuel before supplied to the offgas combustion unit.    USE - Fuel cell apparatus (claimed).    ADVANTAGE - The apparatus suppresses explosive ignition by ignition delay during re-ignition after accidental fire in offgas combustion unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell apparatus. (Drawing includes non-English language text)    Fuel cell apparatus (1)    Modifier (3)    Fuel cell (6)    Offgas combustion unit (7)    Burner (8)    Ignition device (9)    Flame detector (10)    Connection port (20)
NOVELTY - The system has a circulation fluidization bed gasifier (11) that includes feeding inlet (10) for inputting biomass material inside. The fluidization bed gasifier includes air inlet for inputting the gasification medium. The fluidization bed gasifier is used for taking the biomass material gasification obtained in the following action of the gasification medium at specific temperature to oxygen-enriched combustion boiler for obtaining mixed gas. The cyclone separator (12) is connected to the circulating fluidization bed gasifier, for separating the gasification gas.    USE - Biomass gasification system for preparing oxygen-enriched combustion boiler fume.    ADVANTAGE - The energy using efficiency of the biomass gasification system can be improved. The quality of biomass gasification can be increased and the production cost can be reduced effectively. The economical efficiency of the power plant can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biomass gasification method for preparing oxygen-enriched combustion boiler fume.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of biomass gasification system for preparing oxygen-enriched combustion boiler fume.    Air separator (1)    Air pre-heater (3)    Feeding inlet (10)    Circulation fluidization bed gasifier (11)    Cyclone separator (12)
NOVELTY - The system has a circulation fluidization bed gasifier (12) that includes feed inlet for inputting the biomass material inside. The circulation fluidization bed gasifier includes air inlet for inputting oxygen-enriched combustion fume of boiler. The circulation fluidization bed gasifier is provided for oxygen-enriched combustion in the boiler fume effect for the biomass material gasification, to obtain gasification gas. The cyclone separator (13) is connected with the circulation fluidization bed gasifier, for separating the gasification gas.    USE - Biomass gasification system for preparing oxygen-enriched combustion boiler fume.    ADVANTAGE - The energy using efficiency of the biomass gasification system can be improved. The quality of biomass gasification can be increased and the production cost can be reduced effectively. The economical efficiency of the power plant can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biomass gasification method for preparing oxygen-enriched combustion boiler fume.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of biomass gasification system for preparing oxygen-enriched combustion boiler fume.    Air pre-heater (3)    Dust remover (4)    Circulation fluidization bed gasifier (12)    Cyclone separator (13)    Spray tower (14)
NOVELTY - Device comprises an entry channel (112) for receiving entry goods, at least one segment (114) of the entry channel made of a microwave-transparent material, at least one microwave applicator (116) fed with a microwave source (122) via a microwave conductor (120). The segment of the entry channel is connected with the microwave applicator to focus the entry goods into the microwave field volume. An adjustment element for adjustment of the microwave field is set in the entry goods volume.    USE - The device is useful: for entry of entry goods into a reactor; for treatment e.g. heating and/or decomposition of the entry goods, preferably entry good comprising a solid material and pyrolysis of the entry goods (hard coal, brown coal, timber and/or biomass) and/or conversion of the entry goods to a gaseous phase (claimed).    ADVANTAGE - The device: is energy-efficient; and ensures fast preheating of the goods.    DESCRIPTION OF DRAWING(S) - The figure shoes a schematic representation of the device for entry of entry goods into a reactor.    Entry channel (112)    Segment (114)    Microwave applicator (116)    Microwave conductor (120)    Microwave source (122)
NOVELTY - The system has separator (8) to separate treated water (W2) and biogas obtained in reactor (9) which carries out anaerobic treatment of natural water (W1) of process target by anaerobic microbe group. An adjustment tank (2) stored with water supplies level-adjusted water to reactor. A supply piping (1) supplies level-adjusted water to lower portion of reactor, based on dead weight of level-adjusted water from adjustment tank. A circulation piping (7) supplies circulating water which is treated water separated by separator to adjustment tank through pump (6).    USE - Waste water treatment system.    ADVANTAGE - The back flow of natural water to the circulating water drawn tube is avoided effectively by providing supply piping that supplies level-adjusted water to lower portion of reactor, and circulation piping that supplies treated water separated by separator to adjustment tank through pump. The adaptable force is heightened with respect to the rapid increase in the variation of natural water flow volume.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water treatment system. (Drawing includes non-English language text)    Supply piping (1)    Adjustment tank (2)    Pump (6)    Circulation piping (7)    Separator (8)    Reactor (9)    Natural water (W1)    Treated water (W2)
NOVELTY - A plant biology diesel oil production with transesterification device, comprising transesterification tank and heater, transesterification tank top part is set with material inlet, material outlet and steam methanol gas outlet, gas outlet and methyl alcohol methyl alcohol recovery device connected with the reaction tank and upper side wall provided with feedback input, its bottom set with discharging mouth, the discharging mouth on connected with circulation pump, circulation pump through pipeline transport reaction tank discharging mouth for discharging the material transport to heater in heating process, in later discharging opening and material outlet of reaction tank of the steam heater are connected to feed pipe, and return pipe through heater for heating the material and material steam outlet discharging the steam through the material feedback input transport to reaction tank by material and uniformly mixing, transport pipe above also has one branch for discharging pipe of the finished product material discharging. The utility model is new type circulation heating by the method, have increase reaction efficiency of transesterification, enhance have reaction and can control character, reducing have energy consumption.
NOVELTY - The new type utility claims have one kind of biomass gasification furnace, comprising a furnace body, and furnace cover pedestal, orderly set with material storage room, heat splitting room, activate indoor, heat splitting room is the cracking pool in the furnace body internal cone, and inverted cone heat splitting cone in the middle pool provided with thermal shape cutting device, provided with the scraper in thermal cracking on umbrella cutter, thermal umbrella cutter through motor drive then rotating, make the scraper after splitting for production of carbon from cone pool and the thermal cracking and thermal cracking umbrella cutter middle gap discharging to activate room, and scraper of carbon from the discharging mouth for discharging. This utility new type greatly increase have conversion rate and thermal cracking gas and biomass, with strong industrial prospect.
NOVELTY - The new type utility claims one kind peristaltic solid phase reactor, comprising furnace main body, furnace main body comprises centre tube, can be between outside wall and inside wall and centre pipe, the outer rotary body is sleeved on centre pipe outside of the forming annular cavity is capable of containing garbage, one end furnace main body is equipped with feedstock unit, the lower part main body and another end equipped with discharge unit, furnace set with supporting unit, furnace main body incline set, and with one end set with feedstock unit is formed with one end higher than the discharging unit and the inner wall of the outer cover body formed with multiple can send blade and garbage, week and these blade inner end forming discontinuous is spiral line. By splitting the furnace design and implementation primarily for decomposing garbage to the goal, structure is reasonable, suitable service, furnace main body incline, the garbage is smooth and complete discharging of to ensure quality and at the same time increase efficiency, using mode of the reactor can make the garbage splitting is sum, oil, coal, is one change process of the waste as treasure, energy regeneration, suitable for popularization and application.
NOVELTY - The utility model is new type of agricultural waste made fuel device relates to one plant fuel manufacturing device, is by drying tower, a pulverizer, hardening and tempering and extrusion forming machine composed of tank, drying tower top part has a feeding port, bottom outlet of material conveyer lifting to entrance of pulverizer, the pulverizer bottom outlet to sieving machine, a sieving bottom outlet entering into tempering tank top entrance, bottom outlet is connected with tempering tank entering into extrusion forming machine, the tail extrusion forming machine with the forming die head. The utility model is new type of agricultural waste made fuel device, it can make after smashing and agricultural wastes and extrusion forming to obtain fuel, the device manufacturing fuel and raw material has wide source, low cost, high profit, it get the fuel not only occupies small volume, high combustion efficiency and can be via become carbide block coal or fuel gas for use, to agricultural waste with more deeply and using, which avoids have agricultural waste can then use local cause burning and pollute.
NOVELTY - Ethanol or saccharide is manufactured by successively performing alkali treatment process of contacting herbal biomass and/or wood biomass and alkaline solution, pH control process of adding acid to solution or slurry and adjusting pH, and amylase treatment process of making amylase act on solution or slurry and hydrolyzing starch in solution or slurry.    USE - Manufacture of ethanol or saccharide.    ADVANTAGE - Ethanol yield can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a system for manufacturing saccharide or ethanol. (Drawing includes non-English language text).    Alkali treatment tank (1)    Solid-liquid separator (2)    Tank for pH control (3)    Amylase processing tank (4)    Tank for pH control (5)
NOVELTY - A silicon carbide photoelectrode comprises photoelectrode containing silicon carbide (13) having relatively low impurity concentration, and metal electrode used as photoelectrode and ohmic contact. The silicon carbide photoelectrode has relatively high impurity concentration between the electrodes.    USE - Silicon carbide photo-electrode used in hydrogen production apparatus (claimed) by decomposing water by light irradiation.    ADVANTAGE - The silicon carbide photoelectrode has excellent electrical resistance and improves energy conversion efficiency of the hydrolysis by light irradiation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of silicon carbide photoelectrode, which involves epitaxially growing relatively low impurity concentration silicon carbide film on a silicon carbide monocrystal substrate, forming high impurity concentration film, forming metal electrode, and removing silicon carbide monocrystal substrate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of hydrogen generation by silicon carbide photoelectrode.    Electrolyte solution storage container (11)    Counter electrode (12)    Silicon carbide (13)
NOVELTY - The device (2) has several elongated retaining elements (12,14) that are extended in parallel to a longitudinal direction (X), for forming a support surface (16) for bulk material. The retaining elements are placed side by side in a transverse direction (Y) perpendicular to the longitudinal direction by defining a gap between the retaining elements to allow the gravitating flow of portion of the bulk material. The retaining elements are moved relative to each other in translation along the longitudinal direction in opposite directions.    USE - Device for unloading bulk material e.g. lingocellulosic biomass at outlet of container e.g. storage silo or biomass torrefaction container.    ADVANTAGE - The free flow of the bulk material is enabled so that the unloading efficiency of the bulk material is improved.    DETAILED DESCRIPTION - The device comprises two endless elements (18,20) that are driven so that the retaining elements are moved in translation in the longitudinal direction relative to each other. The endless elements are wound on two shafts (26,28) and two countershafts and are co-operated with a fixed wheel (30) and an insane wheel (32) of the shafts. The endless elements are provided with a holding element and return strands (22,24) defined along a path away from the support surface. An INDEPENDENT CLAIM is included for installation comprising container for receiving the bulk material.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the device for unloading bulk material.    Device for unloading bulk material (2)    Retaining elements (12,14)    Support surface (16)    Endless elements (18,20)    Return strands (22,24)    Shafts (26,28)    Fixed wheel (30)    Insane wheel (32)    Longitudinal direction (X)    Transverse direction (Y)
NOVELTY - Improved process for the preparation of furan compound (I) comprises reaction of furan-2-carbaldehyde (II) in presence of ruthenium catalyst at 160-250 degrees C for 0.2-3 hours under hydrogen pressure of 2-30 bar in a solvent.    USE - The process is useful for preparing furan compound (claimed) that is 2,5-dimethylfuran which is a good alternative to bio-ethanol and used as fuel.    ADVANTAGE - The process: utilizes ruthenium catalyst comprising ruthenium nanoparticles alone or in combination with transition metal supported on NaY zeolite; allows 90-100 mol% conversion of (II) and provides 75-90 mol% of (I) (all claimed); utilizes a catalyst that is economical, easy to prepare, store and use, recyclable at least 5 times with no appreciable loss in activity and due to its high activity and reusability it has excellent potential for the conversion of biomass into biofuels; exhibits greater than 50 selectivity to 2,5-dimethylfuran; produces 2,5-dimethylfuran having superior properties compared to ethanol; utilizes moderate hydrogen pressure and temperature; and does not require expensive equipment.    DETAILED DESCRIPTION - Improved process for the preparation of furan compound of formula (I) comprises reaction of furan-2-carbaldehyde of formula (II) in presence of ruthenium catalyst at 160-250 degrees C for 0.2-3 hours under hydrogen pressure of 2-30 bar in a solvent.    R=CH3 or H;    R1=CH3 or CH2OH; and    R2=CH2OH or H.
NOVELTY - Mini-reactor for continuous production of biodiesel and for high efficiency transesterification of fats and oils, comprises: (a) a sinusoidal tubular thin walled structure capable of transmitting vibrations to 5 MHz; (b) a first ultrasonic cavitator over 10 MHz with a power of 50 watts at the first point of the tubular structure; (c) a second ultrasonic cavitator over 10 MHz with a power of 67 watts; (d) a third ultrasonic cavitator over 10 MHz with a power of 83 watts placed on the second point of the tubular structure; and (e) a data processor.    USE - The mini-reactor is useful for continuous production of biodiesel and for high efficiency transesterification of fats and oils.    ADVANTAGE - The mini-reactor is unique and specific to continuous production of biodiesel which is intended to achieve a near 100% maximum conversion of triglyceride to methyl esters.    DETAILED DESCRIPTION - Mini-reactor for continuous production of biodiesel and for high efficiency transesterification of fats and oils, comprises: (a) a sinusoidal tubular thin walled structure capable of transmitting vibrations to 5 MHz; (b) a first ultrasonic cavitator over 10 MHz with a power of 50 watts at the first point of the tubular structure; (c) a second ultrasonic cavitator over 10 MHz with a power of 67 watts peak positioned at the first point of the tubular structure; (d) a third ultrasonic cavitator over 10 MHz with a power of 83 watts placed on the second point of the tubular structure; and (e) a data processor capable of putting in phase the vibrations generated by the ultrasonic cavitators based on the minimization of power reflected from each cavitators.
NOVELTY - A genetically engineered microorganism having a reverse beta oxidation (BOX-R) cycle that grows a primer by adding a 2-carbon donor to it in each cycle, is new.    USE - The genetically engineered microorganism is useful for producing carboxylic acids, alcohols, hydrocarbons, amines and their alpha , beta -, and omega -functionalized derivatives.    ADVANTAGE - Provided are new approaches that could enable efficient production of second-generation biofuels.    DETAILED DESCRIPTION - A genetically engineered microorganism has a BOX-R cycle that grows a primer by adding a 2-carbon donor to it in each cycle, the BOX-R cycle comprises (a) an overexpressed thiolase that catalyzes the non-decarboxylative condensation of an acyl-CoA primer with a 2-carbon donor acetyl-CoA to produce a beta -ketoacyl-CoA; (b) an overexpressed 3-oxoacyl-(acyl-carrier-protein (ACP)) reductase or overexpressed 3-hydroxyacyl-CoA dehydrogenase that catalyzes the reduction of a beta -ketoacyl-CoA to a beta -hydroxyacyl-CoA; (c) an overexpressed 3-hydroxyacyl-(ACP) dehydratase or an overexpressed enoyl-CoA hydratase or 3-hydroxyacyl-CoA dehydratase that catalyzes the dehydration of a (3R)- beta -hydroxyacyl-CoA to a transenoyl-CoA; (d) an overexpressed enoyl-(ACP) reductase or acyl-CoA dehydrogenase or trans-enoyl-CoA reductase that catalyzes the reduction of a transenoyl-CoA to an acyl-CoA that is two carbons longer than the acyl coA primer; (i) where one of the enzymes from steps (b)-(d) is a fatty acid synthesis enzyme; (e) an overexpressed termination pathway that catalyzed the exit of an intermediate from the BOX-R cycle.
NOVELTY - A kind of horizontal biomass particle granulator, comprising power device and main machine, the main machine comprises gear box and pelleting device, the gearbox comprises gear box, transmission shaft and drive shaft, the transmission shaft and driven shaft mutually parallel, between transmission shaft and driving shaft through gear pair; the power device and transmission shaft connected with, pelleting device comprises machine shell, ring die and at least one pressure roller 1 the axial direction, axial direction of ring module and mutual axial direction of drive shaft of pressure roller parallel; and ring mould and the axis is vertical and direction. And the ring die in position in housing, internal space of housing is ring mould into two separate two area, that is, the region outside the material extrusion area and ring mould inner ring die, material extrusion area and feedstock wherein connection, and discharging mouth are connected with the lower driving shaft in driving, pressure roller and ring module rotate speed, pressure roller in material extrusion area. All local bearing of ball/roller uniformly stressed. Spiral feeder level forced feeding into vertical gravity feeding, feeding no need power.
NOVELTY - A longer life plant biomass particle granulator, comprising motor and main machine, main machine comprises gear tank and pelletizing device; between gearbox comprises gear box, transmission shaft and driven shaft, transmission shaft and driven shaft by gear pair; electric machine and transmission shaft through transmission mechanism connected with, pelleting device comprises machine shell, ring die and at least 1 of compression roller, the ring die in position in housing, internal space of housing is ring mould into two separate two area, material extrusion area and feedstock wherein connection, and discharging mouth are connected; the outer diameter of compression roller and ring module rotate speed, compression roller ring mould is less than inner diameter of between pressure roller extrusion region, electric machine and transmission shaft in the material transmission mechanism is belt wheel or chain wheel, and axis direction of ring mould is vertical and, one end output shaft, transmission shaft of the motor and connected with belt wheel, between the belt pulley through belt connected with two, or, one end output shaft, transmission shaft of the motor and connected with chain wheel, between two chain wheel through chain connection.
NOVELTY - A plant for granule cutting machine of biomass particle granulator, comprising, scraper and scraper drive device, bottom of the barrel cover is opened with the first through hole, inner diameter of opening end of the barrel cover is large ring die outside diameter of biomass particle granulator, a scraper driving device comprises motor, large gear and large gear connecting rod, large gear connecting rod has one more, they connected at bottom of barrel cover, the end of each connecting pole and connected with " T "-shaped roller shaft, large gear and centre is opened with the second through hole, the second through hole and hole diameter is not less than the first through hole and hole diameter, provided with section is inverted T-shaped and annular groove, " T "-shaped roller shaft is embedded in inner annular groove, and " T "-shaped roller shaft is embedded and annular groove sliding connected with upper on one side of the gear, scraper connection up at another one side of large gear of the gear between the scraper ring die on the biomass particle granulator outside wall and barrel cover inner wall rotate, track of the scraper blade is one of annular, and the annular and biomass particle granulator and ring die and outside wall of corresponding position.
NOVELTY - The utility model is new type supply have one A garbage carbonization reaction system, comprising a reaction kettle, reaction tank, a steam generator and control device, wherein, a steam generator connected with the reaction kettle, the steam generator to the reaction kettle for providing steam, the reaction tank for placing garbage, when reaction time, the reaction tank for pushing the reaction kettle generating carbonizing reaction mixture, after reaction is finished, when using the reaction tank from the reaction kettle in; The reaction kettle comprises kettle body and kettle cover, the kettle body and the kettle cover sealing connected with, the control device connected with the reaction kettle, the control device used for control change and reaction time and temperature and pressure of the reaction kettle, in the kettle body set with the first guide rail along the length direction of the extending of the kettle body. The utility model is new type construction scheme is reasonable, equipment is advanced, the automatic degree high, equipment investment cost low, plant needed square meter floor space small, and prepare biomass fuel combustion value is high, low discharge.
NOVELTY - The utility model is new type relates to one kind biomass carbonizing and cooling purification integrated device, comprising bracket, heat source and set on bracket on the carbonizing cylinder, upper part of carbonization cylinder with feedstock wherein, heat source for heating carbonizing, wherein also comprising cooling cylinder and filtering cylinder, a cooling cylinder by smoke tube and carbonization cylinder connected, by sum and filter cylinder connected tube, internal cooling cylinder is provided with multiple pieces of cooling pipe, upper cooling cylinder and set with water inlet and water outlet of said cooling pipe connected, lower part of cooling cylinder is set with tar exit, filter cylinder and discharge pipe connected, and filter cylinder filter object. Carbonizing production in biomass raw material in carbonizing furnace and fume enter into cooling cylinder cooling, cooling cylinder for tar from fume and separation, realize have recovery using the tar, then fume and non condensed sum then enter into the filtering cylinder through filtering purification after again outward discharge, discharge accord with ring heat preservation requirement, protect have environment.
NOVELTY - The new type utility claims have one plant with water cool wall and integrated garbage plasma gasification furnace, gasification furnace hearth divided synthesis sum reforming on part of the gasification area and lower slag melting area, synthesis sum reforming cell is in middle part on the same one horizontal plane at uniformly provided with three supporting plasma torch A, side face and feedstock and gasifying system connected, also set with side air inlet, bottom for bearing the garbage is set with grate, the waste side face the middle slag melting area is set with three of the plasma around , the utility new type can make convention gasification, synthesis sum reforming and slag melt in one gasification furnace in the whole, the whole structure is simple and compact, can increase whole gasification device running efficiency and stability, full using waste heat firstly carrying out convention by gasification, using plasma torch consume can greatly reduce, increase have economical efficiency of whole system operation, water cold wall can reducing refractory material usage, at the same time prolongs using life of fireproof material, recovery part wall and loss of energy.
NOVELTY - The new type utility claims have one plant biomass gasification sum tar removing device, comprising shell, snake-shaped pipe and oil collecting tank, the snake-shaped pipe is set in shell, said oil collecting tank is set on shell, and the oil collecting tank is snake-shaped pipe and; also comprises tube wall scraping module, collected oil pool oil scraper component and tar out module. The utility model is new type biomass gasification tar removing device comprises sum without second time pollute, safety and environment-friendly, low cost, using suitable equal.
NOVELTY - Chemical conversion of agricultural and forestry waste comprises adding agricultural and forestry waste into carbonization furnace and heating to obtain primary carbon, combustible gas, gaseous tar and gaseous wood vinegar; taking primary carbon, adding combustible agent, mixing, extruding molding, and drying to obtain eco-charcoal; taking combustible gas, gaseous tar and wood vinegar and separating using cyclone dust removal system; adding resulting combustible gas into gas generation system and adding gaseous tar into cooler; and taking gaseous wood vinegar and secondary cooling.    USE - Method for chemical conversion of agricultural and forestry waste (claimed).    ADVANTAGE - The method is simple.
NOVELTY - Preparing artificial coal using domestic rubbish and domestic sludge comprises mixing processed straw, waste asphalt, domestic sludge and household rubbish, adding water and stirring uniformly, and pressing. The processing method comprises smashing straw, smashing the waste asphalt, deodorizing raw sludge, modifying, pressure filtering, dehydrating, drying, smashing, deodorizing and sterilizing domestic rubbish, removing metal objects using a magnetic separator, using a sieve to remove fine material, after removing out, subjecting to plastic winnowing, drying and smashing the residual sludge.    USE - The artificial coal is useful in burning kiln-bricks and industrial heating processes (claimed).    ADVANTAGE - The artificial coal has high calorific value.    DETAILED DESCRIPTION - Preparing artificial coal using domestic rubbish and domestic sludge comprises mixing 10-80 pts. wt. processed straw, 10-20 pts. wt. waste asphalt, 10-80 pts. wt. domestic sludge, and 10-80 pts. wt. household rubbish, adding water and stirring uniformly, and pressing under 15-20 MPa condition. The processing method comprises smashing straw into particle diameter of less than 5 mm, smashing the waste asphalt into particle diameter of less than 5 mm, deodorizing raw sludge, modifying, pressure filtering, dehydrating, drying until water content is 20% or less, smashing, deodorizing and sterilizing domestic rubbish, removing metal objects using a magnetic separator, using a sieve to remove fine material having particle diameter of less than 50, after removing out, subjecting to plastic winnowing, drying and smashing the residual sludge into particle diameter of less than 5 mm. An INDEPENDENT CLAIM is also included for artificial coal prepared by the above mentioned method.
NOVELTY - The fermentation method of food waste involves taking food waste and then filtering, drying the food waste and then crushing, adding Aspergillus niger spore liquid to the food waste, filtering the mixture and then drying, fermenting the mixture for 5 days and then stirring, separating the mixture for 12 hours, adding saccharifying enzyme, tap water and lactic acid to the mixture and then fermenting at 45 degrees C for 25 hours to obtain a fermented liquid, solid liquid separating the fermented liquid and then desalinating using water, and purifying.    USE - The method is useful for fermentation of food waste (claimed).    DETAILED DESCRIPTION - The fermentation method of food waste involves taking food waste and then filtering, drying the food waste with a diameter of less than 1.5 cm3 and then crushing, adding 16-17 spore/ml or 8 %mass Aspergillus niger spore liquid to the crushed food waste, uniformly mixing, filtering the mixture and then drying at 32 degrees C, fermenting the mixture for 5 days and then stirring, separating the mixture for 12 hours, adding 2.5 %mass saccharifying enzyme with a particle diameter of less than 0.1 cm, tap water and 7-8 %mass lactic acid to the mixture and then fermenting at 45 degrees C for 25 hours to obtain a fermented liquid, solid liquid separating the fermented liquid and then desalinating using water, and purifying. Aspergillus niger is Aspergillus niger UV448 or Lactobacillus plantarum TD175. Lactic acid has a moisture content of 75-85%.
NOVELTY - Preprocessing of lignocellulosic biomass involves providing wood-based biomass, reacting wood-based biomass and calcium chloride solution in fermentable sugar at 150-170 degrees C, fermenting, separating leachate and solid residue, extracting, and recovering resultant product.    USE - Preprocessing of lignocellulosic biomass (claimed).    ADVANTAGE - The method enables effective preprocessing of lignocellulosic biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for preprocessing of lignocellulosic biomass.
NOVELTY - The method involves comparing amount of fluorescence measured with amount of fluorescence measured in similarly tested fuel contained prescribed maximum allowable amount of waterborne chloride ions. Fuel for use in an engine is accepted if amount of measured fluorescence corresponds to measured fluorescence emission for fuel that does not comprise greater than prescribed maximum allowable amount of waterborne chloride ions, where first wavelength falls within excitation spectrum of fluorescence spectra and second wavelength falls within emission spectrum of fluorescence spectra.    USE - Method for providing liquid hydrocarbon fuel i.e. hydrocarbon fuel e.g. diesel, jet fuel, kerosene, petroleum, ethanol and biofuel (all claimed), aviation fuel, paraffinic, naphthenic, heavy fuel oils, waste oils e.g. esters, poly alpha olefins, lubricant oils, hydraulic fluids and gear oils for use in an engine for automobiles and lorries.    ADVANTAGE - The method enables detecting salts present in part per billion levels, so that chance for interference of test is minimal.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for producing jet fuel by merox treatment process.
NOVELTY - Operation of blast furnace involves inserting an iron ore and corks into blast furnace, blowing powdered coal from tuyere normally from furnace top to inside, blowing coke oven gas and/or natural gas in with powdered coal from the normal tuyere, blowing in the reformed furnace top waste gas obtained by removing carbon dioxide and water vapor of the blast furnace from furnace top waste gas in furnace from the normal tuyere and/or shaft portion tuyere.    USE - Operation of blast furnace used in pig-iron manufacture.    ADVANTAGE - The method enables long term operation of blast furnace by significantly reducing carbon dioxide discharge amount, and enables stable manufacture of pig-iron.
NOVELTY - Composite sealant comprises a glass frit prepared by melting metal oxide mixture (I) and barium disilicate crystallized filler synthesized by using silicon oxide and barium oxide.    USE - The composite sealant is useful for producing solid oxide fuel cell (claimed).    ADVANTAGE - The sealant induces or inhibits crystal formation during working operation, has improved strength, structural stability, excellent long-term reliability, thermal expansion coefficient, and electrical insulation effect.    DETAILED DESCRIPTION - Composite sealant comprises a glass frit prepared by melting metal oxide mixture formula of (R1O2-R22O3-R3O) (I) and barium disilicate crystallized filler synthesized by using silicon oxide and barium oxide.    R1 = Si, Zr, Ti;    R2 = Al, La; and    R3 = Ba, Ca, Sr.    An INDEPENDENT CLAIM is also included for producing composite sealant, comprising (a) melting a metal oxide mixture at 1450 degrees C to produce glass frit, (b) synthesizing barium disilicate crystallized filler using silicon oxide-barium oxide and glass to produce filler mixed composite sealant, (c) mixing crystal filler with the glass to produce composite sealant, (d) thermal cycling the composite sealant to determine physical properties change under oxidizing atmosphere and reducing atmosphere for 0, 100, 300 and 500 hours, and checking a change in the bending strength values, (e) mixing the composite sealant powder with 30 wt.% binder mixed vehicle, stirring the mixer using high-speed mixture for 30 minutes, milling the stirred slurry using a three-roll mill, degassing by using a vacuum pump to prepare a paste, and dispensing the paste on a shear connector to form coating type composite sealant. The binder is nitrocellulose. The organic solvent is alpha terpineol/butyl carbitol acetate.
NOVELTY - Producing biofuel from lignocellulosic biomass and starch involves reducing lignocellulosic biomass. The amylolytic microorganisms are added to wort for carrying out fermentation to produce and modulate the production of enzymes that degrades lignin, cellulose and hemicellulose at temperature 10-80 degrees C and pH 2-12. Bacillus is fermented at temperature 10-50 degrees C and Saccharomyces is fermented at temperature 10-50 degrees C. The alcohol is extracted to obtain biofuel.    USE - Method for producing biofuel from lignocellulosic biomass and starch (claimed).    ADVANTAGE - The method enables to produce biofuel from lignocellulosic biomass in eco-friendly and cost-effective manner by eliminating acid hydrolysis or enzymatic hydrolysis.
NOVELTY - Method for producing biochar mass, involves introducing a biomass to a reactor, and heating the biomass in the reactor in accordance with a predetermined set of operating parameters attuned to the biomass to produce a stable biochar core, where the heating is done in an aqueous solution under oxygen deficient conditions.    USE - The method is useful for producing biochar mass (claimed).    ADVANTAGE - The method enables to allow for synergistic remediation and resource generation on-site.
NOVELTY - The system (100) has a pyrolysis chamber that includes a feedstock outlet and pyrolysis solid processing device that is connected with a solid outlet. A cooling and purification device is provided with a gas outlet connected to pyrolysis chamber. An oil storage tank is connected with cooling and purification device, rotary heat accumulating type heat exchanger and regenerative rotary heat exchanger. The cooling and purification device is connected with hot air inlet of rotating bed pyrolysis furnace, for taking non-condensable gas after carrying out pyrolysis heating process.    USE - Pyrolysis system for performing pyrolysis process of to-be-pyrolysis raw material such as coal, biomass, waste material, waste tire, waste organic substance and organic sludge (all claimed).    ADVANTAGE - The pyrolysis system can obviously increase thermal efficiency and pyrolysis efficiency of the pyrolysis material. The energy consumption of the pyrolysis system is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the illustrating the pyrolysis process of pyrolysis chamber.(Drawing includes non-English language text)    Pyrolysis system (100)
NOVELTY - Producing methane by hydraulic turbulent stirring ultra-efficient methane generation system comprises pouring the fermentation raw material into a fermentation system to produce biogas by providing a space as fermentation area between the collection feed tube/discharge tube side wall and adjacent air resistance plate, passing the biogas into biogas feedstock flow tube, a discharge tube, a cloth device tube and into hydraulic pressure chamber in a unidirectional flow, increasing the pressure of fermentation area using one biogas area, refluxing the biogas in fermentation pipeline.    USE - The method is useful for producing methane by hydraulic turbulent stirring ultra-efficient methane generation system (claimed).    DETAILED DESCRIPTION - Producing methane by hydraulic turbulent stirring ultra-efficient methane generation system comprises pouring the fermentation raw material into a fermentation system to produce biogas by providing a space as fermentation area between the collection feed tube/discharge tube side wall and adjacent air resistance plate, passing the biogas into biogas feedstock flow tube, a discharge tube, a cloth device tube and into hydraulic pressure chamber in a unidirectional flow, increasing the pressure of fermentation area using one biogas area, refluxing the biogas in fermentation pipeline within the hydraulic pressure chamber through feedstock flow tube, discharge tube and cloth device tube, decreasing the pressure of fermentation area, completing the biogas slurry circulation, repeating the step in other fermentation area.
NOVELTY - Cogeneration of biogas using molasses and straw waste involves taking 20-70% straw and then crushing using a pulverizer into powder with a length of 1-2 cm, treating the powder using diluted hydrochloric acid for 5-10 hours and then neutralizing using sodium hydroxide, adding molasses to the neutralized powder, uniformly mixing, transferring the mixture to a pool, and carrying out anaerobic fermentation at 40-50 degrees C for 20-30 days.    USE - The method is useful for cogeneration of biogas using molasses and straw waste (claimed).
NOVELTY - A glucose optical nanosensor preparing method involves utilizing graphite oxide prepared by Hummers GO, preparing dark brown gold nano cluster, and amino-functionalized graphite oxide solution. The prepared gold clusters and amino-functionalized graphite oxide are added in PBS, mixing by shock, to obtain aqueous solution of composite material, and lyophilized to give powder, followed by dissolving powder in PBS added oxidase specific substrate, and measuring fluorescence intensity of the reaction solution after the shock.    USE - Method for preparing glucose optical nanosensor.    ADVANTAGE - The optical sensor can be prepared with and great practical value in simple, and pollution-free manner.    DETAILED DESCRIPTION - A glucose optical nanosensor preparing method involves utilizing graphite oxide prepared by Hummers GO. Droplets chloroauric acid is added to aqueous solution of bovine serum albumin in water bath at 35-37 degrees C, alkaline solution is added to adjust the pH value to obtain dark brown gold nano cluster AuNCs. The ultrasonic dispersed graphite oxide is added into a secondary distilled water and to the phosphate buffer solution, and 1-(3-dimethylaminopropyl)-3-ethylcarbodiimide EDC solution, reacted for 1-3 hours, after a certain amount of activator is added at room temperature and ethylenediamine at 25 degrees C, stirred, dialysis remove excess ethylene diamine to give amino-functionalized graphite oxide solution GO-NH2. The prepared gold clusters and amino-functionalized graphite oxide are added in PBS, mixing by shock, to obtain aqueous solution of composite material AuNCs/OXI GO-NH2, which has been configured OXI oxidase solution added to an aqueous solution of the composite material, thoroughly mixed, and lyophilized to give AuNCs/OXI OGO-NH2 powder, followed by dissolving AuNCs/OXI OGO-NH2 powder in PBS added oxidase specific substrate, and measuring fluorescence intensity of the reaction solution after the shock.
NOVELTY - The invention relates to a hauled mechanical-hydraulic equipment for preparing compost and plant biomass, to be applied in the field of sustainable agriculture, for preparing the compost to be used as ecological fertilizer and in the field of renewable energy, for preparing the plant biomass as a source of alternative energy, and which, using simple innovative technical solutions exclusively based on classic components of general use, eliminates the mechanical drive and the need of bedframe tilting and achieves a homogeneous drive of the equipment working mechanisms only with hydrostatic energy taken from the hydraulic system of the tractor used by the equipment. According to the invention, the equipment mainly consists of a bedframe (BAT) on which the working mechanisms are mounted, as follows: a main mechanism (MPC) for compost preparation and overturning, having as a working member a compost preparation drum (TPC) on which there are some working blades (APC) located on the path of two propellers of opposite winding sense/angle along the axis, the drum (TPC) being driven by some mechanisms (MAT) for driving the drum from some rotary hydraulic engines (MHR1 and MHR2); two integrated lifting and rolling mechanisms (MRR) located on the side walls of the bedframe (BAT) in diagonally-opposite positions, each of them comprising an oscillating bar (29) articulated, at one end, to the bedframe (BAT) and having, at the other end, a ball bearing (33) on the shaft (34) of which a pneumatic tyre wheel (35) is mounted, between which there is articulated the rod of a hydraulic cylinder (CH1 or CH2) which has the body articulated to the bedframe (BAT), as well as a tiltable hauling mechanism (MRT) employed for the equipment motion while operating or to the workplace.
NOVELTY - The complex structure has a mixer that is installed before a reactor of biological gas. An inclined container which is made in the form of a tray is provided with partitions on the bottom portion. A gas-sampling branch pipe is placed on a lid of support case. A channel for selection of worked out feedstock is made in the form of retractable branch pipe. A bunker-receiving box is connected with a water lock. The branch pipe is connected with a mixer which enriches initial slurry by the methane-forming microorganisms.    USE - Complex structure for processing feedstock with organic components.
NOVELTY - A succinic acid producing method involves culturing an Enterobacter in a medium with glycerol and lactose as base material, followed by separating supernatant from the biomass to produce succinic acid.    USE - Method for producing succinic acid from Enterobacter culture medium.
NOVELTY - 4,6-Dihydro-benzo(h)tetrazole(5,1-b)quinazoline-7-8-diketone (I) is new.    USE - Compound (I) used for treating cancer.    ADVANTAGE - The compound (I) uses readily available raw materials, and has simple, high yield and environment-friendly manufacturing method.    DETAILED DESCRIPTION - 4,6-Dihydro-benzo(h)tetrazole(5,1-b)quinazoline-7-8-diketone of formula (I) is new. An INDEPENDENT CLAIM is included for the preparation of compound (I).
NOVELTY - Wood structure anaerobic power supply station comprises an anaerobic tank unit, a purification tower, an anaerobic tank warming system, a power generation unit (13), an anaerobic tank construction material (24), a steel column beam frame structure (19) and a wood structure construction. Anaerobic tank body is cylinder. The tank body is steel mixing structure. Feeding anaerobic tank comprises a material pipe (23), a distributor, a sealing door (22) and a secondary anaerobic tank. Power generation unit comprises water tank, engine and electric generator.    USE - Wood structure anaerobic power supply station.    ADVANTAGE - The wood structure anaerobic power supply station saves raw material, protects environment, and has increased efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of wood structure anaerobic power supply station.    Power generation unit (13)    Steel column beam frame structure (19)    Sealing door (22)    Material pipe (23)    Anaerobic tank construction material (24)
NOVELTY - Device comprises feeding pipe (11) and discharge pipe (12). The raw material is fed into feeding pipe and then marsh gas is collected at feeding pipe. The blocking plate (24) is present between the feeding pipe and the discharge pipe. The feeding pipe is provided with pipe drainage hole (40) and inner discharging pipe drainage hole. The discharge pipe is provided with discharging pipe drainage hole. The biogas is stored at fermented biogas slurry area. The fermented biogas slurry area is provided with fermentation tube (20).    USE - Device used for producing biogas (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biogas production device.    Feeding pipe (11)    Discharge pipe (12)    Fermentation tube (20)    Blocking plate (24)    Pipe drainage hole (40)
NOVELTY - Producing methane gas involves feeding raw material into feeding pipe (40) to produce methane gas in fermentation system. The methane gas is collected in fermentation zone, which is formed between adjacent block plates (34). When gas pressure is increased in fermentation system liquid is flowed in feeding pipe and discharge pipe. The liquid pressure is increased in feeding tube and then liquid is flowed into discharge pipe (20) and drain pipe (44) to the lowest position.    USE - Method for producing methane gas (claimed).    DETAILED DESCRIPTION - Producing methane gas involves feeding raw material into feeding pipe (40) to produce methane gas in fermentation system. The methane gas is collected in fermentation zone, which is formed between adjacent block plates (34). When gas pressure is increased in fermentation system liquid is flowed in feeding pipe and discharge pipe. The liquid pressure is increased in feeding tube and then liquid is flowed into discharge pipe (20) and drain pipe (44) to the lowest position. When liquid pressure is reduced in fermentation system, liquid is flowed into feeding pipe, discharging pipe, drain pipe and reflux pipe to pipe (30) inside fermentation system. The liquid is collected into other fermentation system to obtain methane gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of methane gas production method.    Discharge pipe (20)    Pipe (30)    Block plates (34)    Feeding pipe (40)    Drain pipe (44)
NOVELTY - Preparing short chain fatty acid involves adding copper sulfate into sludge to obtain mixture. The mixture is fermented in anaerobic condition to obtain fermentation material, where mixture pH is adjusted to alkaline. The fermentation material is separated to obtain short chain fatty acid.    USE - Method for preparing short chain fatty acid (claimed).    ADVANTAGE - The method enables to prepare short chain fatty acid that requires low dose of copper sulfate.
NOVELTY - Anaerobic digestion of hogpen wastewater, involves solid-liquid separation, acidification, anaerobic fermentation, aeration, and secondary biological purification.    USE - The method is useful for anaerobic digestion of hogpen wastewater to produce biogas for use as domestic fuel.    ADVANTAGE - The method removes 90% chemical oxygen demand. The processed wastewater can be used as agricultural fertilizer, or for farmland irrigation and aquaculture.
NOVELTY - Conversion of ethane to liquid fuels, involves: (a) directing an ethane stream into a thermal activation unit in a first stage to produce an intermediate hydrocarbon stream and a raw ethylene stream; (b) combining the raw ethylene stream with a raw ethanol stream to form a mixture, where the raw ethanol stream is derived from biomass; (c) contacting the mixture with a catalyst to produce a mixed product stream; and (d) separating the mixed product stream to produce an intermediate hydrocarbon stream comprising hydrocarbons.    USE - The process is useful for converting ethane to liquid fuels (claimed).    ADVANTAGE - The process can efficiently co-convert ethane and biomass-derived ethanol to liquid hydrocarbons fuels, and allows incorporation of increased quantities of biomass-derived ethanol into gasoline, while preserving the ability to utilize the resulting fuel in all gasoline-powered vehicles and maintaining the Reid vapor pressure of the fuel at acceptable levels.    DETAILED DESCRIPTION - Conversion of ethane to liquid fuels involves: (a) directing an ethane stream into a thermal activation unit in a first stage to produce an intermediate hydrocarbon stream and a raw ethylene stream comprising less than 60 wt.% ethylene; (b) combining the raw ethylene stream with a raw ethanol stream to form a mixture, where the raw ethanol stream is derived from biomass and comprises at least 4 vol.% water; (c) contacting the mixture with a catalyst to produce a mixed product stream comprising an increased percentage of hydrocarbons containing four or more carbon atoms; and (d) separating the mixed product stream to produce an intermediate hydrocarbon stream comprising hydrocarbons containing four or more carbon atoms and a light hydrocarbon stream comprising hydrocarbons containing from one to three carbon atoms.
NOVELTY - Producing biohydrogen, comprises (a) preparing an electrochemically active biofilm (EAB) on a support by adding an anaerobic sludge under anaerobic conditions after impregnating the support in an inorganic salt medium containing an electron donor; and (b) producing metal nanoparticles by impregnating the prepared EAB in a solution containing metal precursor and the electron donor under anaerobic conditions and simultaneously preparing hydrogen by using the metal nanoparticles as a catalyst.    USE - The method is useful for producing biohydrogen (claimed).    ADVANTAGE - Biohydrogen does not require any hazardous chemicals and external energy input and can be manufactured using EAB, electron donor and (+) charged metal nanoparticles, and effectively achieves a total hydrogen yield of 44%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for biohydrogen produced by the above method.
NOVELTY - Invention refers to producing industrial ethanol. The method provides milling lignocellulosic raw material at two stages, at the first stage - to a particle size of no more than 20 x 20 x 5 mm, at the second stage - to a particle size of no more than 50 mcm, mixing the milled raw material with 5% sulphuric acid to produce a batch, performing flow ultrasound treatment of the latter, saccharifying with enzyme preparations, thermostating at 45-55 degrees C, fermenting and recovering the alcohol from fermentable wort by distillation.    USE - Chemistry.    ADVANTAGE - Invention enables increasing the alcohol yield and reducing the production-related energy consumption.1 tbl
NOVELTY - Green organic fertilizer comprises 40-50 pts. wt. animal manure, 80-90 pts. wt. vegetable cake product, 35-42 pts. wt. diammonium phosphate, 15-18 pts. wt. peanut shell, 28-33 pts. wt. soybean cake product, 12-18 pts. wt. larch, 8-15 pts. wt. biological enzyme, 33-45 pts. wt. plant ash, 20-26 pts. wt. Chinese herbal medicine and 0.5-4 pts. wt. leavening agent.    USE - Green organic fertilizer used for crop.    ADVANTAGE - The green organic fertilizer is eco-friendly, increases crop yields, and avoids pollution caused by spraying of pesticides.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing green organic fertilizer, which involves:    (A) crushing animal manure, vegetable cake product, peanut cake product and larch by using a pulverizer    (B) adding plant ash, biological enzyme and leavening agent with the product, and then adding water (5-15 times) to carry out fermentation for 15-25 days; and    (C) adding remaining components with the fermented product, and then granulating to obtain final product.
NOVELTY - Preparation of 3-methyl-4-oxo-4-(p-amino)phenyl-butyric acid (I) includes reacting p-nitrobenzoic acid (A) with dioxane compound (B) in the presence of dicyclohexylcarbodiimide and N,N-dimethylaminopyridine to obtain nitro-containing compound (II); reacting with methyl iodide in sodium ethoxide to prepare dimethyl-containing compound (III); reacting with ethanol to prepare ethoxy-containing compound (IV); reacting with bromoacetic acid in sodium ethoxide to prepare carbonyl-containing compound (V); and reacting with sodium hydroxide in the presence of hydrochloric acid.    USE - Preparation of 3-methyl-4-oxo-4-(p-amino)phenyl-butyric acid (I) (claimed) used as levosimendan intermediate.    ADVANTAGE - The method uses easy to obtain raw materials, is environment-friendly and suitable for safe industrial production, does not use toxic chemicals and has high yield in each reaction step, high total yield and simple operation.    DETAILED DESCRIPTION - Preparation of 3-methyl-4-oxo-4-(p-amino)phenyl-butyric acid of formula (I) comprises:    (A) reacting p-nitrobenzoic acid of formula (A) with dioxane compound of formula (B) in the presence of dicyclohexylcarbodiimide and N,N-dimethylaminopyridine to obtain nitro-containing compound of formula (II);    (B) reacting with methyl iodide in sodium ethoxide to prepare dimethyl-containing compound of formula (III);    (C) reacting with ethanol to prepare ethoxy-containing compound of formula (IV);    (D) reacting with bromoacetic acid in sodium ethoxide to prepare carbonyl-containing compound of formula (V);    (E) reacting with sodium hydroxide in the presence of hydrochloric acid to prepare carboxy-containing compound of formula (VI); and    (F) hydrogenating in the presence of nickel catalyst to prepare (I).
NOVELTY - A high purity neomycin A4 is prepared by filtering neomycin A4 liquid at room temperature to obtain mycelium, extracting silk body, solid-liquid separating with polar solvent to obtain neomycin A4 extract, decompression concentrating extract, extracting with ethyl acetate, concentrating extracting liquid, drying to obtain neomycin A4 powder, adding with organic solvent, dissolving, filtering in filter film to obtain sampling liquid, adding to medium pressure chromatography column (C18), adding elution solvent, collecting HPLC content, decompression concentrating, filtering, and vacuum drying.    USE - Preparation of high purity neomycin A4 for preparation of antibacterial medicine.    ADVANTAGE - The preparation effectively eliminates secondary fermentation, has short preparation time and strong controllability, and obtains product which has high purity and good antibacterial effect for Enterococcus and Staphylococcus.    DETAILED DESCRIPTION - A high purity neomycin A4 is prepared by filtering neomycin A4 liquid at room temperature to obtain mycelium, extracting silk body, solid-liquid separating with polar solvent to obtain neomycin A4 extract, decompression concentrating extract to obtain concentrated liquid, extracting with ethyl acetate, concentrating extracting liquid, drying to obtain neomycin A4 powder, adding powder with organic solvent, dissolving, filtering in 0.45 mu m filter film to obtain sampling liquid, adding sampling liquid to medium pressure chromatography column (C18), adding elution solvent, collecting HPLC content having greater than or equal to 98.5% removing liquid, decompression concentrating, filtering, and vacuum drying.
NOVELTY - Preparation of sofosbuvir (I) comprises taking uridine as starting material, etherifying with 1,3-dichloro-1,1,3,3-tetraisopropyl-1,3-disiloxane to obtain 3',5'-oxo-(tetraisopropyl disiloxane-1,3-diether) uridine, oxidizing to obtain 2'-carbonyl-3',5'-oxo-(tetraisopropyl disiloxane-1,3-diether) uridine, adducting carbonyl and hydrolyzing to obtain 2'S-2'-hydroxymethyl uridine, selectively protecting to obtain 2'S-2-methyl-3',5'-di-(oxo-pivaloyl) uridine, fluorinating and deprotecting to obtain 2'R-2'-deoxy-2'-fluoro-2'-methyl-urea glycoside, and condensing.    USE - Method for preparing sofosbuvir (claimed).    ADVANTAGE - The economical and environment-friendly method has easy-to-obtain raw materials, simple technique, and is suitable for industrial production.    DETAILED DESCRIPTION - Preparation of sofosbuvir of formula (I) comprises taking uridine as starting material, etherifying with 1,3-dichloro-1,1,3,3-tetraisopropyl-1,3-disiloxane to obtain 3',5'-oxo-(tetraisopropyl disiloxane-1,3-diether) uridine, oxidizing to obtain 2'-carbonyl-3',5'-oxo-(tetraisopropyl disiloxane-1,3-diether) uridine, adducting carbonyl and hydrolyzing to obtain 2'S-2'-hydroxymethyl uridine, selectively protecting to obtain 2'S-2-methyl-3',5'-di-(oxo-pivaloyl) uridine, fluorinating and deprotecting to obtain 2'R-2'-deoxy-2'-fluoro-2'-methyl-urea glycoside, and condensing.
NOVELTY - The method involves covering the connecting portion of rotation shaft (8) and rotating blades (9a) of stirring apparatus by coating elements (13a). The medium for removal, such as to-be-processed liquid, sewage gas, nitrogen, or carbon dioxide is supplied to rotation shaft, by reversely rotating the stirring apparatus at the time of normal driving for every fixed period. The sewage residue twining round the stirring apparatus is removed, by discharging the medium for removal from the opening portions (14a-14c) of coating element via the opening portion of rotation shaft.    USE - Method for removing sewage residue twining round stirring apparatus in methane fermentation tank (claimed).    ADVANTAGE - The sewage residue twining round the stirring apparatus in methane fermentation tank can be removed effectively. The power consumption required for sewage residue removal operation can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for methane fermentation tank.    DESCRIPTION OF DRAWING(S) - The drawing shows an enlarged view of the coating element. (Drawing includes non-English language text)    Rotation shaft (8)    Rotating blade (9a)    Coating element (13a)    Opening portions (14a-14c)
NOVELTY - Preparation of sawdust soil free cultivation matrix comprises adding sawdust into water, saturating, adding 1-3 kg iron sulfate/cm3 sawdust and 0.5-1.5 kg urea/cm3 sawdust, mixing to distribute uniformly, and open-air fermenting for 40-60 days.    USE - Method for preparation of sawdust soil free cultivation matrix (claimed).
NOVELTY - The system has a boiling bed reactor connected with a gas-solid separator. Ecological oil is formed on a double-level spray tower. A drying furnace is connected with the boiling bed reactor that is arranged with a pneuma outlet. The gas-solid separator is arranged with the pneuma outlet and connected with the double-level spray tower that is arranged with a pneuma entrance. The double-level spray tower is arranged with the pneuma outlet. The drying furnace is arranged with a hearth. A bottom of the boiling bed reactor is provided with a pressure air blower.    USE - Biomass liquefied system.    ADVANTAGE - The system realizes slow gasification reaction, increases splitting gas production rate, reduces carbon in pneuma, saves secondary reactor and ensures system operation safety.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a biomass liquefied system.'(Drawing includes non-English language text)'
NOVELTY - Preparation of bran extract amino acid water-soluble fertilizer comprises taking waste bran, fermenting at 60 degrees C, adding microbial agent, extracting, soaking in water for 3-4 hours, separating, filtering, mixing, centrifuging and concentrating.    USE - Method for preparing bran extract amino acid water-soluble fertilizer (claimed).    ADVANTAGE - The preparation method is simple, inexpensive, easy, has reduced pesticide residue and has increased crop yield.
NOVELTY - Complex bacterial preparation is prepared by inoculating Clostridium lentocellum, xylan-degrading Bacteroides xylanisolvens, Cytophaga and Coprinus cinereus into culture medium, performing fermentation at 33-37 degrees C for 7 days, mixing fermented product, where the ratio of C.lentocellum, xylan-degrading Bacteroides, Cytophaga and C.cinereus in fermented mixture is 20-25:15-20:15-20:40-50.    USE - The complex bacterial preparation is useful for producing cellulase (claimed).    ADVANTAGE - The complex bacterial preparation is cost-effective, and simple to prepare.    DETAILED DESCRIPTION - Complex bacterial preparation is prepared by inoculating Clostridium lentocellum, xylan-degrading Bacteroides xylanisolvens, Cytophaga and Coprinus cinereus into culture medium, performing fermentation at 33-37 degrees C for 7 days, mixing fermented product, where the ratio of C.lentocellum, xylan-degrading Bacteroides, Cytophaga and C.cinereus in fermented mixture is 20-25:15-20:15-20:40-50, and the concentration of C.lentocellum, xylan-degrading Bacteroides, Cytophaga and C.cinereus is 0.8-1.2x 106 colony forming unit. An INDEPENDENT CLAIM is included for the method for producing cellulase, which involves crushing and mixing straw with culture medium, and sterilizing medium at 115-120 degrees C for 15-30 minutes, and cooling sterilized medium, inoculating microbial inoculum into cooled medium, performing culturing process at 30-35 degrees C for 7-10 days, and fermenting and vacuum-drying product.
NOVELTY - Preparation of 3-carbonyl-4-azaandrost-17( beta ) derivative (I) involves dissolving 3-((6S,10R)-6,10-dimethyl-11-oxotricyclo-tridecan-10-yl)propanoic acid compound (II) in dioxane in presence of an acid catalyst, adding aqueous ammonia, heating, slowly dripping reducing agent, aminating, carrying out ring-closing reaction, adding acid to the resultant product to destroy the reducing agent, concentrating under normal pressure, recovering dioxane, cooling the resultant product, isolating, obtaining crude product of 3-carbonyl-4-azaandrost-17 beta derivative, pulping and isolating.    USE - Preparation of 3-carbonyl-4-azaandrost-17( beta ) derivative (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly preparation of 3-carbonyl-4-azaandrost-17( beta ) derivative having high quality with high yield at low reaction temperature.    DETAILED DESCRIPTION - Preparation of 3-carbonyl-4-azaandrost-17 beta derivative of formula (I) involves dissolving3-((6S,10R)-6,10-dimethyl-11-oxotricyclo-tridecan-10-yl)propanoic acid compound of formula (II) in dioxane in presence of an acid catalyst, adding aqueous ammonia, heating, slowly dripping reducing agent, aminating, carrying out ring-closing reaction, adding acid to the resultant product to destroy the reducing agent, concentrating under normal pressure, recovering dioxane, cooling the resultant product, isolating, obtaining crude product of 3-carbonyl-4-azaandrost-17 beta derivative, pulping the resultant product, isolating and obtaining 3-carbonyl-4-azaandrost-17 beta derivative (I) and (2R,7S,15S)-2,15-dimethyl-6-azatetracyclo-heptadecan-5-one derivative of formula (III).    R=carbonyl, carboxylic acid, carboxylate, amido, acetyl, hydroxy, hydrocarbyl, ether or chloro.
NOVELTY - Modification method of vegetable biofuel involves atomizing bamboo to particle size of less than or equal to 6 mm, immersing atomized bamboo in water at normal pressure, dehydrating bamboo immersed in water, using dehydrated bamboo as fuel, and using solution obtained by dehydration as fertilizer.    USE - Modification method of vegetable biofuel for production of vegetable biofuel (claimed).    ADVANTAGE - The modification method can easily remove potassium and chlorine from bamboo.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) biofuel reforming system which comprises atomization apparatus which atomizes bamboo, elution apparatus which elutes water-soluble substance from atomized bamboo, water removal device which dehydrates bamboo discharged from elution apparatus, silo which stores dehydrated bamboo, and eluate tank which stores solution discharged from water removal device; and    (2) production of vegetable biofuel which involves atomizing bamboo to particle size of less than or equal to 6 mm, immersing atomized bamboo in water at normal pressure and eluting part for fertilizer, and dehydrating bamboo.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the biofuel reforming system. (Drawing includes non-English language text).
NOVELTY - Preparing fertilizer involves inoculating Freund's strain bacteria into culture medium and then culturing to obtain seed culture. The seed culture is cultured into fermentation culture medium for 24 hours to obtain fermentation culture. The fermentation culture is cultured in culture medium at 27-39 degrees C for 72-96 hours to obtain fermentation liquid. The liquid is centrifuged and then freeze-dried to obtain the powder. The powder is added into peat, absorbent materials and silicone preservative dry powder and then mixed to obtain the product.    USE - Method for preparing fertilizer (claimed).    ADVANTAGE - The method enables to prepare fertilizer in simple manner, and ensures easy control of production parameters.
NOVELTY - This utility new type claims a organic waste receiving a storage and transportation compost integrated processing system, this processing system comprises one or multi of a processing unit, the processing unit comprises a box body, a blower and gas purification system, a blowing system and gas purification system mounted b inner wall of the box body, the box body set with feeding wherein a seal cover, the bottom box body provided with a gas pipeline, a gas pipeline through pipeline and the air blast system and gas purification system. This utility new type collect organic waste is a garbage bucket, fermenting groove and compost of carriage of vehicle inner integrated in organic waste storage operation stack fertilizer integrated processing system, realize the storage of organic waste compost operation.
NOVELTY - This utility new type comprehensive use system is one of a agricultural plant waste. Namely, for a one to agricultural waste substance by smashing, add material molding dry distillation and pyrolysis for preparing high quality gas, straw biomass carbon, activated carbon, organic substance and chemical raw material and removing (carbon dioxide) and a system for preparing a high pressure steam. The system comprises raw material molding device, destructive distillation pyrolysis device, a condensing separating device, a gas device, activate carbon cleaning device, a steam input device. This utility new type fully use straw a regeneration resource, each for a waste of crop straw by carbonization pyrolysis for preparing fuel, organic substance and chemical raw material. This utility new type not only a fuel gas, straw biomass carbon, activated carbon, further obtaining a vinegar and tar, and separated in gas carbon dioxide, low quality variety straw carbon for preparing a high pressure steam, this utility new type a creates a considerable economic benefit. For comprehensive use rate of straw equal biomass waste raw material is high, and without any three wastes.
NOVELTY - The utility model is new type belongs to power generation technology field, especially relates to a using a combined solar energy environmental protection marsh gas power generation is multifunctional, comprises marsh gas pool, pipeline, a booster pump, a marsh gas tank, an air storage tank, a marsh gas generator, electric control device, controller, inverter and lead, solar energy solar panels, bracket, electrical appliance, storage battery, a room, common toilet, public toilet lower part provided with a marsh gas pool, the marsh gas pool by guiding pipe and a marsh gas tank connected, a booster pump and a tank connect the marsh gas, the marsh gas tank and a storage tank connected pneuma, air storage tank and a marsh gas generator a, a marsh gas generator and electric control device of a distribution, the distribution electric control device in a management room, a room provided with the storage battery, the storage battery respectively connected electric appliance and stop.
NOVELTY - Preparation of diuron comprises adding 3,4-dichlorophenyl isocyanate into organic solvent, dropping liquid dimethylamine under positive pressure, heating to recover excess dimethylamine, and cooling.    USE - Method for preparation of diuron (claimed).    ADVANTAGE - The method is environment-friendly, avoids decomposition of 3,4-dichlorophenyl isocyanate, improves yield and quality of product, reduces vaporization process and dimethylamine consumption, and it has low cost and no wastewater. The diuron is easy to store and transport, and it has high content of liquid dimethylamine.
NOVELTY - Glycerol processing device comprises reaction kettle (101), feeding port (102), methanol recovery device (2), glycerol treatment tank (3), methanol gas outlet (104), stirrer, vents, outlet, material circulation pump, inlet, discharge pipe, circulation discharging pump, glycerol finished product outlet, condenser, and vacuum generator.    USE - Glycerol processing device used for recovering biodiesel (claimed).    ADVANTAGE - The device is simple, has fast processing speed, and improves production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of glycerol processing device.    Methanol recovery device (2)    Glycerol treatment tank (3)    Reaction kettle (101)    Feeding port (102)    Methanol gas outlet (104)
NOVELTY - Production of calcium formate includes subjecting formaldehyde, acetaldehyde and calcium hydroxide as condensation catalyst and pentaerythritol by-product calcium formate reactant to condensation reaction, crosslinking, flocculating, precipitating, filtering, and discharging lime and heavy metals; and two-stage crystallizing, gradually increasing ratio of calcium formate and pentaerythritol, washing with water, discharging unsaturated pentaerythritol liquid phase, centrifuging, and drying.    USE - Method for production of calcium formate (claimed).    ADVANTAGE - The method solves existing pentaerythritol by-product calcium formate large organic impurities and inorganic ash content problem.    DETAILED DESCRIPTION - Production of calcium formate comprises subjecting formaldehyde, acetaldehyde and calcium hydroxide as condensation catalyst and pentaerythritol by-product calcium formate reactant to condensation reaction, crosslinking, flocculating, precipitating, filtering, and discharging lime and heavy metals to obtain reduced heavy metal and inorganic ash-containing by-product calcium formate; and two-stage crystallizing to obtain calcium formate crystal, gradually increasing ratio of calcium formate and pentaerythritol, washing with water when pentaerythritol and calcium solubility trends are different, discharging unsaturated pentaerythritol liquid phase to obtain reduced pentaerythritol and other organic impurities-containing calcium formate, centrifuging, and drying.
NOVELTY - A reforming reactor with hybrid plasma and catalyst comprises a reactor provided for plasma reforming, a plasma generator for generating plasma dissociation hydrocarbons, and a catalyst bed that is filled and equipped between the conductive rod and the conductive tape to simultaneously generate plasma dissociation and catalyst reforming. When a power is applied to the plasma generator, the catalyst bed will produce high energy electron impact that passes through the hydrocarbon gases of the catalyst bed to generate ionization, dissociation, excitation reactions, then the mixed gases composed of ion, electron and free radical are formed to perform a reforming reaction with the catalyst surface of the catalyst bed to produce hydrogen.
NOVELTY - Trazodone or its hydrochloride salt is prepared by reacting 1-(3-chloropheyl)-4-(3-chloropropyl)piperazine or its hydrochloride salt with triazolo pyridone compound optionally in the presence of inorganic base and catalyst to obtain trazodone as a free base and treating trazodone as free base with alcoholic solution of hydrogen chloride in which trazodone as free base and/or trazodone are isolated by precipitation at lower temperature.    USE - Preparation of trazodone or its hydrochloride salt.    ADVANTAGE - The environment-friendly method produces trazodone or its hydrochloride with improved yield and purity in a short time without involving use of costly reagents.    DETAILED DESCRIPTION - Trazodone of formula (I) or its hydrochloride salt is prepared by reacting 1-(3-chloropheyl)-4-(3-chloropropyl)piperazine of formula (II) or its hydrochloride salt with triazolo pyridone compound of formula (III) optionally in the presence of inorganic base and catalyst to obtain trazodone as a free base and treating trazodone as free base with alcoholic solution of hydrogen chloride in which trazodone as free base and/or trazodone are isolated by precipitation at lower temperature..
NOVELTY - A catalyst comprises Zeolite Socony Mobil-5 (ZSM); ultrastable Y (USY) zeolite; metallic component, e.g. copper, nickel, chromium, tungsten, molybdenum, metal carbide, metal nitride, and/or metal sulfide; basic material, e.g. alkaline-exchanged zeolite, alkaline earth-exchanged zeolite, basic zeolite, alkaline earth metal oxide, cerium oxide, zirconium oxide, titanium dioxide, mixed oxides of alkaline earth metal oxides, and/or mixed oxides of magnesia-alumina, magnesia-silica, titania-alumina, titania-silica, ceria-alumina, ceria-silica, zirconia-alumina, and/or zirconia-silica, and binder.    USE - A catalyst for biomass conversion (claimed).    ADVANTAGE - The metallic promoter in the catalyst imparts a bi-metallic functionality or stabilizes the metallic component, enhancing the performance of the metal component of the multi-functional catalyst.    DETAILED DESCRIPTION - A catalyst comprises Zeolite Socony Mobil-5 (ZSM); ultrastable Y (USY) zeolite; metallic component, e.g. copper, nickel, chromium, tungsten, molybdenum, metal carbide, metal nitride, and/or metal sulfide; basic material, e.g. alkaline-exchanged zeolite, alkaline earth-exchanged zeolite, basic zeolite, alkaline earth metal oxide, cerium oxide, zirconium oxide, titanium dioxide, mixed oxides of alkaline earth metal oxides, and/or mixed oxides of magnesia-alumina, magnesia-silica, titania-alumina, titania-silica, ceria-alumina, ceria-silica, zirconia-alumina, and/or zirconia-silica in which exchanged zeolite has 40-75% of exchanged cationic sites; and binder which is kaolin based, alumina based, and/or silica based. An INDEPENDENT CLAIM is included conversion of solid biomass to hydrocarbons which involves feeding the catalyst into a biomass conversion unit and pyrolyzing the biomass in the biomass conversion unit.
NOVELTY - Jet fuel, diesel, and/or gasoline components are produced from lipid-rich biomass (10) by pyrolyzing (20) lipid-rich biomass in the presence of water to produce biovapor (26) and biochar (25), catalytically converting (30) biovapor and biochar having greater than or equal to 15 wt.% paraffin content, and collecting biofuel (35) as liquid.    USE - Production of jet fuel, diesel, and/or gasoline components from lipid-rich biomass.    ADVANTAGE - The process avoids capital intensive investment in oil extraction technologies by incorporating oil extraction and oil conversion in one step and uses inexpensive catalyst to produce fuel in high yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the manufacture of jet fuel, diesel fuel, and/or gasoline fuel components.    Lipid-rich biomass (10)    Pyrolysis process (20)    Biochar (25)    Biovapor (26)    Catalytic conversion process (30)    Biofuel product (35)
NOVELTY - A photoelectrochemical cell or photocatalytic cell comprises a body of electrolyte, a capillary photoelectrode structure comprising an electrolyte-transporting strip comprising a porous network of cellulose nanofibers, and a working electrode comprising a porous photocatalytic material, where the electrolyte-transporting strip separates the body of electrolyte from porous photocatalytic material and is configured to transport electrolyte from electrolyte to the porous photocatalytic material via capillary force, and a counter electrode in electrical communication with the working electrode.    USE - Photoelectrochemical cell or photocatalytic cell for producing hydrogen (all claimed).    ADVANTAGE - The cell has excellent charge transport properties, long optical paths for efficient light absorption, and increased photoactivity.    DETAILED DESCRIPTION - A photoelectrochemical cell or photocatalytic cell comprises a body of electrolyte, a capillary photoelectrode structure comprising an electrolyte-transporting strip comprising a porous network of cellulose nanofibers, and a working electrode comprising a porous photocatalytic material, where the electrolyte-transporting strip separates the body of electrolyte from the porous photocatalytic material and is configured to transport electrolyte from the body of electrolyte to the porous photocatalytic material via capillary force, and a counter electrode in electrical communication with the working electrode. An INDEPENDENT CLAIM is also included for a method for producing hydrogen using the photoelectrochemical cell or photocatalytic cell.
NOVELTY - The utility model is new type supply one kind environment-friendly constant temperature vacuum double-layer cupping jar, which solves the problem is the existing vacuum heat tank, when in use with the tank body, using the external condition needed by heating, the utility model is new type of technology point is: the tube wall of the vacuum jar body is provided with inside cavity, inside inner cavity formed with conductor, heat conducting body mounted with heating device, heating device through lead and power supply socket connected with each other. Use vacuum extraction device for cup, by the negative pressure in tank body, tank body and heat and drug property of the emitting body to enter into the skin by the local heat stimulate temperature, can make good recover body function.
NOVELTY - The utility model is new type belongs to biomass rubbish heat energy conversion use technology field, specifically relates to one kind of biomass garbage sealing type quantitative feeding device. The utility model is new type the biomass rubbish sealing type quantitative feeding device using vertical hoisting machine for biomass rubbish from underground material stack transport to storage hopper, storage hopper is sealing and with the taper hopper connected with quantitative feeding mechanism as follows, quantitative feeding machine using equal volume transport method for biomass rubbish transport to blanking pipe or hydraulic propeller below in reciprocating movement of air cylinder, finally using thrust for sealing door is double-head spiral propeller or propeller type open for biomass rubbish transport to gasification furnace inside. The device not only solves have feeding biomass rubbish gasification transport system is not smooth and cannot control the problem that feeding precise, also solves have because of sealing and not caused by gasification furnace in the gas can overflow to storage in storage bin fire and explosion initiating equal safety problem.
NOVELTY - Producing biogas from biomass (2) in a biogas reactor, comprises (a) introducing biomass into biogas reactor containing a fermentation liquid (4), (b) adding magnetizable particles, and (c) performing biogas production. The biogas reactor has a means which for supplying and removing gases, liquids and solids. The magnetizable particles are magnetizable carbon particles comprising a carbon-containing phase and an inorganic magnetizable phase, where the carbon-containing phase comprises elemental carbon.    USE - The method and the device are useful for producing biogas from biomass in a biogas reactor (all claimed).    ADVANTAGE - The method is simple and cost-efficient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for performing the above method, comprising the biogas reactor (1), at least one magnetic separator (6), and at least one fluid line (7) leading from the biogas reactor through the at least one magnetic separator and back into the biogas reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device.    Biogas reactor (1)    Biomass (2)    Fermentation liquid (4)    Magnetic separator (6)    Fluid line (7)
NOVELTY - A desulfurizing apparatus comprises 1st desulfurizer (1-4) which removes tetrahydrothiophene in source gas and 2nd desulfurizer (5) which removes sulfurated carbonium in source gas and is arranged downstream from 1st desulfurizer. The 1st desulfurizer is arranged such that desulfurization units can be connected.    USE - A desulfurizing apparatus for fuel cell system which uses hydrogen generating apparatus and removes sulfur content in the gas of hydrocarbon components, such as town gas and liquefied petroleum gas.    ADVANTAGE - The desulfurizing apparatus is low cost and can respond to various source gas from which a sulfur component is reliably removable even if a source gas state changes in the middle of use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage method of desulfurizing apparatus which involves removing tetrahydrothiophene in source gas using 1st desulfurizer, flowing source gas from 1st desulfurizer to 2nd desulfurizer, and removing sulfurated carbonium in source gas using 2nd desulfurizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the desulfurizing apparatus. (Drawing includes non-English language text).    1st desulfurizer (1-4)    2nd desulfurizer (5)    Hydrogen generating apparatus (6)
NOVELTY - Performing esterification of fatty acid involves reacting alcohol and fatty acids in a reaction medium in presence of immobilized lipase to obtain esters of fatty acid. The lipase enzyme is immobilized on hydrophobic porous support.    USE - Method for performing esterification of fatty acid (claimed) used in biofuel, food, cosmetic, and pharmaceutical composition.
NOVELTY - A hydrogen-producing alloy has a passive film dissolving layer containing granular metal material chosen from aluminum, magnesium, silicon and zinc, and a finely divided eutectic alloy diffused layer extended in the crystal grain boundary of the granular metal material contained in the passive film dissolving layer. The granular metal material is made of gallium-indium-tin eutectic alloy, and is liquid at room temperature. The passive film dissolving layer and the eutectic alloy diffused layer suppress oxidation of the granular metal material in atmosphere.    USE - Alloy is used for producing hydrogen for fuel cell system (all claimed).    ADVANTAGE - Hydrogen is economically produced using reduced amount of alloy, with high yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of hydrogen-producing alloy;    (2) hydrogen-producing cartridge;    (3) hydrogen-production apparatus;    (4) hydrogen production method; and    (5) fuel cell system.
NOVELTY - The system has U type fermentation pipe (30) that is set with gas-guide tube (32). The discharging water pipe is set with control over water pressure in the biogas liquid in one-way flow into feedstock tube (10) and one-way valve. The biogas slurry is flowed into the one-way check valve in water pressure. The discharge tube (22) is detachably inserted into the two end sides of the U type pipe and fermentation feedstock pipe.    USE - Ultra-efficient marsh gas generating system.    ADVANTAGE - The uniform strain distribution of the marsh gas generating system is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the marsh gas generating system.    Feedstock tube (10)    Discharge tube (22)    U type fermentation pipe (30)    Gas-guide tube (32)    Cloth bacteria device (50)
NOVELTY - The soil fuel cell comprises an electrode (100) installed in an oxide layer (10) of soil, and another electrode (200) installed in a reduction layer (20) formed at the lower portion of the oxide layer of soil. The latter electrode is a carbon porous electrode dipped in anaerobes, in which the reduction layer returns the organic compound. The aerobic microorganisms oxidizing the organic compound exist in the oxide layer and supply electrons to the former electrode. The plant is planted to the oxide layer of soil.    USE - Soil fuel cell for producing electricity.    ADVANTAGE - Economical production of electricity is enabled using the soil microbes existing inside the soil. Non-utility generation of electricity is enabled in an efficient manner without an additional electric power supply.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a soil fuel cell.    Oxide layer (10)    Reduction layer (20)    Electrodes (100,200)    Direct current to direct current convertor unit (300)    Storage battery (400)
NOVELTY - A solid oxide fuel cell manufacturing method involves preparing a fuel electrode, forming first electrolyte layer comprising yttrium-doped barium zirconate solid oxide, forming a second electrolyte layer comprising yttrium doped barium cerate solid oxide on the first electrolyte layer. The fuel electrode, first electrolyte layer and second electrolyte layer are sintered to form half cell, followed by forming an air electrode on the second electrolyte layer to obtain a finished product.    USE - Method for manufacturing solid oxide fuel cell.    ADVANTAGE - The method enables manufacturing solid oxide fuel cell with improved hydrogen ion conductivity, high sinterability, excellent chemical stability, increased cerium/zirconium ratio, high proton conductivity, and improved performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a solid oxide fuel cell.
NOVELTY - A fossil fuel is obtained by processing animal and human feces.    USE - Fossil fuel is used as source for producing electricity, automobile fuel and nuclear energy.    ADVANTAGE - The fossil fuel is economical and environmentally-friendly.
NOVELTY - A fuel package consists of biomass fire-log bound by an adhesive containing starch and hydroxide, and ignition aid(s).    USE - Fuel package is used for cooking foodstuffs and heat generation.    ADVANTAGE - The fuel package is environmentally-friendly, economical, clean and safe, and has easy handleability, excellent transportability and laminating characteristics, and suppressed generation of defects.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of fuel package, which involves forming biomass fire-log having moisture content of 8-20% and adding starch and hydroxide separately to activate adhesive, and adding ignition aid(s) to biomass fire-log.
NOVELTY - Conversion of guest-gas species to augmented-guest compounds in an electrolytic cell including cathode, anode and electrolyte involves preparing clathrate hydrate (28) to include a guest-gas species, exposing the guest-gas species to cathode in presence of electrolyte (26) in electrolytic cell at 5-40 Coulombs to produce augmented-guest compounds, and collecting the resulting augmented-guest compounds.    USE - Conversion of guest-gas species e.g. carbon dioxide and methane to augmented-guest compound e.g. methane, ethane, propane and formic acid (all claimed) .    ADVANTAGE - The method enables conversion of guest-gas species to augmented-guest compound with high yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an electrochemical cell and flow cell.    Copper working electrode (22)    Chemical cell housing (23)    Platinum counter electrode (24)    Electrolyte (26)    Clathrate hydrate (28)
NOVELTY - Method for preparing a nanocellulose material, involves (a) providing a lignocellulosic biomass feedstock, (b) fractionating the feedstock in the presence of lignosulfonic acids or its derivative, at a pH 0-6, to generate cellulose-rich solids and a liquid containing hemicellulose and lignin, (c) mechanically treating the cellulose-rich solids to form cellulose fibrils and/or cellulose crystals, for generating a nanocellulose material having a crystallinity of at least 60%, and (d) recovering the nanocellulose material.    USE - The method is useful for preparing a nanocellulose material (claimed) which is used as a foam, an aerogel, a polymer composition, a carbon composition, a film, a coating, a coating precursor, a current or voltage carrier, a filter, a membrane, a catalyst, a catalyst substrate, a coating additive, a paint additive, an adhesive additive, a cement additive, a paper coating, a thickening agent, a rheological modifier or additive for a drilling fluid.    ADVANTAGE - The method prepares product at reduced energy cost with increased hydrophobicity.
NOVELTY - The fuel cell (100) comprises a cathode (104) opposing an anode (102). A first electrolyte membrane (106) and a second electrolyte membrane (108) are disposed between the anode and the cathode. An alternating current junction electrode (110) is disposed between the first electrolyte membrane and the second electrolyte membrane. A current collector is disposed between a first gas diffusion layer and a second gas diffusion layer of the alternating current junction electrode. Two catalyst layers are disposed between the electrolyte membranes and the gas diffusion layers.    USE - Fuel cell for generating hydrogen gas, electrical power, and mediation of electrochemical reactions and reactant transport.    ADVANTAGE - The fuel cell uses hydrogen to generate electricity from an alcohol fuel and provides increased power output.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for generating electric power.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell.    Fuel cell (100)    Anode (102)    Cathode (104)    Electrolyte membranes (106,108)    Alternating current junction electrode (110)
NOVELTY - Fermentation method of straw silage feed by adding Ganoderma lucidum involves (a) inoculating solid culture medium with G.lucidum and recovering the strain in a dish, inoculating liquid culture medium with activated strain to obtain homogeneous bacterium suspension, inoculating broth in fermentation tank with bacterium suspension, and fermenting mixture to obtain suspension containing suspended hypha, and inoculating straw with fermentation liquid containing suspended hypha, and fermenting mixture at room temperature for 15-60 days.    USE - The method is useful for fermenting straw silage feed by adding G.lucidum (claimed).    ADVANTAGE - The method is simple and cost-effective, has short period of fermentation, and prepares product which has suitable acidity, and is palatable and nutritious.    DETAILED DESCRIPTION - Fermentation method of straw silage feed by adding Ganoderma lucidum involves (a) inoculating solid culture medium with G.lucidum and recovering the strain in a dish which is the first activation, inoculating liquid culture medium with activated strain for second activation to obtain homogeneous bacterium suspension, inoculating broth in fermentation tank with bacterium suspension, maintaining ventilation and fermenting mixture to obtain suspension containing suspended hypha, and (b) inoculating straw with fermentation liquid containing suspended hypha and sealing the tank, and fermenting mixture at room temperature for 15-60 days.
NOVELTY - Treating industrial waste water to obtain organotin compound involves filtering sewage water containing tin ions through ion exchange resin to obtain filtrate. Ratio of water sample and ion exchange resin is 6-10:1. Sample flow rate is 1-2 bed volumes per hour. Eluate has tin ions. Ratio of eluate and effluent is 1:15-20. Eluate is eluted at flow rate of 0.5-1 bed volumes per hour. Eluate having tin ions, and industrial and agricultural by-products, and microbial agents are fermented in ratio of 1:1000-2000:10-20 for 25-30 days at room temperature.    USE - Method for treating industrial waste water to obtain organotin compounds used as feed additive (all claimed).    DETAILED DESCRIPTION - Treating industrial waste water to obtain organotin compound involves filtering sewage water containing tin ions through ion exchange resin to obtain filtrate. Ratio of water sample and ion exchange resin is 6-10:1. Sample flow rate is 1-2 bed volumes per hour. Eluate has tin ions. Ratio of eluate and effluent is 1:15-20. Eluate is eluted at flow rate of 0.5-1 bed volumes per hour. Eluate having tin ions, and industrial and agricultural by-products, and microbial agents are fermented in ratio of 1:1000-2000:10-20 for 25-30 days at room temperature. Fermentation material is stirred once in 12 hours. Obtained fermentation product is dried, and granulated to obtain organotin compounds.
NOVELTY - Purification of capsular polysaccharide involves dissolving polysaccharide crude product in water, adding ethanol and calcium chloride, mixing, centrifuging precipitate, standing for 6-12 hours, collecting supernatant liquid, performing ultrafiltration, adding 1-cetyl trimethyl ammonium bromide, centrifuging precipitate, standing for 6-12 hours, collecting precipitate, performing ultrafiltration, freeze-drying and purifying.    USE - Method for purifying capsular polysaccharide used for making Neisseria meningitidis capsular film, and Haemophilus influenzae capsular film and Salmonella typhi capsular film (claimed) or vaccine.    ADVANTAGE - The method is simple, environmental-friendly and efficient. It is suitable for suitable for diagnosis, prevention and treatment of diseases.
NOVELTY - Recovering biomass from construction waste comprises recovering biomass from construction waste in a pyrolysis furnace by pyrolysis and gasification, carrying out primary purification and secondary purification, carrying out first-stage separation and second-stage separation, and removing exhaust gas using a fan.    USE - The method is useful for recovering biomass from construction waste comprises subjecting construction waste to pyrolysis and gasification (claimed).    ADVANTAGE - The method realizes gasification energy conversion, and is safe and reliable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for recovering biomass from construction waste, comprising a pyrolysis furnace, a primary purifier, a secondary purifier, a primary separator, a secondary separator, a roots blower and a pipeline for connecting the components.
NOVELTY - The furnace has a furnace body formed with a furnace cover. An upper end of the furnace body is connected with a feeding port that is formed with a material cavity. A lower end of the furnace body is provided with a flame lighter that is connected with an air outlet. A lower part of a wall is connected with another air outlet. The wall is arranged with a vertical separation plate. A lower part of the slag discharging door is connected with the former air outlet. The latter air outlet is connected with a tar filter that is connected with an oil relux pipe.    USE - High rate tar splitting biomass gasification furnace.    ADVANTAGE - The furnace reduces discharge amount of the tar filter so as to reduce environment pollution rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a high rate tar splitting biomass gasification furnace.
NOVELTY - The method involves performing biomass pyrolysis gasification process. Tar pyrolysis gasification is performed by using a reaction furnace. High tar pyrolysis quantity and tar gasification quantity are measured. Biological oil and biological quantity are separated from the high tar pyrolysis quantity and the tar gasification quantity. Raw materials are added with solid product pyrolyzed biomass. Residual carbon is combusted. High temperature smoke is produced. The High temperature smoke is supplied to a heating pipe.    USE - Biomass gas supply heat cogeneration method.    ADVANTAGE - The method enables performing biomass gas supply heat cogeneration process in an effective manner and reducing device cost and management cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a biomass gas supply heat cogeneration method.
NOVELTY - Preparation of pellet fuel comprises drying biomass material with flue gas at 120-180 degrees C until water content of 10-20%, steaming sludge at 160-200 degrees C, and drying until water content of 10-20%; crushing biomass raw materials and dried sludge into less than or equal to 5mm; adding additive, mixing, adding into extrusion molding machine, and extruding; and adding into baking device, baking at 200-280 degrees C for 20-60 minutes with flue gas at 220-300 degrees C under hypoxic condition, and cooling.    USE - Method for preparing pellet fuel (claimed).    ADVANTAGE - The pellet fuel is easily to be mold, has strong water absorption ability, low transportation cost, and high strength. The method has low operating cost, mild molding condition, and high thermal efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pellet fuel preparation system comprising material handling system, forming system, baking system, boiler system, biomass raw material handling system, sludge treatment system, biomass drying device, biomass crushing device, biomass storage hopper, sludge drying device, sludge crushing device, sludge storage hopper, sludge additive storage hopper, mixing device, forming machine, first cooling device, forming fuel baking device, second cooling device, biomass boiler, air supply pipe, high temperature air pipe, high temperature dust remover, high temperature fan, high temperature steam pipe, and discharge system.
NOVELTY - The anaerobic power generation gas station has a main portion which is provided with a purifying tower and anaerobic tank heating system. The power generation units are provided in the main portion. The anaerobic tank is composed of plastic material. The plastic steel structure and structural beam column frame are connected together. The overflow pipe (17) is connected with the lower portion of anaerobic tank feeding pipe (1). A warming layer is provided between the two walls of anaerobic tank. An insulating layer (3) is provided in the outside of anaerobic tank.    USE - Plastic steel reinforced concrete structure anaerobic power generation gas station.    ADVANTAGE - The heat preservation effect, warming function and alarming function of the gas station are improved. The biogas production efficiency is improved. The biogas production efficiency is increased. The investment cost of the gas station is reduced. The environment purification effect is improved. Clean energy stored is obtained. The size of anaerobic device is large. The tank is changed easily. The raw materials can be saved. The efficiency of gas station is improved. The environmental protection effect is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the anaerobic power generation gas station.    Anaerobic tank feeding pipe (1)    Insulating layer (3)    Marsh gas outlet (8)    Overflow pipe (17)    Stirrer (18)
NOVELTY - The structure has feedstock tube (10), drain pipe (20), U-type fermentation pipeline (30) and water pressure chamber. Water pressure chamber is placed at top portion of fermentation pipeline. Water pressure chamber and feedstock tube are connected with feedstock tube and drain pipe. Drain pipe is connected between chamber and feedstock tube. Gas-guide tube (32) is provided on U-type fermentation pipe. Discharging water pipe is connected with one-way valve. Horizontal lowest point of discharging water pipe is higher than horizontal lowest point of feedstock pipe and drain pipe.    USE - Hydraulic U-shaped efficient marsh gas pool structure for biogas liquid circulative convection.    ADVANTAGE - The fermentation path of the structure is increased. The operation difficulty of the fermentation device is reduced without manual intervention. The production difficulty is reduced. The uniform strain distribution is promoted efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydraulic U-shaped efficient marsh gas pool structure.    Feedstock tube (10)    Drain pipe (20)    U-type fermentation pipeline (30)    Gas-guide tube (32)    Bacteria device (50)
NOVELTY - Activity of methanogenic bacterial agent comprises cobalt nitrate, nickel chloride, ammonium molybdate, potassium acetate, and magnesium sulfate in a mass ratio of 5:5:20:30:40. The activity of methanogenic bacterial agent is applied directly to a digester.    USE - Activity of methanogenic bacterial agent is useful for production of methane gas.    ADVANTAGE - The methanogenic bacterial agent produces methane gas with high purity and quality using agricultural waste, and excellent biological activity.
NOVELTY - The utility model is new type relates to biochemical experiment device, and more particularly, to a adjustable EP tube and a temperature mixer, the adjustable temperature of EP tube mixer containing device and a temperature regulating device, the holding device is detachably fixed on the temperature regulating device, receiving device comprises a plate frame, a bottom plate, a handle in a protective cover, a main plate provided with a clamping slot, the bottom plate provided with a through hole, a bottom plate and a clamping slot is embedded in a plate frame on a main plate frame, handle fixed on a frame bottom plate, protection cover moving link on a plate at a, temperature regulating device setting in a plate frame, the utility model is new type structure is simple, design is reasonable, because of a carry out mixing uniformly by hand, it will not produce noise and pollute, fit a super-clean workbench at a use, and can realize batch mixing uniformly, with a high efficiency and practicability, and a low cost, energy saving and environment-friendly, for mixing the EP tube in the agent device comprises heat preservation effect, widely fit and use.
NOVELTY - A recombinant C1 metabolizing microorganism comprising a first exogenous nucleic acid chosen from exogenous nucleic acid that encodes an L-amino acid biosynthesis enzyme and an exogenous nucleic acid comprising an expression control sequence that is operably linked to a nucleic acid that encodes a native L-amino acid biosynthesis enzyme, is new. The recombinant C1 metabolizing microorganism is capable of converting a natural gas-derived carbon feedstock into a desired L-amino acid. The delta 13C of the recombinant C1 metabolizing microorganism is less than -30%.    USE - The recombinant C1 metabolizing microorganism is useful for converting a natural gas-derived carbon feedstock into a desired L-amino acid, where the natural gas-derived feedstock is natural gas or methane and producing biomass (all claimed) which is used as a animal feed ingredients.    ADVANTAGE - The recombinant C1 metabolizing microorganism cost-effectively enhances production of a desired amino acids and biomass. The animal feed ingredient has improved nutrient-content, energy-content, and/or disease fighting properties.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass, which is derived from a culture of the recombinant C1 metabolizing microorganism.
NOVELTY - Conversion of biomass-derived pyrolysis oil involves preparing a catalyst containing element(s) chosen from group VIII metals, and contacting a feed containing biomass-derived pyrolysis oil with hydrogen at 50-350 degrees C in presence of catalyst. The catalyst is prepared by comulling (a) a refractory oxide (a1), small amount of liquid (a2) chosen such that loss on ignition (LOI) at 485 degrees C of the mixture is 20-70 wt.%, and metal component(s) (a3) which is/are partially insoluble in the used liquid to form a mixture, shaping, drying and calcining the obtained mixture.    USE - Conversion of biomass-derived pyrolysis oil is used for producing bio-fuels and bio-chemicals.    ADVANTAGE - The method enables safe ad economical conversion of biomass-derived pyrolysis oil.    DETAILED DESCRIPTION - Conversion of biomass-derived pyrolysis oil involves preparing a catalyst containing 12 wt.% or more, preferably 65 wt.% or less element(s) chosen from group VIII metals with respect to total weight of the catalyst, and contacting a feed containing biomass-derived pyrolysis oil with hydrogen at 50-350 degrees C in presence of catalyst. The catalyst is prepared by comulling (a) a refractory oxide (a1), small amount of liquid (a2) chosen such that loss on ignition (LOI) at 485 degrees C of the mixture is 20-70 wt.% with respect to total weight of the catalyst composition, and metal component(s) (a3) which is/are partially insoluble in the used liquid to form a mixture, optionally shaping and drying the obtained mixture, and calcining the obtained composition to provide a calcined catalyst. The metal component (s) (a3) is/are chosen from Group VIII metal components, preferably nickel or its component. An INDEPENDENT CLAIM is included for preparation of catalyst.
NOVELTY - Sewage treatment system comprises aerator (9), reverse flushing system (12), aeration tank (1), aeration plate (10), inner elastic filler (2), inner ball filler, cellular filler, biofilm filler, clay pipe, water inlet pipe, water outlet pipe, first return pump, first return pipe, second return pump, and second return pipe.    USE - Sewage treatment system used for processing organic matter and precipitating biological bacteria.    ADVANTAGE - The system reduces sewage sludge, phosphorus and other pollutant values.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of sewage treatment system.    Aeration tank (1)    Inner elastic filler (2)    Aerator (9)    Aeration plate (10)    Reverse flushing system (12)
NOVELTY - Method for processing organic wastewater, involves contacting organic wastewater containing substance which reacts with the carbon dioxide and produces a precipitate, with gas containing carbon dioxide, precipitating at high concentration, performing solid-liquid separation to separate the precipitated solid substance, performing high-speed methane fermentation treatment on the separated solid substance and producing biogas.    USE - The method or apparatus is useful for processing organic wastewater and producing biogas (all claimed).    ADVANTAGE - The method processes organic wastewater cost-effectively and stably for long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing apparatus of the organic wastewater.
NOVELTY - An oral administration liquid comprises 115-125 pts. wt. Astragalus, 115-125 pts. wt. Codonopsis pilosula, 115-125 pts. wt. kudzu root, 75-85 pts. wt. Rhodiola rosea, 45-55 pts. wt. pseudoginseng, and 45-55 pts. wt. sea-buckthorn.    USE - Oral administration liquid used for treating gastric mucosa and liver damage (claimed).    ADVANTAGE - The oral administration liquid has increased isorhamnetin and ginsenoside Re transfer rate to more than 90%, improved efficiency, and reduced cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of oral administration liquid comprising washing raw materials, drying, adding 8 times total weight purified water, boiling twice every 1.5 hours, filtering, combining filtrates, and concentrating to 60 degrees C at - 0.08 MPa until relative density of clear cream is 1.10-1.15; and recovering alcohol until no more alcoholic taste, adding 0.4 pts. wt. stevioside and 0.5 pts. wt. potassium sorbate, stirring to dissolve, adding 1000 pts. wt. purified water, stirring, filtering, sterilizing, and filling 15 mL oral liquid into bottles.
NOVELTY - Utilization of iron ions in iron-containing industrial wastewater filtering iron-containing industrial wastewater, taking filtrate and ion exchange resin at volume ratio of 6-10:1, adsorbing and eluting at 1-2 bed volume/hour, adding eluent and water at weight ratio of 1:15-20, eluting at 0.5-1 bed volume/hour to obtain iron ions concentrated solution, adding industrial/agricultural by-products and microbial agents at weight ratio of 1000-2000:10-20, fermenting for 25-30 days while stirring once every 12 hours, drying and granulating.    USE - Method for utilizing iron ions in iron-containing industrial wastewater used for preparing organoiron feed additive (claimed).    ADVANTAGE - The method has good ecological, economic and social benefits.
NOVELTY - Crop straw returning method comprises selecting fermentation pool, digging pond around the pool, pulverizing crop straw, piling pool with 1-100 cm thick crop straw, laying a layer of rice straw on top of farm manure, repeating straw stacking procedure, covering with soil and farm manure to thickness of 5-10 cm, allowing decay of materials for more than a month, using rotten straw as basal fertilizer and plowing.    USE - Method of preparing crop straw (claimed).    ADVANTAGE - The method is environment-friendly and saves fertilizer cost.
NOVELTY - A biodiesel oil is prepared by taking lipid, solid acid catalyst, and 1-6C alcohol, mixing, carrying out transesterification reaction at 60-125 degrees C under 0.8-1.1 MPa, separating ester and glycerol phase, taking ester phase, adding solid alkali catalyst, heating at 60-120 degrees C under 0.8-2.0 MPa, carrying out flash evaporation reaction under 0.05-0.5 MPa, separating alcohol, taking ester and glycerol phase, vacuum distilling at 120-300 degrees C, concentrating, and decompressing.    USE - Method for preparing biodiesel oil (claimed).    DETAILED DESCRIPTION - A biodiesel oil is prepared by taking lipid, solid acid catalyst comprising zirconium sulfate, sulfated zirconia or H-ZSM-5 type molecule sieve, and 1-6C alcohol, mixing, carrying out transesterification reaction at 60-125 degrees C under 0.8-1.1 MPa, separating ester and glycerol phase, taking ester phase, adding solid alkali catalyst comprising zinc oxide, magnesium-aluminum composite oxide catalyst or ETS-10 type molecule sieve, heating at 60-120 degrees C under 0.8-2.0 MPa, carrying out flash evaporation reaction under 0.05-0.5 MPa, separating alcohol, taking ester and glycerol phase, vacuum distilling at 120-300 degrees C, concentrating, and decompressing.
NOVELTY - A microwave assisted transesterified wet algae biodiesel is prepared by taking microalgae liquid, filtering or centrifuging, taking wet algal biomass, adding low carbon alcohol and concentrated sulfuric acid, homogenizing, microwave treatment, reacting, cooling, adding n-hexane, extracting, adding deionized water, homogenizing, centrifuging, taking upper layer, adding deionized water, centrifuging, taking upper layer, adding n-hexane, and heating.    USE - Method for preparing microwave assisted transesterified wet algae biodiesel (claimed).    ADVANTAGE - The biodiesel is 14-22C and has biological crude oil content of 80-98%.    DETAILED DESCRIPTION - A microwave assisted transesterified wet algae biodiesel is prepared by taking microalgae liquid, filtering or centrifuging to obtain 40-90 wt.% wet algal biomass, taking 1-10 g wet algal biomass, adding 8-800 ml low carbon alcohol and 0.24-24 mL 98 wt.% concentrated sulfuric acid, homogenizing for 20-40 seconds, carrying out microwave treatment at 500-4000 power for 40-80 seconds at 60-100 degrees C, lowering microwave power to 400-1000, reacting for 2-60 minutes, cooling to 25-30 degrees C for 20-40 minutes, adding 8-800 ml n-hexane, extracting, adding 15-300 ml deionized water, homogenizing for 1 minute, centrifuging at rate of 4000 revolutions/minute (rpm) for 5 minutes, taking upper layer, adding 10-200 ml deionized water, centrifuging at rate of 4000 rpm for 5 minutes, taking upper layer, adding n-hexane, and heating at 50-80 degrees C.
NOVELTY - A biodiesel oil additive is prepared by taking orange peel, stem, branch, root and leaf, drying, crushing into 60-120 mesh, adding biodiesel oil, extracting 1-3 times for 8-24 hours at 15-50 degrees C, filtering, carrying out gradient dilution using NB/SH/T0825-2010 method, adding biodiesel oil, and mixing.    USE - Method for preparing biodiesel oil additive (claimed).    ADVANTAGE - The additive is low-cost and nontoxic.
NOVELTY - An alcohol oil biomass ethanol-based fuel formulation comprises 45-60 wt.% 90# gasoline, 20-25 wt.% methanol, 2-6 wt.% thinner, 5-10 wt.% combustion improver, 0.2-0.7 wt.% additive, 0.05-0.2 wt.% fast ignition agent and 2-4 wt.% bio-oil.    USE - Alcohol oil biomass ethanol-based fuel formulation.    ADVANTAGE - The fuel is low-cost, energy efficient, environment-friendly and has excellent performance.
NOVELTY - Preparation of cattle manure efficient organic fertilizer comprises taking cow dung, reacting in the presence of catalyst at 150-180 degrees C and 0.8-1.2 MPa for 20 minutes; carrying out solid-liquid separation; and preparing separated solid into biomass granules.    USE - Method for preparing cattle manure efficient organic fertilizer (claimed) used as alternative for fuel wood.    ADVANTAGE - The method solves the problem of farm manure pollution, reduces greenhouse effect, has zero emissions, utilizes agricultural waste, and promotes energy saving strategic measures.
NOVELTY - Production of biodiesel comprises adding waste vegetable oil into a container, adding alcohol and bromine-iodine, reflux reacting, cooling, separating the upper layer solution, decompression distilling the upper layer solution to remove alcohol and water, obtaining oil product, adding 1.5-2.0 times ethyl alcohol and 0.5-1 wt.% bromine-iodine, adding into a reaction kettle, reflux reacting at 80-100 degrees C for 0.5-3 hours, cooling, separating the upper layer oil phase, 50-60 degrees C hot water washing until neutral and drying to obtain the biodiesel product.    USE - Production of biodiesel (claimed).    ADVANTAGE - The method is simple and suitable for industrial implementation, has low device investment and little environmental pollution, avoids the use of strong acid and strong alkali, uses alcohol, which can be recycled, and achieves high product purity and high conversion rate i.e. more than 96.5%.    DETAILED DESCRIPTION - Production of biodiesel comprises adding waste vegetable oil into a container, adding 1.5-2.0 times alcohol and 0.9-1.5% bromine-iodine, reflux reacting at 85-95 degrees C for 0.5-3 hours, cooling, separating the upper layer solution, where volume ratio of bromine and iodine in bromine-iodine is 1:0.8-0.9, decompression distilling the upper layer solution to remove alcohol and water, obtaining oil product, adding 1.5-2.0 times ethyl alcohol and 0.5-1 wt.% bromine-iodine, adding into a reaction kettle, reflux reacting at 80-100 degrees C for 0.5-3 hours, cooling, separating the upper layer oil phase, 50-60 degrees C hot water washing until neutral and drying to obtain the biodiesel product.
NOVELTY - Preparing fresh low degree yellow millet wine involves brewing and fermenting raw materials by enzymes at low temperature. Traditional Chinese medicine wine is treated with amylase for 12-24 hours, and then yeast rice is added to treated product. Saccharifying enzyme is added to obtained mixture. Mixture is fermented at 16-26 degrees C to obtain wine with purine and fusel oil content of 10mg/L and 120mg/L respectively.    USE - Method for preparing fresh low degree yellow millet wine (claimed).    ADVANTAGE - The method is environment-friendly and suitable for large-scale production. The prepared wine is tasty and rich in microelements.
NOVELTY - The method involves providing two sides of the double sided pipe (30) with a feedstock pipe (10) and a discharge pipe (20). The discharge pipe is provided with a drain pipe (44). The pipeline and feedstock pipe are connected detachably. The end of the discharge pipe is connected with a discharging tube plate (34). The hydraulic pressure unit (40) is provided with movement.    USE - Multi-regional flow distribution method for producing methane bacteria.    ADVANTAGE - The efficiency of the multi-regional flow distribution for producing methane bacteria is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the methane producing device.    Feedstock pipe (10)    Discharge pipe (20)    Double sided pipe (30)    Discharging tube plate (34)    Hydraulic pressure unit (40)    Drain pipe (44)
NOVELTY - Method for efficiently mixing methane producing bacteria to produce methane, involves providing feedstock and biogas slurry into fermentation system, where pressure is increased in fermentation zone, the system comprises discharging tube, cloth device, reflux tube and pipeline, and the methane is produced based on circulation flow of slurry.    USE - The method is used for efficiently mixing methane producing bacteria to produce methane (claimed).
NOVELTY - A Rhodococcus sp. strain NSX2 (CGMCC No: 9611), is new.    USE - The strain is useful for decontaminating heavy metal polluted soil, in phytoremediation of Sedum plumbizincicola, and in plant growth promoting preparation. The heavy metal is at least one chosen from cadmium, copper and zinc (all claimed).    ADVANTAGE - The strain increases polluted soil repairing efficiency, and is environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) use of Rhodococcus sp. strain NSX2 for decontaminating heavy metal polluted soil; and (2) plant growth promoting preparation comprisingRhodococcus sp. strain NSX2.
NOVELTY - The method involves increasing the methane gas fermentation zone pressure, by pushing the flow of fermentation methane gas feeding pipe (10). One-way valve is provided in a discharging pipe (20). Any area of methane fermentation is used as methane gas pressure drop fermentation area. The methane gas slurry is circulated in the slurry storage section through the feeding pipe and the fermentation bacteria reflux pipe.    USE - Method of generating methane gas using methane gas generation system, for use in agricultural field.    ADVANTAGE - The methane gas slurry circulation flow stirring performance is improved, and the uniform distribution of strain is promoted using the stirring methane gas slurry circulation flow. The crusting phenomenon is prevented effectively, and the gas production is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane gas generation system.    Feeding pipe (10)    Discharging pipe (20)    Straight pipe (30)    Feeding pipe blocking plate (32)    Discharging pipe blocking plate (34)
NOVELTY - The method involves providing fermentation material into space within fermentation region to produce marsh gas. The fermentation region is formed between adjacent air resistance plates (36,38). The flow of fermentation marsh gas in feeding tube (10) and discharge tube (20) is promoted, when pressure of marsh gas fermentation region is increased. The drained marsh gas is flowed into cloth between strain separating units, when marsh gas strain level reaches lowest point of drain device.    USE - Method for generating marsh gas using multi-area biogas turbulent flow type marsh gas fermentation system.    ADVANTAGE - The marsh gas is generated effectively with uniform material distribution efficiency, high reliability and increased production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multi-area biogas turbulent flow type marsh gas fermentation system.    Feeding tube (10)    Discharge tube (20)    Fermenting pipeline (30)    Air resistance plates (36,38)    Water pressure control unit (40)
NOVELTY - Method for enzymatically processing straw, involves (a) taking wheat straw, and drying and crushing the wheat straw to obtain straw powder, (b) adding diluted hydrochloric acid to straw powder, performing acidification reaction, reducing product to room temperature, and collecting slurry, and (c) processing the slurry using mixture comprising cellulase, xylanase, magnesium chloride, and Tween-80 (RTM: Polysorbate 80) and distilled water.    USE - The method is useful for enzymatically processing straw (claimed).
NOVELTY - Liquefied carbon dioxide gas expansion involves containing or not containing an impurity of carbon dioxide gas through turbocharger pressurized at 7.50-.8.50 megapascals. The impurities contained carbon dioxide gas is cooled by a heat exchanger at 10 to -20 degrees C. The carbon dioxide gas containing gaseous impurities is expanded to a pressure of 2.3-2.7 MPa at -14 to -10 degrees C, where the majority carbon dioxide gas is liquefied, and turned into a gas-liquid mixture containing liquid carbon dioxide or gaseous carbon dioxide-containing gas not liquefied impurities.    USE - Method for expanding liquefied carbon dioxide gas (claimed).    ADVANTAGE - The method expands liquefied carbon dioxide gas in a simple, safe and eco-friendly manner without using toxic liquid ammonia.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the liquefied carbon dioxide gas expanding method. (Drawing includes non-English language text).    Pre-cooler (10)    Water separator (20)    Water (30)    Dealkylation heater (52)    Dealkylation reactor (53)
NOVELTY - The method involves processing a silicon chip. The silicon chip is provided with a snake-shaped convex micro flow channel and a square lug boss array unit. An electrode is connected with a cathode flow field plate and an anode flow field plate. Mold assembly process is performed. PDMS glue solution injection process is performed. The cathode flow field plate is coated with PDMS material. Metal plate cutting process is performed according to anti-corrosive treatment process. Micro direct formic acid fuel cell packaging process is performed.    USE - MEMS based micro direct formic acid fuel cell manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of a micro direct formic acid fuel cell.
NOVELTY - Non-load type synthesis methanation catalyst comprises metal particle of 70-95 wt.% nickel (Ni) and 5-30 wt.% molybdenum (Mo) oxide auxiliary agent.    USE - Non-load type synthesis methanation catalyst.    ADVANTAGE - The catalyst has long service life, and high conversion rate under low temperature.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of non-load type synthesis methanation catalyst comprising mixing soluble Ni salt and solvent at 60-80 degrees C to obtain 0.1-0.35 mol/l Ni ion solution, adding 2-20 wt.% polyethylene pyridine ketone, at mol ratio of hydrazine and Ni of 10-30:1, adding dropwise sodium hydroxide until pH 10-12, reacting for 2-4 hours at 50-80 degrees C and stirring; centrifuging, removing upper layer clear liquid from black solid precipitate, washing precipitate using alcohol and distilled water, and drying under nitrogen and argon inert atmosphere; controlling Mo and Ni mol ratio of 2-15:100, saturating soluble molybdenum salt solution, and dipping for 10-24 hours; under argon atmosphere, dipping at 270-350 degrees C, baking for 2-4 hours, reducing temperature at to 400-550 degrees C, and reducing normal compression hydrogen space velocity under 200-1000 ml/g for 1-1.5 hours; and reacting at 700-800 degrees C for 1-3 hours under hourly compression hydrogen hourly space velocity of 300-1200 ml/g, and reducing temperature in argon atmosphere; and    (2) application of non-load type synthesis methanation catalyst comprising adding hydrogen, solvent and surface active agent into reactor, adding catalyst, and reacting under hydrogen atmosphere and 1-4 MPa, stirring at 1400-2200 revolutions/minute at 270-320 degrees C.
NOVELTY - Cultivating high mountain lucid Ganoderma in flat land using waste strain culture material comprises strain preparation, inoculation, fruiting bar preparation, fruiting management, harvesting and processing. The method comprises growing high mountain lucid Ganoderma parent species at an altitude of more than 1500 m above, obtaining mother species and final species, cultivating the species, preparing fruiting bars from waste used in cultivation of shiitake mushrooms and black fungus, opening shade net of greenhouse, increasing illumination, and prompting pileus growth.    USE - The method is useful for cultivating high mountain lucid Ganoderma in flat land using waste strain culture material (claimed).    ADVANTAGE - The method: utilizes the waste used in cultivation of shiitake and black fungus as lucid Ganoderma medium replacing basswood, which is important to ecological balance protection; supplies underground water to the lucid Ganoderma mushroom for growth requirements during mushroom management; can widen temperature difference to provide the unique environment for lucid Ganoderma during growth; and retains original characteristics and contents of the mushroom product.    DETAILED DESCRIPTION - Cultivating high mountain lucid Ganoderma in flat land using waste strain culture material comprises strain preparation, inoculation, fruiting bar preparation, fruiting management, harvesting and processing. The method specifically comprises growing high mountain lucid Ganoderma parent species at an altitude of more than 1500 m above to prepare stock culture, obtaining mother species and final species by tissue isolation, cultivating the species, preparing fruiting bars from waste used in cultivation of shiitake mushrooms and black fungus, when the fruiting body grows up to 8-10 cm, then opening shade net of greenhouse, increasing illumination, and prompting pileus growth.
NOVELTY - Cultivating straw mushroom using Flammulina velutipes residue as raw material, comprises adding straw mushroom spawn into cultivation material and cultivating, where the cultivation material includes pure Flammulina velutipes mushroom residue.    USE - The method is useful for cultivating straw mushroom using Flammulina velutipes residue as raw material (claimed).    ADVANTAGE - The method is economical, increases the mushroom yield and reduces the environmental pollution caused by mushroom residue.
NOVELTY - A pepper family plant active extract based herbicide is prepared by taking pepper fruit, stems, roots and leaves, grinding into mortar, reflux extracting, solvent evaporating, and adding emulsifier and additive.    USE - Method for preparing pepper family plant active extract based herbicide (claimed) used for killing annual, biennial and perennial weeds.    ADVANTAGE - The herbicide has simple structure, no poison and low cost, is nonresidual and environment-friendly, and uses wide raw material source.
NOVELTY - The prevention system has a sprayed module (200) which is provided for jetting the inert gas supplied from a control valve. An inert gas supply module produces and supplies the inert gas through the generating station, condenser, blower, buffer tank, manifolder and control valve within the coal seam. The sprayed module sprays inert gas to the coal seam through the multi-stage inside jet pipe (211,212) and multi-stage outside jet pipe (215,216) which is arranged around inside jet pipe. The multi-stage inside jet pipe is communicated with the control valve.    USE - Prevention system for spontaneous ignition of coal bed in heat power plant.    ADVANTAGE - The inert gas supply module produces and supplies inert gas through the generating station, condenser, blower, buffer tank, manifolder and control valve within coal seam, such that the spontaneous ignition through the sprayed module is prevented effectively. The construction cost is reduced. The convenience operation is realized. The spontaneous ignition is suppressed by supplying the inert gas to the coal seam.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the spontaneous ignition prevention system.    Sprayed module (200)    Jet pipe (210)    Multi-stage inside jet pipes (211,212)    Multi-stage outside jet pipes (215,216)    Rotating unit (230)
NOVELTY - Recovery of oil from involves dry milling corn at ethanol manufacturing unit by converting starch in corn to sugar, fermenting sugar to produce ethanol and whole stillage, separating whole stillage to produce distillers wet grains and thin stillage containing corn oil, evaporating thin stillage to remove water and form concentrated byproduct containing corn oil, centrifuging concentrated byproduct in a centrifuge located downstream from the evaporator to separate at least a portion of corn oil from concentrated byproduct, and recovering separated oil.    USE - Recovery of oil from thin stillage in dry milling corn-to-ethanol plant (claimed).    ADVANTAGE - The method enables efficient and economical recovery of oil from thin stillage in dry milling corn-to-ethanol plant, by simple method.
NOVELTY - The invention relates to a process for preparing a liquid fertilizer with crop plants symbiosis stimulating effects. According to the invention, the process consists in macerating chopped stinging nettles in rain water followed by fermentation for 4...5 days, at a temperature of 18...20 degrees C, homogenizing the fermented nettle macerate at a pressure of 150 MPa, after which the homogenized composition is diluted 5 times, is subjected to filtration and microbiological ultrafiltration by passing it on a filtering membrane of polyethersulphone with pores of 0.5, at a rate of 500 l/h and a pressure difference of 0.2 bar, to result in a highly stable filtrate.
NOVELTY - The bench has a fermentation substrate reservoir (1) connected with a fermentation tank (2). Another fermentation tank (3) is connected with a fermentation substrate and includes an insulating protective layer heating mantle (5). The fermentation substrate is provided in a pre-form fermentation vessel and a final fermentation vessel. Biogas is transported from the fermentation tank for discharging conduits (23) to a bus (23') that is connected to a biogas tank (24).    USE - Bench for biogas production from substrate as mixture of manure and organic waste and vegetable matter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a bench.    Fermentation substrate reservoir (1)    Fermentation tanks (2, 3)    Insulating protective layer heating mantle (5)    Discharging conduits (23)    Bus (23')    Biogas tank (24)
NOVELTY - Acid-catalyzed dehydration of ethanol involves distilling ethanol feedstock (101) containing nitrogen-containing contaminant(s) to form an overhead stream (102) and bottom stream (103) containing ethanol, and reacting bottom stream in presence of an acid catalyst such that a product stream containing ethylene and/or diethyl ether is formed. The reflux ratio of ethanol feedstock in distillation process is at least 20:1.    USE - Acid-catalyzed dehydration of ethanol in production of ethylene and diethyl ether (claimed). Uses include but are not limited to dehydrate oxygen, carbon dioxide, carbon monoxide and/or nitrogen depleted ethanol feedstock. The ethanol is used as fuel additive and antifreeze agent, and used in germicide, food and beverage industry, and chemical feedstock.    ADVANTAGE - The acid-catalyzed dehydration process has excellent energy efficiency by heat exchanging using spare heat source as reboiler. The process enables use of favorable properties and conditions, and is a continuous process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage of process, which involves dehydrating nitrogen-containing contaminant-depleted, preferably acetonitrile-depleted, ethanol feedstock in presence of acid catalyst to produce ethylene and/or diethyl ether.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view illustrating of acid-catalyzed dehydration process of ethanol.    Distillation of ethanol feedstock (101)    Overhead stream (102)    Bottom stream (103)    Condensed stream (104)    Gaseous stream (105)
NOVELTY - Production of road asphalt involves feeding (100) biomass into two pass drying chamber, drying (101) biomass to produce dry biomass, heating (102) dry biomass to produce vapor phase bio oil, carrying (104) vapor phase bio oil to a condenser, condensing (110) vapor to liquid phase raw bio oil, separating (112) water from raw bio oil in a separator to produce refined bio oil, and processing refined bio oil to obtain road asphalt.    USE - Production of road asphalt (claimed).    ADVANTAGE - The method enables production of road asphalt with improved elasticity and weather resistance. The addition of water during the quenching process provides better contact of water and oil, and a cooling medium. The addition of ethanol suppresses the separation of water, and maintains the bio oil in a homogeneous phase with no increase in viscosity for at least 6 months. Ethanol added acts as an ignition improver, helps improve clogging in lines and keeps the storage and contact surfaces clean. The combination of quench, water extraction and ethanol addition provides fuel that has higher pH, more stability, extremely low viscosity and usability as a heating fuel without needing any external heating.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the production of road asphalt.    Feeding process (100)    Drying process (101)    Heating process (102)    Carrying process (104)    Quenching process (106)    Cooling process (108)    Condensing process (110)    Separating process (112)    Mixing processes (114a,114b)
NOVELTY - Method for inhibiting precipitation of biodiesel fuel component involves providing a biodiesel fuel composition, providing a copolymer comprising polymeric unit (a) derived from a carboxylic acid anhydride and polymeric unit (b) derived from olefin, and forming treated fuel composition by blending the copolymer with biodiesel fuel.    USE - Method for inhibiting precipitation of biodiesel fuel component used for motor vehicle.    ADVANTAGE - The method efficiently and economically inhibits precipitation of biodiesel fuel component with high cold soak filter blocking tendency value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for reducing cold soak filter blocking tendency of biodiesel fuel composition.
NOVELTY - Fermentation of organic fertilizer comprises collecting straw, drying, crushing to obtain straw powder, collecting livestock and poultry excrement, drying to obtain dry excrement, collecting traditional Chinese medicine, crushing to obtain traditional Chinese medicine dregs, mixing and stirring materials, mixing with bacterial strain and water to humidity of 60%, detecting carbon/nitrogen ratio, piling to height of 1.2-1.5 m, fermenting at 65 degrees C for 2 days, turning for 3 times and completing fermentation until material color is brown, material volume is reduced and there is no bad smell.    USE - Method for fermenting organic fertilizer (claimed).    ADVANTAGE - The organic fertilizer improves soil and provides nutrients for growth of crops.    DETAILED DESCRIPTION - Fermentation of organic fertilizer comprises collecting straw, drying, crushing to obtain straw powder, collecting livestock and poultry excrement, drying to obtain dry excrement, collecting traditional Chinese medicine, crushing to obtain traditional Chinese medicine dregs, mixing and stirring materials at straw powder to dry excrement ratio of 3:7 and traditional Chinese medicine dregs to dry excrement ratio of 3:7, mixing with bacterial strain and water to humidity of 60%, detecting carbon/nitrogen ratio, piling to height of 1.2-1.5 m, fermenting at 65 degrees C for 2 days, turning for 3 times and completing fermentation until material color is brown, material volume is reduced and there is no bad smell.
NOVELTY - Molecular identification and production of Lyophyllum mushroom spawn are carried out by performing internal transcribed spacer (ITS) amplification, sequencing amplified product, and comparing basic local alignment search tool (BLAST) homologous data to determine taxonomic status; culturing parent species at 25-27 degrees C and at pH of 6-7 in medium comprising potato, banana, glucose, beef extract, agar, and water; culturing seed in liquid culture medium; culturing cultivars; carrying out seed technology of parent species, original species, and cultivars; and performing mushroom culture.    USE - Method for molecular identification and production of Lyophyllum mushroom spawn (claimed).    ADVANTAGE - The method has short culture period and no pollution, and can increase biological conversion of Lyophyllum mushroom.    DETAILED DESCRIPTION - Molecular identification and production of Lyophyllum mushroom spawn comprise:    (A) carrying out ITS amplification, sequencing amplified product, and comparing BLAST homologous data to determine taxonomic status;    (B) culturing parent species at 25-27 degrees C and at pH of 6-7 in culture medium comprising 100 g potato, 100 g banana, 20 g glucose, 4 g beef extract, 20 g agar, and 100 ml water;    (C) culturing seed in liquid culture medium comprising 70 g grains dipping juice, 200 g potatoes, 20 g glucose, 0.3 g potassium dihydrogen phosphate, 0.15 g magnesium sulfate, 3 g beef extract, and 100 ml water;    (D) culturing cultivars in culture medium comprising 10% grain, 40% peat, 30% corn cob or straw, 18% wheat bran, 1% gypsum, and 1% lime;    (E) carrying out seed technology of the parent species, the original species, and the cultivars; and    (F) performing mushroom culture in culture medium comprising 10% grains, 40% peat, 30% corn cob or straw, 18% wheat bran, 1% gypsum, and 1% lime.
NOVELTY - Fertilizer comprises 30-60 pts. wt. humic acid organic fertilizer, 30-55 pts. wt. caustic sludge, 10-30 pts. wt. salt waste liquid potassium and magnesium fertilizer, 10-25 pts. wt. nitrogen-containing compound and 0.5-2 pts. wt. additive.    USE - Fertilizer.    ADVANTAGE - The fertilizer has quick-acting effect, simple and easy preparation without using equipment, low cost, and high economic benefit. It effectively treats waste alkali, and realizes utilization of waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer comprising taking humic acid organic fertilizer and water, mixing, heating to 30-80 degrees C, adding nitrogen-containing compound, taking alkali residue and potassium magnesium fertilizer, stirring uniformly, carrying out heat preservation reaction for 20-60 minutes to prepare intermediate product; adding additive, reacting for 10-30 minutes; and pelletizing at not greater than 40 degrees C, drying, and crushing.
NOVELTY - Production of N-cyclohexylurea comprises quantitatively adding water, urea and cyclohexane to reactor, reflux heating, reacting for 5-10 hours, cooling, filtering, recovering ammonia, filtering, and drying.    USE - Method for producing N-cyclohexylurea (claimed).    ADVANTAGE - The method solves environmental pollution in wastewater treatment.
NOVELTY - Increasing multi-arc alkali yield of methomyl comprises reacting methyl isocyanate and methomyl aqueous solution, controlling temperature at 5-10 degrees C, adding sodium chloride, separating, filtering, and taking solids.    USE - Method for increasing multi-arc alkali yield of methomyl (claimed).    ADVANTAGE - The simple and low-cost method reduces discharge amount of pollutants in wastewater, and ensures high purity, good quality and strong practicability.
NOVELTY - Production of cloperastine comprises reacting 4-chloro-diphenyl methanol (V) and sulfate catalyst with 2-chlorethanol to obtain 4-chloro-diphenyl ether compound (III); and etherifying compound (III) with piperidine in presence of acid-binding agent to obtain cloperastine (I).    USE - Production of cloperastine.    ADVANTAGE - The method has short and convenient operation, uses cheap and easy to obtain catalyst with high catalytic activity and does not corrode reaction equipment, has less waste pollution, produces superior product quality at high yield, and is suitable for industrial production.    DETAILED DESCRIPTION - Production of cloperastine comprises reacting 4-chloro-diphenyl methanol (V) and sulfate catalyst under 2-chlorethanol to obtain 4-chloro-diphenyl ether compound of formula (III); and etherifying compound (III) with piperidine in presence of acid-binding agent to obtain cloperastine (I). Structures (I), (III), and (V), page 2 tiff, claim 2)
NOVELTY - A tetrafluoropropene-containing mixed refrigerant comprises 10-90 mol.% 1st component and 10-90 mol.% 2nd component in which 1st component is trans-1,3,3,3-tetrafluoropropene and/or 2,3,3,3-tetrafluoropropene, and 2nd component is propane, propylene, isobutane, butane, 1-butene, and/or isobutylene.    USE - A tetrafluoropropene-containing mixed refrigerant.    ADVANTAGE - Tetrafluoropropene-containing mixed refrigerant is environment-friendly and has reduced flammability. high energy efficiency, good intersolubility and safety performance, no ozone-depletion potential (ODP), and low global warming potential (GWP).
NOVELTY - The method involves performing fermentation of raw materials provided through feeding pipe (11). The methane is collected in feeding pipe/discharging pipe (12). The fermentation region is formed between adjacent blocking plates. The biogas slurry liquid level is increased. The biogas slurry is passed to discharging pipe drainage hole. The slurry is returned back to fermentation pipe through unidirectional reflux tube drainage holes. The methane fermentation space is reduced to complete the slurry circulation, when water pressure of biogas storage chamber is lower than predetermined value.    USE - Method for producing methane using bending multi-area super efficient methane fermentation system.    ADVANTAGE - The methane production process is performed easily and efficiently. The biogas slurry circulation effect is improved. The fermentation process is simplified. The uniform distribution of biogas fungus is ensured, such that the yield of methane is not affected. The fermentation route is long.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the super efficient methane fermentation system.    Feeding pipe (11)    Discharging pipe (12)    Discharging pipe (20)    Hydraulic portion (30)    Gas collecting pipe (40)    Drainage pipe (50)
NOVELTY - The device has a feeding pipe (11) and a discharging pipe (12) that are provided with the U-type fermentation pipe (20). The pipe is provided with a water pressure portion. A discharging pipe is provided with a discharging pipe drainage hole. The U type pipe and the feeding pipe are connected by a connecting seat equipped with a feeding tube plate. The discharging pipe plate is provided with an air-blocking plate and the feeding pipe blocking plate.    USE - Curved path long fermentation methane generating device.    ADVANTAGE - The uniform distribution of strain is achieved. The crusting phenomenon is effective prevented. The generation efficiency is improved. The device is fit for large-scale production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the curved path long fermentation methane generating device.    Feeding pipe (11)    Discharging pipe (12)    U-type fermentation pipe (20)    Discharge hole (32)    Gas collecting pipe (50)
NOVELTY - Producing methane gas involves feeding raw material into feeding pipe (40) to produce methane gas in fermentation system. The methane gas is collected in fermentation zone, which is formed between adjacent block plates (34). When gas pressure is increased in fermentation system liquid is flowed in feeding pipe and discharge pipe. The liquid pressure is increased in feeding tube and then liquid is flowed into discharge pipe (20) and drain pipe (44) to the lowest position.    USE - Method for producing methane gas (claimed).    ADVANTAGE - The method enables to produce methane gas in efficient manner.    DETAILED DESCRIPTION - Producing methane gas involves feeding raw material into feeding pipe (40) to produce methane gas in fermentation system. The methane gas is collected in fermentation zone, which is formed between adjacent block plates (34). When gas pressure is increased in fermentation system liquid is flowed in feeding pipe and discharge pipe. The liquid pressure is increased in feeding tube and then liquid is flowed into discharge pipe (20) and drain pipe (44) to the lowest position. When liquid pressure is reduced in fermentation system, liquid is flowed into feeding pipe, discharging pipe, drain pipe and reflux pipe to pipe (30) inside fermentation system. The liquid is collected into other fermentation system to obtain methane gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of methane gas production method.    Discharge pipe (20)    Pipe (30)    Block plates (34)    Feeding pipe (40)    Drain pipe (44)
NOVELTY - Producing methane gas involves feeding raw material into feeding pipe (11) to produce methane gas in fermentation system. The methane gas is collected in fermentation zone, which is formed between adjacent block plates. When gas pressure is increased in fermentation system liquid is flowed in feeding pipe and discharge pipe. The liquid pressure is increased in feeding tube and then liquid is flowed into discharge pipe (12) and drain pipe (50) to the lowest position.    USE - Method for producing methane gas (claimed).    DETAILED DESCRIPTION - Producing methane gas involves feeding raw material into feeding pipe (11) to produce methane gas in fermentation system. The methane gas is collected in fermentation zone, which is formed between adjacent block plates. When gas pressure is increased in fermentation system liquid is flowed in feeding pipe and discharge pipe. The liquid pressure is increased in feeding tube and then liquid is flowed into discharge pipe (12) and drain pipe (50) to the lowest position. When liquid pressure is reduced in fermentation system, liquid is flowed into feeding pipe, discharging pipe, drain pipe and cloth pipe (52) to pipe (20) inside fermentation system. The liquid is collected into other fermentation system to obtain methane gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of methane gas production method.    Feeding pipe (11)    Discharge pipe (12)    Pipe (20)    Drain pipe (50)    Cloth pipe (52)
NOVELTY - A polymeric membrane comprises a polymeric blend comprising a polymer (a) of intrinsic microporosity (PIM) and polymer (b). The polymeric membrane is treated with ultraviolet radiation and plasma.    USE - Polymeric membrane is used for device for separating components and gases (all claimed) e.g. hydrogen/argon, hydrogen/nitrogen, nitrogen/methane, and hydrogen/methane, and recovering hydrogen from ammonia production gas stream, and removing hydrogen from cracked gas e.g. methane, ethylene and propylene.    ADVANTAGE - The polymeric membrane has excellent selectivity, and permeability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for separating 1 or more components from a mixture of components, which involves contacting a mixture of components (c1) on side (s1) of polymeric membrane such that 1 or more components are retained on the side (s1) in the form of retentate and other component (c2) is permeated through the membrane to side (s2) in the form of permeate;    (2) method of treating surface of polymeric membrane; and    (3) gas separation device.
NOVELTY - A treated biomass-derived pyrolysis oil (15) deoxygenating method involves exposing the treated biomass-derived pyrolysis oil to a catalyst having a neutral catalyst support comprising titanium oxide in the anatase phase.    USE - Method for deoxygenating treated biomass-derived pyrolysis oil.    ADVANTAGE - The method enables deoxygenating the treated biomass-derived pyrolysis oil without plugging the reactor, thus improving processability of biomass-derived pyrolysis oil and increasing run duration.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating a method for deoxygenating treated biomass-derived pyrolysis oil.    Biomass-derived pyrolysis oil (15)    Filtration apparatus (20)    Low solids biomass-derived pyrolysis oil (25)    Ion-exchange resin (30)    Fractionator (40)
NOVELTY - The system has U-type pipe (20) whose two ends are respectively attached with feeding pipe (11) and discharging pipe (12). The discharging pipe is provided with a drain hole. The feeding pipe blocking plate is arranged between the feeding pipe and U-type pipe. The discharging pipe blocking plate is arranged between the discharging pipe and U-type pipe. The gas collecting pipe (40) is attached to the top portion of the U-type pipe. The lowest position of discharging pipe drain hole is higher than the lowest point of feeding pipe drain hole.    USE - Dragon-type multiple partition ultra-efficient bacterial cloth integrated marsh gas fermentation system.    ADVANTAGE - Uniform distribution of bacteria can be ensured, so that the crushing phenomenon can be prevented effectively and gas production rate can be improved. The fermentation efficiency of the system can be improved, so that the system can be used for large-scale production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the dragon-type multiple partition ultra-efficient bacterial cloth integrated marsh gas fermentation system.    Feeding pipe (11)    Discharging pipe (12)    U-type pipe (20)    Water pressure chamber (30)    Gas collecting pipe (40)
NOVELTY - Producing bio-methane, comprises (a) providing a first organic waste, (b) injecting a methanogenic anaerobic microorganisms mixture in the first organic waste, (c) primary anaerobic culturing the organic waste and microorganisms mixture by stirring under mesothermal temperature, (d) precipitating the primary anaerobic culture, (e) discharging the remaining effluent after precipitation, and secondary anaerobic culturing secondary organic waste by stirring under mesothermal temperature, and (f) adding trace metals into the primary and secondary anaerobic culture.    USE - The method is useful for producing bio-methane (claimed).    ADVANTAGE - The method is economical.
NOVELTY - The apparatus has a septic tank that is completely anoxic and is separated from the atmosphere. The septic tank is connected with a biogas collection and power generating component. One end of tube is connected with septic tank and the other end is connected with multiple external biogas storage tanks (16). The gas generator (15) is attached to biogas storage tank.    USE - Septic tank apparatus for producing electricity from biogas with enhanced methane content from septic tank.    ADVANTAGE - The modified methanogenic microorganism can be optimized to produce methane gas from domestic wastes, so that the bacteria cultured with the optimized anaerobic bacteria can be flushed down the toilet or dumped down the sink. Thus the gas production rate can be increased effectively. The additional bacteria is genetically modified to amplify the amount of methane product to the significant level.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for enhancing methane content in biogas produced by septic tank system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of septic tank apparatus for producing electricity from biogas with enhanced methane content.    Baffle (1)    Access port (2)    Gas outlet (3)    Liquid outlet (5)    Insulating layer (6)
NOVELTY - Production of sugars from biomass including at least one polysaccharide, comprises putting a biomass in contact with an aqueous solution of at least one organic acid having 1-6C atoms, preferably 1-3C atoms, where the pH of the aqueous solution is 0.6-1.6, preferably 0.9-1.3.    USE - The process is useful for production of sugars from biomass including at least one polysaccharide, where the sugars are used as carbon sources in fermentation processes for the production of alcohols (ethanol, butanol), diols (1,3-propanediol, 1,3-butanediol, 1,4-butanediol or 2,3-butanediol) , lipids, or other intermediates or products, the alcohols, diols, lipids, or other intermediates or products, are used in the chemical industry or in the formulation of fuels for motor vehicles, and the alcohols and the diols are used in the bio-butadiene production (all claimed).    ADVANTAGE - The process provides high yield sugars having 5-6 carbon atoms higher than or equal to 95% can be obtained.
NOVELTY - Biomass is fed into reactor (20), heated in presence of aluminosilicate zeolite catalyst and converted to gaseous product stream (30) comprising p-xylene. The catalyst is manufactured to contain 0.2 wt.% or more iron or pretreated to contain 0.2 wt.% or more iron. The iron is not derived from biomass or reactor walls.    USE - Conversion of biomass to liquid hydrocarbon e.g. p-xylene used as starting material for plasticizer, polyester fiber and terephthalic acid for production of plastic bottles and clothing.    ADVANTAGE - The method enables conversion of biomass to p-xylene with high selectivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of catalyst, which involves providing zeolite catalyst, treating the catalyst to increase the iron content and applying siliceous coating to catalyst, to obtain iron-modified zeolite catalyst having siliceous coating;    (2) hydrocarbon mixture, which comprises biomass-derived mixture of 14C hydrocarbons comprising 10 %mass or more xylene including 85-91% p-xylene;    (3) chemical system, which has a reactor comprising iron-modified zeolite catalyst, biomass and hydrocarbon product stream comprising 10 %mass or more xylene. 80% Or more of xylene is p-xylene; and    (4) aluminosilicate zeolite catalyst, which has silicon/aluminum molar ratio of 100 or less.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the conversion of biomass to liquid hydrocarbon.    Feed stream (10)    Moisture (12)    Dryer (14)    Reactor (20)    Product stream (30)
NOVELTY - Microecological formulation comprises liquid culture of Saccharomyces cerevisiae, Pichia anomala, Rhodopseudomonas palustris, Bacillus licheniformis, B.subtilis, B.megaterium, Streptomyces microflavus, Lactobacillus acidophilus, L.plantarum, and Streptococcus thermophilus, where the liquid culture is obtained using culture medium that comprises molasses, sodium chloride and urea, and the formulation has viable cell count of 1x 1010 colony forming unit (cfu)/ml.    USE - The microecological formulation is useful for sewage purification and deodorizing garbage (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the microecological formulation, which involves (a) preparing seed culture of the above-mentioned strains, (b) preparing liquid culture comprising the above-mentioned strains, (c) performing fermentation using the liquid culture, and (d) continuing fermentation under stirring condition until the cell count reaches 1x 1010 cfu/ml.
NOVELTY - Soil remediation agent comprises maggot dung (65-75wt.%), molasses (10-15 wt.%) and sodium bentonite (15-20 wt.%).    USE - Soil remediation agent used for soil improvement and soil acidification, and for improving soil after desertification and earthquake (all claimed).    ADVANTAGE - The soil remediation agent is stable and easy to use, and has long lasting effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing soil remediation agent, which involves:    (A) mixing maggot dung, molasses and sodium bentonite;    (B) moistening the obtained mixture with water to obtain fermentation matrix having 60-65% water content;    (C) mixing fermentation matrix with 0.3-0.5% of bacilli liquid;    (D) fermenting the material in piles for 3-5 days in summer and autumn, and for 8-10 days in winter and spring;    (E) granulating the obtained mixture to obtain granulated material;    (F) charring the granulated material in oxygen-free or low-oxygen environment at low temperature; and    (G) cooling the charred material to obtain the final product.    .
NOVELTY - Organic fertilizer comprises human urine (10-26 pts. wt.), longan shell (20-30 pts. wt.), peanut shell (20-40 pts. wt.), sweet potato powder (10-20 pts. wt.), silkworm excreta (50-70 pts. wt.), calcium nitrate (15-30 pts. wt.), potassium nitrate (15-30 pts. wt.) and biological amino acids (6-20 pts. wt.).    USE - Organic fertilizer used for corn.    ADVANTAGE - The organic fertilizer is used in drought and water logging states, and has simple production process and high fertilizer content, and promotes absorption of nutrients.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) pulverizing longan shells, peanut shells and sweet potato powder;    (B) adding human urine, silkworm excrement, biological calcium nitrate and amino acids to pulverized powder;    (C) mixing the obtained material;    (D) adding 30% water to the obtained material;    (E) processing the obtained mixture in fermenter under stirring condition at 40-45 degrees C for 72 hours;    (F) cooling the fermentation tank;    (G) drying and granulating the obtained material; and    (H) packaging the obtained material.
NOVELTY - Biofertilizer comprises 33-37 wt.% vermicompost, 27-31 wt.% straw, 4-8 wt.% bamboo shavings, 1-3 wt.% amino acid, 5.5-9.5 wt.% humic acid, 4.5-8.5 wt.% plant ash, 0.2-2.2 wt.% lees, 1-3 wt.% wheat bran, 7-10 wt.% cow dung, 0.6-1 wt.% trace elements, and 0.5-1 wt.% microbial agent.    USE - The biofertilizer is useful for improving soil texture (claimed).    ADVANTAGE - The biofertilizer improves soil ecological environment, increases yield and quality of agricultural products, and is simple, cost-effective and easy to prepare.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the biofertilizer, which involves mixing the above-mentioned materials, performing fermentation, collecting fermented product, drying and crushing product, pelletizing crushed product, and drying pellets.
NOVELTY - Synergistic compound fertilizer comprises 75-90 pts. wt. nitrogen fertilizer, 1-3 pts. wt. zeolite powder, 1-5 pts. wt. iron, 1-3 pts. wt. manganese, 1-5 pts. wt. potassium, 0.5-1 pt. wt. ammonium lauryl sulfate, 1-3 pts. wt. water retention agent, 2-4 pts. wt. complex microbial agent and 1-3 pts. wt. bentonite.    USE - Synergistic compound fertilizer.    ADVANTAGE - The synergistic compound fertilizer increases crop yield, and reduces amount of irrigation.
NOVELTY - Preparation of 2,4-difluoro-benzoic acid involves providing 2,4-dinitrotoluene as raw material, and obtaining 2,4-difluoro-benzoic acid by oxidizing using potassium permanganate as oxidant and potassium fluoride as fluorinating agent.    USE - Preparation of 2,4-difluoro-benzoic acid (claimed).    ADVANTAGE - The method enables simple, economical and environmentally-friendly preparation of 2,4-difluoro-benzoic acid with high yield.
NOVELTY - Nalidixic acid is prepared by reacting 2-amino-6-methylpyridine and diethyl ethoxymethylenemalonate at 90 degrees C to obtain intermediate A; reacting intermediate A with diphenyl ether at 200-230 degrees C to obtain intermediate B; adding intermediate B and dimethylformamide (DMF), heating to 40 degrees C, stirring, adding potassium carbonate, then dropwise adding bromoethane, and reacting to obtain intermediate C; and adding intermediate C, water and tetrahydrofuran to a reaction kettle, stirring, adding sodium hydroxide, refluxing, and evaporating tetrahydrofuran to obtain nalidixic acid finished product.    USE - Method of preparing nalidixic acid (claimed).    ADVANTAGE - The method has short reaction time, reduced cost of reactants and reduced occurrence of impurities, and increased finished product quality.    DETAILED DESCRIPTION - Preparation of nalidixic acid comprises:    (A) charging 2-amino-6-methylpyridine and diethyl ethoxymethylenemalonate to a reaction container, stirring, heating to 90 degrees C and reacting, then cooling to room temperature to obtain crude product, and purifying crude product to obtain intermediate A;    (B) adding diphenyl ether in a reaction container, heating at 200-230 degrees C, adding intermediate A, and refluxing until material is consumed up, and subjecting reaction liquid to post-treatment to obtain intermediate B;    (C) adding intermediate B and DMF, heating to 40 degrees C, stirring, adding potassium carbonate, then dropwise adding bromoethane, and reacting to obtain intermediate C; and    (D) adding the intermediate C, water and tetrahydrofuran to a reaction kettle, stirring and dissolving, adding sodium hydroxide, refluxing, and evaporating tetrahydrofuran to obtain nalidixic acid finished product.
NOVELTY - Bacillus licheniformis strain UTM107 (CGMCC NO: 9678) is new.    USE - The strain is useful: for producing high temperature keratinases, allantoin enzyme, cellobiase and beta -endoglucanase; in organic solid waste compost fermentation; and preparing organic fertilizer (all claimed).    ADVANTAGE - The strain can decompose organic matter in waste, is environmentally friendly, and has excellent performance in processing organic solid waste to realizes harmlessness.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) use of strain in producing high temperature keratinases, allantoin enzyme, cellobiase and beta -endoglucanase; (2) Bacillus licheniformis UTM107 containing microbial inoculum; (3) preparing Bacillus licheniformis UTM107 containing microbial inoculum comprising (i) preparing fermentation liquid, inoculating Bacillus licheniformis strain UTM107 in lysogeny broth (LB) liquid culture medium and fermenting, and (ii) drying fermentation liquid to obtain powder; (4) use of Bacillus licheniformis strain UTM107 or microbial inoculum in organic solid waste compost fermentation; and (5) the application method of strain UTM107 or microbial inoculum comprising (i) inoculating 0.1-1% strain UTM107 or microbial inoculum in organic solid waste, mixing uniformly, carrying out aerobic compost fermentation, where the organic solid waste material according to nitrogen ratio is 10-50:1, the water content is 45-65%, maintaining oxygen content at 8-15%, carry out compost fermentation, at interval of 3-5 days, turning once, and (ii) composting for 12-20 days, reducing material moisture to 28-33%.
NOVELTY - Spouted fluidized bed reactor comprises bottom-divided reaction zones, which are connected in turn to buffer zones, and fast pyrolysis main reaction zone. The subsequent secondary pyrolysis and combustion of biomass in the fast pyrolysis main reaction zone generates unreacted or completely pyrolyzed biomass aside. The generated pyrolytic carbon and biofuel by the condensation of pyrolysis gas confirms the stability of airflow during the operation.    USE - Spouted fluidized bed reactor.    ADVANTAGE - The spouted fluidized bed reactor is capable of controlling fast pyrolysis reaction occurring at high temperature precisely, and thus resulting in significantly increament in the producion of pyrolytic carbon and biofuel by condensation of pyrolysis gas. Thus, the spouted fluidized bed reactor is applicable on large-scale.
NOVELTY - A bromine-carrying carbon adsorbent comprises carbon-based porous absorption material with surface containing vapor-deposited bromine radicals for inhibiting nitrogen (N2) adsorption.    USE - A bromine-carrying carbon adsorbent for absorptive separation of methane/nitrogen (CH4/N2) in coal bed gas (claimed).    ADVANTAGE - Bromine-carrying carbon adsorbent increases separation coefficient of CH4/N2.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of bromine-carrying carbon adsorbent which involves paving untreated activated carbon on porcelain boat, placing in high-temperature tubular furnace, introducing N2 with flowrate of 3-20 ml/minute, blowing bromine vapor using liquid-bromine containing bromine vapor production bottle, heating to 300 degrees C, maintaining temperature for 5 hours, taking out sample, placing in fume hood, and naturally cooling with mass change rate of less than or equal to 0.5%/hour.
NOVELTY - A catalyst comprises modified natural graphite with free electrons as main body raw material, and catalyst carrier active component comprising nickel, rhodium or ruthenium, ferroferric oxide and alkali metal oxide.    USE - Catalyst used for coal methane and carbon monoxide reaction (claimed).    ADVANTAGE - The modified graphite has good porous structure and surface property. The catalyst has fast transmission of methanation heat to coal surface for coal pyrolysis, thus saving energy. The method increases utilization rate and yield of coal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catalyst comprising crushing natural graphite to granularity of 5 mesh, heating at 800-1000 degrees C for 3-5 hours in presence of nitrogen gas, carbon dioxide gas or oxygen gas to obtain modified porous graphite, soaking in mixed solution of active component and alkali metal nitrate for 6-10 hours, filtering, oven-drying at 110 degrees C to constant weight, baking under nitrogen atmosphere at 600-900 degrees C for 3-5 hours, soaking in 1-10% ferric nitrate for 6-10 hours, oven-drying at 110 degrees C to constant weight and baking under nitrogen atmosphere at 600-900 degrees C for 3-5 hours.
NOVELTY - Purification of raltitrexed involves dissolving raltitrexed crude in alcohol solvent or/and ester solvent, heating in water bath, stirring, heat-preserving, filtering, cooling obtained filtrate, crystallizing, filtering, washing with alcohol solvent and/or ester solvent, and drying.    USE - Purification of raltitrexed (claimed).    ADVANTAGE - The method enables simple, environmentally-friendly and economical purification of raltitrexed with high yield of 90%, and provides high-quality raltitrexed.
NOVELTY - A method for gasification of unsegregarted waste to produce high energy gas fuel, which method comprises: gasification of unsegregated waste feed in an inert, oxygen-free atmosphere, in an endothermic thermolysis reaction chamber to thus gasify the same in the absence of substantial by-production of liquid reaction products; said thermolysis chamber comprising a dense bed of heated fluidized sand bed and unsegregated solid waste; the heat energy required for said thermolysis reaction being generated by the exothermic combustion reaction zone; the heated fluidized sand bed and unsegregated waste in said endothermic thermolysis reaction zone being in communicating relationship with the heat obtained from the combustion reaction zone in said exothermic combustion chamber; the process of application of superheated steam to the plastic and styrofoam in the unsegregated waste, converting it into brittle form thus, easily ground to reduce its size, and said process of combustion and thermolysis of producing high energy gas fuel is clean-air-act compliant as there is no odor, smoke, and the flu gas is purified and recycled as oxidant for proper combustion.    USE - Thermolysis method and apparatus for production of high energy gas fuel from unsegregated wastes.    DESCRIPTION OF DRAWING(S) - The drawing shows the thermolysis process.
NOVELTY - The method involves pumping lipid into water in electromagnetic field processor to process an electromagnetic field. The alkali catalyst and solvent are added in a reactor, in which alkali catalyst is provided by sodium hydroxide and calcium hydroxide. The solvent is added with methyl alcohol and isopropyl alcohol, for carrying out supercritical reaction in reactor. The reaction condition is set with 400-500 degrees C, pressure of 10-25MPa and time of 30-60 min to get product enter into tower fractionation and decompression fractionation, to obtain biological diesel oil product.    USE - Preparation method of biological diesel oil.    ADVANTAGE - The biological diesel oil is prepared with high yield, catalyst high selectivity, convenient for the subsequent separating.
NOVELTY - The method involves mixing pre-processing oil uniformly with biomass oil and source oil or heavy crude oil at normal temperature. Insulin is added with constant temperature water, where biomass oil is selected from turpentine oil, castor oil, tung oil, palm oil, soybean oil, sunflower seed oil, rapeseed oil, peanut oil or corn blank bud oil.    USE - Source oil or heavy crude oil distillation strengthening method.    ADVANTAGE - The method enables ensuring green and environment-friendly level, providing mild normal pressure distillation reaction condition and increasing gas productivity and operation convenience.
NOVELTY - Method of preparing compost, involves mixing kitchen garbage, corn straw and phosphogypsum paste, adding compost material and performing aerobic fermentation to obtain the product.    USE - The method is useful for preparing compost (claimed).    ADVANTAGE - The method reduces discharge amount of methane and ammonia during compost process, and is simple, cost-effective and environmentally-friendly.
NOVELTY - An organic-inorganic microorganism fertilizer comprises 20-40 wt.% potassium humate, 13-16 wt.% potassium chloride, 5-16 wt.% urea, 26-28 wt.% diammonium phosphate, 1-3 wt.% zinc sulfate, 2-4 wt.% ferrous sulfate, 1-3 wt.% borax, 4-6 wt.% microorganism preparation, 0.5-1.5 wt.% copper, 0.5-1.5 wt.% manganese sulfate, and 2-4 wt.% EDTA.    USE - Organic-inorganic microorganism fertilizer for peanut (claimed).    ADVANTAGE - The fertilizer is environment-friendly and improves farmland soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer comprising mixing humate powder and microorganism preparation; keeping at 35-45 degrees C for 7-12 days; crushing urea, potassium chloride, and diammonium phosphate, passing by 20 items sieve, and mixing; crushing zinc sulfate, manganese sulfate, ferrous sulfate, borax, copper, and EDTA, passing by 20 items sieve, and mixing; and mixing all materials and packing.
NOVELTY - Preparation of high purity triisopropyl silylacrylate involves taking triisopropyl silanol and acid-binding agent at mol ratio of 1:1.1-1.4, mixing with 350-450 mL solvent, adding 0.02-0.04 wt.% phenothiazine or copper acetate, heating at 10-80 degrees C, adding acryloyl chloride dropwise, filtering, taking liquid and distilling.    USE - Method for preparing high purity triisopropyl silylacrylate (claimed) used for making bullet-proof helmet.    ADVANTAGE - The high purity triisopropyl silylacrylate has high strength and good toughness. It is non-toxic and environmental-friendly.
NOVELTY - Separation purification of etimicin is carried out by sending etimicin hydrolysis liquid to continuous chromatographic column, eluting with solvent, collecting elution liquid, concentrating and drying to obtain purified etimicin.    USE - Method for separation purification of etimicin (claimed).    ADVANTAGE - The method involves continuous process, has high etimicin yield, high etimicin purity, and low cost, and is environment-friendly, and suitable for industrial production.
NOVELTY - Separation of methane-carbon dioxide-nitrogen multicomponent involves filling two-parallel adsorption bed with flexible material TUTCH-1 or TUTCH-2 as an adsorbent, introducing methane-carbon dioxide-nitrogen mixture gas through adsorbent bed (a1), adsorbing methane and carbon dioxide, collecting nitrogen gas from the outlet, closing the intake valve, collecting methane and residual carbon dioxide gas remaining in the adsorbent bed, closing the adsorbent bed (a1), mixing the feed gas to switch to adsorbent bed (a2) and repeating the above process using TUTCH-1 and TUTCH-2.    USE - Separation of methane-carbon dioxide-nitrogen multicomponent used for liquefied natural gas and compressed natural gas for vehicle.    ADVANTAGE - The separation of methane-carbon dioxide-nitrogen multicomponent is efficiently performed, with methane separation rate of more than 98%. The method can completely separate carbon dioxide and nitrogen.    DETAILED DESCRIPTION - Separation of methane-carbon dioxide-nitrogen multicomponent involves filling two-parallel adsorption bed with flexible material TUTCH-1 or TUTCH-2 as an adsorbent, controlling adsorbent bed inlet pipeline temperature to 25 plus minus 5 degrees C, introducing methane-carbon dioxide-nitrogen mixture gas through adsorbent bed (a1) in the two-parallel adsorption bed, controlling pressure of the adsorption bed by back pressure valve, adsorbing methane and carbon dioxide, collecting nitrogen gas from the outlet, closing the intake valve, collecting residual methane and carbon dioxide gas remaining in the adsorbent bed, closing the adsorbent bed (a1), mixing the feed gas to switch to adsorbent bed (a2) in the two-parallel adsorption bed, and repeating the above process using TUTCH-1 under inlet pipe pressure of 4 MPa and TUTCH-2 under inlet pipe pressure of 6 MPa. An INDEPENDENT CLAIM is included for device for separation of methane-carbon dioxide-nitrogen multicomponent.
NOVELTY - Treating aquaculture wastes, by (a) mixing bacteria, husk powder or wet chicken coop and wet manure or waste feed, covering with cloth or woven, and turning, (b) scraping chicken manures in a chicken house to a blending area of a fermenting workshop, and crushing illness-caused dead chickens into fragments, and (c) in the blending area of the fermenting workshop, blending chicken manures with fragments, spreading crop straws and product obtained in step (a), transferring to fermentation tank, fermenting, turning once a day, drying, and sieving obtained product.    USE - The method is used for treating aquaculture wastes biologically which is used as an organic fertilizer (claimed).    ADVANTAGE - The obtained organic fertilizer has organic matter content of greater than or equal to 60%, and total nutrient content of greater than or equal to 60%.    DETAILED DESCRIPTION - Method for treating aquaculture wastes biologically, involves (a) mixing bacteria, husk powder or wet chicken coop and wet manure or waste feed in ratio of 1:200-300:2-3, adjusting moisture content to 40-45%, forming the mixture into pile, covering with cloth or woven, maintaining at 30 degrees C for greater than or equal to 24 hours, and turning the mixture, (b) scraping chicken manures in a chicken house to a blending area of a fermenting workshop by using an automatic manure scraping machine, and crushing illness-caused dead chickens into fragments of 2-3 cm using crusher, and (c) in the blending area of the fermenting workshop, blending the chicken manures with the fragments, spreading crop straws and 0.2-1 wt.% product obtained in step (a), adjusting moisture content to 50-55%, transferring to fermentation tank, fermenting at 65-70 degrees C for 15-21 days, turning once a day, where moisture content of obtained product after fermentation is 35-40%, drying, and sieving obtained product.
NOVELTY - Method for producing saline-alkali soil remediation agent, involves dissolving carbon source, nitrogen source, phosphorus source and potassium source in at least portion of 100 pts. wt. 60-100 degrees C water, stirring, cooling to 18-40 degrees C, adding effective microorganism, adding remaining water and 5-10 pts. wt. weathered coal, stirring, and fermenting at 38 degrees C for 3-7 days, where viable count of effective microorganism is (2-9)x 109 colony forming units (CFU) per g weathered coal.    USE - The method is used for producing saline-alkali soil remediation agent (claimed).    ADVANTAGE - The produced agent has carbon content of 10-20 wt.%, nitrogen content of 0.5-0.6 wt.%, phosphorus content of 0.4-0.5 wt.% and potassium content of 0.35-0.45 wt.%, and improves soil fertility.
NOVELTY - Universal seedling matrix comprises organic mixture, peat, perlite, vermiculite, plant ash and a small amount of inorganic fertilizer.    USE - The universal seedling matrix is useful for soilless cultivation of vegetable and fruit plants, flowering plants and cotton.    ADVANTAGE - The universal seedling matrix has light texture and is rich in nutrients and cost-effective as vinegar residue, cassava waste residue and other organic waste are utilized as raw materials.
NOVELTY - The present invention is discovered a new technology to cut the solid biomass cellulose and hemicellulose polymer into small molecules by using ionic scissors. The special chemicals of small molecules are separated from the aqueous solution for applications. The cutted small molecules in aqueous solution are for reducing into another types of special chemicals and then separated into solid and liquid special chemicals or their mixtures and etherization to produce the green transportation fuel.
NOVELTY - The present invention provides a membrane electrode assembly and method for fabricating the same. The membrane electrode assembly is used for hydrogen generation and comprises a proton exchange membrane, having a first surface and a second surface; a first catalytic layer, disposed on the first surface of the proton exchange membrane; a second catalytic layer, disposed on the second surface of the proton exchange membrane; two gas diffusion layers, disposed on the first catalytic layer and the second catalytic layer, respectively; and two conductive layers, being in contact with the two gas diffusion layers for providing electric power for electrolysis.
NOVELTY - The utility model is new type relates to one kind full print patch-type medicine taking reminder, the full print patch-type medicine taking reminder using the screen print method for electric conduction are printed by conductive ink on flexible material on, the flexible upper material set with regulating time and alarm clock is set with key, used for alarm and loudspeaker, used for module of mode display and storage data of the PET film the utility new type for neodymium iron boron magnet and print coil respectively set in double layer parallel with gap and at the time when the alternating magnetic field direction neodymium iron boron magnet generating the magnetic field and fixed print coil produce the same, substrate for neodymium iron boron magnet, the printed coil and the PET film mutually, when magnetic field direction when generating the two different, mutually separate. The utility model is new type of beneficial effect is: because of flexible material is attached on the medicine bottle on, can remind the patient take medicine. And the reminding device has simple structure, low cost, and it is economical and environment-friendly.
NOVELTY - The disposable infusion apparatus has a puncture device that is set with a puncture device cap (3) and a puncture outfit (2). A transfusion pipe is provided in upper end of a discharge pipe (1). A regulator (9) is connected with the lower end of a dropper pipe (8), and mounted with the transfusion pipe. The regulator is provided with two round holes and directly connected in series with the transfusion pipe. A transfusion filter (11) is set in the end of transfusion pipe. The transfusion filter and the transfusion pipe are connected integrally.    USE - Disposable infusion apparatus for use in clinic.    ADVANTAGE - Since the transfusion filter is set in the end of transfusion pipe, the height of transfusion is adjusted easily. The need for separating needle and connecting tube is avoided, and the drug and air pollution is eliminated. The convenience of nursing personnel is improved. The nursing time and cost are saved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the disposable infusion apparatus.    Discharge pipe (1)    Puncture outfit (2)    Puncture device cap (3)    Dropper pipe (8)    Regulator (9)    Transfusion filter (11)
NOVELTY - Loading an axial-radial flow vessel containing a bed of a particulate catalyst having a radial-flow portion and an axial-flow portion supported on and in fluid communication with the radial flow portion, by (a1) placing a first catalyst material in the radial-flow portion and (a2) placing a second catalyst material in the axial-flow portion, where second catalyst material has a smaller particle size than the first catalyst material is claimed.    USE - The method is useful for loading axial-radial flow vessel which is used for performing a catalyzed reaction (claimed) which is exothermic or endothermic.    ADVANTAGE - The method provides more effective loading profile than where the only catalyst particles in the axial flow portion are the same as those on the radial-flow portion.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) the axial-radial flow vessel containing bed of particulate catalyst, where the bed comprises first catalyst material in the radial-flow portion and second catalyst material in the axial-flow portion and the second catalyst material has a smaller particle size than the first catalyst material; and    (2) performing a catalyzed reaction by passing process fluid through vessel containing first catalyst material and a second catalyst material.
NOVELTY - A plant cell, plant seed, or plant comprising a nucleic acid construct comprising a nucleic acid encoding a polypeptide with greater than or equal to 80% sequence identity with any of the defined sequences of 320, 324, 346, and 327 amino acids (SEQ ID NO. 1, 3 5, and 7), given in the specification, that is operably linked to a heterologous promoter operable in a plant tissue, is new.    USE - The plant cell, plant seed, or plant is useful for harvesting lipid or oil and for manufacturing biofuel from the lipid or oil (all claimed). The nucleic acid is useful for increasing the amount of harvestable amount of plant oils from plants/acre, for decreasing the cost/liter of plant oil, and for growing oil crop plants for increasing the amount of harvestable oil in plants destined as sources of biofuel.    ADVANTAGE - The plant and nucleic acid are used for low cost and high yield lipid or oil and biofuel production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method comprises (a) transfecting a plant tissue or plant cell with a nucleic acid construct comprising a nucleic acid encoding a polypeptide with greater than or equal to 40% sequence identity with an amino acid sequence selected from SEQ ID NO. 1, 3 5, and 7, that is operably linked to a heterologous promoter operable in a plant tissue; and (b) growing the tissue or the cell into a whole plant; and    (2) a method comprises (a) growing a plant from a seed with a nucleic acid construct comprising a nucleic acid encoding a polypeptide with greater than or equal to 40% sequence identity with an amino acid sequence selected from SEQ ID NO. 1, 3 5, and 7, that is operably linked to a heterologous promoter operable in a plant tissue; and (b) harvesting lipid or oil from the plant or a portion of the plant.
NOVELTY - The device has feeding buffer (2) whose inside middle portion is set with stirrer (3). Air inlet pipe (6) is set at bottom of feeding buffer whose top portion is set with sealing cover (8). Sealing ring is arranged between stirrer and cover. Bottom inlet of feeding buffer is provided with transverse spiral propeller (10) arranged with feed opening (4). Upper portion of discharge end of transverse spiral propeller is set with reactor main portion (1) and lower portion is set with discharge opening. Inner and outer ends of propeller are set with spiral push rod (11) and motor (12).    USE - Feedstock device used for anaerobic fermentation of straw.    ADVANTAGE - The stability of the feedstock device can be improved and the production efficiency of the device can be increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of feedstock device used for anaerobic fermentation of straw.    Reactor main portion (1)    Feeding buffer (2)    Stirrer (3)    Feed opening (4)    Air inlet pipe (6)    Sealing cover (8)    Transverse spiral propeller (10)    Spiral push rod (11)    Motor (12)
NOVELTY - The device has electrolytic aqueous built liquid chamber (1) that is made of cylindrical structure. An inner wall of liquid chamber is provided with a heat preservation cavity (4). The liquid chamber is provided with temperature control device which includes electric heating silk (5). The electric heating silk is set inside heat preservation cavity. The electric heating silk is connected with controller (7) through lead. The controller is connected with power source (8) by lead. A temperature sensor (6) is set in liquid chamber, and is connected with controller through lead.    USE - Anti-freezing hydrogen generator device used for vehicle.    ADVANTAGE - The simple structure of anti-freezing hydrogen generator device is achieved. The good heating heat preservation effect is achieved. The good anti-freezing effect of vehicle hydrogen generating device is improved. The vehicle can be effectively used in winter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anti-freezing hydrogen generator device used for vehicle.    Electrolytic aqueous built liquid chamber (1)    Heat preservation cavity (4)    Electric heating silk (5)    Temperature sensor (6)    Controller (7)    Power source (8)
NOVELTY - The system has a thermo-electric mixed air conditioner equipment connected with an absorption refrigerating unit and a fuel cell for generating an electrochemical reacted electric energy. A mixed power type air conditioner unit of the thermo-electric mixed air conditioner equipment is connected with a power supply. An absorption refrigeration unit is connected with an electric-absorption type air conditioner unit. The absorption refrigeration unit absorbs water hydrogen production by reforming a methanol and waste of refrigeration. An electric heat type air conditioner unit cools the cell.    USE - Methyl alcohol water hydrogen generation system.    ADVANTAGE - The system has better environment-friendly and energy-saving effects, convenient use, small influence and better utilization effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a methyl alcohol water hydrogen generation system control method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a methyl alcohol water hydrogen generation system. '(Drawing includes non-English language text)'
NOVELTY - A fuel additive comprises 2.5-3.5 wt.% nano-potassium carbonate having size of 40-80 nm, 4.5-5.5 wt.% nano-magnesium peroxide having size of 40-80 nm, 1.5-2.5 wt.% nano-silver chloride having size of 40-80 nm, 27-33 wt.% isopropanol, and 57-63 wt.% cetanol.    USE - Fuel additive is used for marine bunker-A oil.    ADVANTAGE - The additive improves the combustion efficiency of fuel.
NOVELTY - The new type utility claims have a a urine collection device, a urine and stool. Urine including one end opening of hollow pipe body and a hollow pipe body and opening matching the cover body, side wall moving the open mouth and a hollow pipe body connected with urine to a urine holding cup, a cup opening of hollow pipe body connected. A urine collecting device, comprising a urine cup, when use, side moving opening and cup wall of the hollow pipe body connected with, the user hand-hold hollow tube body holding a urine holding cup, collecting urine. When after urine collection, a incline urine, urine from opening of hollow tube body entering into a hollow tube shape. When urine after entering into hollow pipe body, a hollow tube body from a cup side wall taken down, a cover body, a centrifugal equal for operation. A urine collection device has simple structure, is convenient to collect urine, and no need to carry out a time transfer, sanitary and clean reducing have the probability of a pollute.
NOVELTY - The utility model is new type supply have a a novel convenient western medicine bottle, comprising a bottle body, a bottom cover, a drying device, a hole, a bottle cover, a weight groove, a bottle, the bottle body is set as lower end through screw thread and bottom cover connected, bottom cover is connected with a cylindrical drying device, the internal is equipped with drying agent, outside surface provided with a hole, the bottom is provided with a circular weight medicine bottle groove, inner surface provided with screw thread, and a bottle mouth connected with, the utility new type has simple structure, when dispensing at a clinic, can avoid the medicament bottle and crashed to prevent patient information off a single medicine wetting and fast when a data tablet suitable and avoids pollute, relieving have working difficulty of medical personnel.
NOVELTY - The utility model is new type relates to biochemical experiment device, and more particularly, to a EP tube a batch by hand mixing, the EP tube batch by hand mixer, comprising a support, a bottom plate, a handle protecting cover, a bottom plate fixed on a upper support, a bottom plate set with through hole, handle fixed link on a support on a support a middle part, protection cover moving, the utility model is new type structure is simple, design is reasonable, because of a carry out mixing uniformly by hand, it will not produce noise and pollute, fit a super-clean workbench at a use, and can realize batch mixing uniformly, with a high efficiency and practicability, and the EP tube by hand mixer batch production cost, energy saving and environment-friendly, widely fit and use.
NOVELTY - The utility model is new type supply have a novel medicament. traditional Chinese medicine split charging device, belonging to medicine split charging device technology field, comprising medicinal sieve, a medicine bag, also comprises rotating shaft, baffle plate, sieve pores, and a photoelectric sensor, the bottom of the medicinal sieve of rotating plate and fixing plate composed of, as follows medicinal sieve funnel provided with a traditional Chinese medicine bag connected, sieve of rotary drive rotating shaft, rotating speed and vibration strength of a control, the utility model is new type. The beneficial effect is: a medicine split charging process can realize automatic, operating information to the real time control, and when error can be timely to remedy to avoid medicine is pollute, sanitary, fast and accurate, which greatly increase have working efficiency of medical personnel.
NOVELTY - The new type utility claims have a micro-aeration plant strengthening ecological floating bed sewage treatment device, the device comprising aquatic plant, floating carrier, a filler layer, micro-pore aeration pipe, bracket, and the aeration machine, the upper floating carrier formed with plant hole, an aquatic plant planting a plant on a floating carrier a, floating in a micro-aeration strengthening ecological floating bed sewage treatment device and a water surface, a lower part set with a filler layer, a micro-aeration pipe through bracket laying annular micro-aeration strengthening ecological floating bed at a bottom of a sewage, and the aeration machine connected with a micro-aeration pipe at a bottom. The utility model is new type micro-aeration system for a device for aerating and charging oxygen, thus promoting the plant root system and growing the microorganism at a filler layer, promoting microorganism and a synergistic effect of aquatic plant system, can repeatedly use, would not to cause pollute water body, low cost, and it is very fit a large square meter in the natural water body pollute treatment.
NOVELTY - The apparatus has a hopper (16) installed on a frame (10) and freely moved forward and backward in a screw case (12) in which the dies (14) are installed. A heating portion (20) is installed in front of the dies, for performing pyrolysis of a workpiece transferred by the screw case. A pusher (16b) is installed within the hopper in the longitudinal direction and is actuated with an actuator (16a) for pushing and extruding the workpiece into the screw case through the hopper. A molding unit (60) is provided for discharging the chute from the extruded workpiece through the dies.    USE - Device for manufacturing renewable fuels from domestic waste and industrial waste.    ADVANTAGE - The operability of the device and the structural stability of the workpiece are improved while suppressing the damage to the workpiece so that the manufacturing of the renewable fuels with high quality is ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of the device for manufacturing of renewable fuels.    Frame (10)    Screw case (12)    Dies (14)    Hopper (16)    Actuator (16a)    Pusher (16b)    Heating portion (20)    Molding unit (60)
NOVELTY - Production of catalyst involves preparing transition metal supported carrier by supporting transition metal salt on carrier, and carrying out mechanochemical reduction using metal hydrogen boride or metal chloride.    USE - Production of catalyst used in methanation of carbon dioxide.    ADVANTAGE - The catalyst enables simple and economical methanation of carbon dioxide without using solution or gas phase process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of catalyst.
NOVELTY - The method involves packing (S100) catalyst particle such as zeolite or porosity silica-alumina inside plasma reactor using dielectric barrier discharge catalyst composite apparatus. The carbon dioxide and methane are supplied (S300) to plasma reactor in which inductively coupled plasma is generated (S200). The reaction product such as hydrogen is separated (S500) after completing the process of reacting (S400) with methane and carbon dioxide. The discharge electrode made of copper is formed in one side of plasma reactor.    USE - Methane and carbon dioxide removal method using dielectric barrier discharge catalyst composite apparatus.    ADVANTAGE - The methane and carbon dioxide are removed efficiently by supplying carbon dioxide and methane to plasma reactor in which plasma is generated, and separating reaction product such as hydrogen after reacting with methane and carbon dioxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an air pollution reduction device for dielectric barrier discharge-catalyst complex process.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the methane and carbon dioxide removal process. (Drawing includes non-English language text)    Step for packing catalyst particle inside plasma reactor (S100)    Step for generating inductively coupled plasma (S200)    Step for supplying carbon dioxide and methane (S300)    Step for reacting with methane and carbon dioxide (S400)    Step for separating reaction product (S500)
NOVELTY - The method involves shattering (S100) the measured rate system vinyl envelope to the excavator. The soil burying in the weight combustibles is removed (S500) while the percentage of water content is lowered. The scattering dust and bad small generation among each wind force ratio is reduced. The lower portion of the first and second air conveyer is opened and separated in fixed interval to slope. The first lower portion transfer conveyor is fell down to weight value ream water transfer conveyor.    USE - Method for separating land filled waste or domestic waste for manufacturing solid refuse fuel.    ADVANTAGE - The energy consumption for separating land filled waste or domestic waste for manufacturing solid refuse fuel is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the method for separating land filled waste or domestic waste for manufacturing solid refuse fuel.(Drawing includes non-English language text)    Excavator (1)    Driving drum (303)    Suction wind force pipe (502)    Step for shattering measured rate system vinyl envelope to excavator (S100)    Step for removing soil burying in weight combustibles (S500)
NOVELTY - The hydrogen generator cell has at least one electrolysis cell (104A,104B) having liquid water (304) as aqueous solution base, and reusable sodium amalgam (306) disposed in the liquid water for use as a catalytic converter. An electrical potential is applied across the pair of electrodes (302A,302B) immersed in the liquid water, in which at least one of the pair of electrodes electrolyzes the liquid water for generating hydrogen gas using the catalytic converter.    USE - Hydrogen generator cell used in e.g. communication base station, automobile, portable power source system.    ADVANTAGE - Achieves high yield of the hydrogen gas by using sodium amalgam as a catalytic converter which is reusable, thus, producing high hydrogen concentration with the same electric energy, in place of magnesium sulfate. Extends the length of time during which the electrolysis cells can operate without service by the operator by performing automatic refilling of cells with water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a generation method of hydrogen from cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen fuel cell system.    Electrolysis cell (104A,104B)    Hydrogen fuel cell system (300)    Electrodes (302A,302B)    Liquid water (304)    Sodium amalgam (306)
NOVELTY - Sisal yarn immobilized microbial sewage treatment comprises: (i) washing the sisal yarn and subjecting to high-temperature sterilization process to kill bacteria on yarn; (ii) mixing the flour and water into paste, then soaking the treated yarn into the paste and drying to adhere the flour into the yarn; (iii) soaking the sisal yarn in sewage treatment using different microbial solution, where the micro-organisms attaches to the sisal yarn; and (iv) placing the micro-organisms adhered sisal yarn in sewage for sewage treatment.    USE - Used as sisal yarn immobilized microbial sewage treatment.    ADVANTAGE - The method is simple, economical, convenient and highly efficient.
NOVELTY - Deacidification of biodiesel involves packing a fixed bed with adsorption resin to obtain a fixed bed adsorption separation column. The acid number of biodiesel is obtained by adsorption separation column. The adsorption deacidification is carried out to obtain an acid number of qualified biodiesel.    USE - Method for deacidification of biodiesel (claimed).    ADVANTAGE - The method enables deacidification of biodiesel in eco-friendly and highly efficient manner with low energy consumption.
NOVELTY - Biodiesel deacidification apparatus comprises adsorptive separation column, adsorption column, biodiesel storage tank (11), alcohol distillation column (12), an alcohol storage tank (13), fatty acid storage tank (14). The biodiesel of non-qualified acid number is transferred to pipeline of adsorptive separation column and to pipeline of adsorption column. The biodiesel of qualified acid number is transferred from adsorptive separation column to pipeline of storage tank (3). The biodiesel is transferred from storage tank and fed to the pipeline of adsorptive separation column.    USE - Biodiesel deacidification apparatus.    ADVANTAGE - The biodiesel deacidification apparatus ensures the standard of biodiesel (BD100) according to the national standard because of acid value of less than 0.50 milligram potassium hydroxide per gram.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biodiesel deacidification apparatus.    Pipeline of storage tank (3)    Biodiesel storage tank (11)    Alcohol distillation column (12)    Alcohol storage tank (13)    Fatty acid storage tank (14)
NOVELTY - Biodiesel production involves mixing vegetable oil or fat having 1-4 carbon atoms and monohydric alcohols containing fatty acid triglyceride with an organic base catalyst for esterification. The formed esterified product is separated to obtain 1-4C monohydric alcohol, crude glycerin fatty acid monoester and a catalyst comprising an organic base. The formed fatty acid monoester containing an organic base catalyst is separated, and then mixed with water and 1-20% organic base catalyst at 25-100 degrees C.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method produces biodiesel in a simple and cost-effective manner.    DETAILED DESCRIPTION - Biodiesel production involves mixing vegetable oil or fat having 1-4 carbon atoms and monohydric alcohols containing fatty acid triglyceride with an organic base catalyst for esterification. The formed esterified product is separated to obtain 1-4C monohydric alcohol, crude glycerin fatty acid monoester and a catalyst comprising an organic base. The formed fatty acid monoester containing an organic base catalyst is separated, and then mixed with water and 1-20% organic base catalyst at 25-100 degrees C. The formed mixture is stirred and kept for to give ester phase and glycerol phase, where the ester phase is dried in vacuum to obtain qualified biodiesel product.
NOVELTY - Producing biodiesel oil involves utilizing tung oil and methyl alcohol as raw material and then performing ester exchange reaction in presence of hydrogenation catalyst and ester exchange reaction catalyst at 60-130 degrees C temperature and at 1-6 megapascal pressure.    USE - Method for producing biodiesel oil (claimed).    ADVANTAGE - The method enables to produce biodiesel oil has solved low cetane number, byproducts and impurity problems.
NOVELTY - Biodiesel production involves mixing waste vegetable oil and glycerol in a mass ratio of 100:18-20 in a reactor with an acidic catalyst under vacuum at 110-150 degrees C for 2-3 hours to form fatty acid glycerides and water. The obtained fatty acid glyceride and methanol are mixed in a weight ratio of 100:13-15 under alkaline catalyst vacuum conditions at 70-110 degrees C for 0.5-1 hour to get supernatant liquid fatty acid methyl ester and byproduct glycerol, where methanol and water are collected in vacuum.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method produces biodiesel in a simple manner.    DETAILED DESCRIPTION - Biodiesel production involves mixing waste vegetable oil and glycerol in a mass ratio of 100:18-20 in a reactor with an acidic catalyst under vacuum at 110-150 degrees C for 2-3 hours to form fatty acid glycerides and water. The obtained fatty acid glyceride and methanol are mixed in a weight ratio of 100:13-15 under alkaline catalyst vacuum conditions at 70-110 degrees C for 0.5-1 hour to get supernatant liquid fatty acid methyl ester and byproduct glycerol, where methanol and water are collected in vacuum. The obtained supernatant liquid is placed into distillation column under vacuum conditions at 40-60 degrees C to form fatty acid methyl ester as biodiesel.
NOVELTY - A Polygonum cuspidatum Sieb. et Zucc planting method involves preparing soil by selecting thick layer, loose, fertile soil, deep plowing the soil and leveling. Breeding process is performed by soaking seeds in warm water, diluting carbendazim WP, soaking seeds in diluted carbendazim WP solution, drying, mixing with sand and sowing. Seedlings of Polygonum cuspidatum are transplanted. Field management is performed by dividing the seedlings, weeding, irrigating and fertilizing. Pest control process is performed, followed by harvesting and processing.    USE - Method for planting Polygonum cuspidatum Sieb. et Zucc.    ADVANTAGE - The method enables planting Polygonum cuspidatum Sieb. et Zucc with high seedling efficiency and better breed consistency, and without heavy metal residue, plant diseases and insect pests in an eco-friendly manner.    DETAILED DESCRIPTION - A Polygonum cuspidatum Sieb. et Zucc planting method involves preparing soil by selecting thick layer, loose, fertile soil, deep plowing the soil and leveling. Breeding process is performed by soaking seeds in 30-40 degrees C warm water for 12 hours to dry out, diluting 50% carbendazim WP for 500 times, soaking seeds in diluted carbendazim WP solution for 5 minutes, drying, mixing with sand and sowing. Seedlings of Polygonum cuspidatum are transplanted up to 5-10 cm height. Field management is performed by dividing the seedlings, weeding, irrigating and fertilizing. Pest control process is performed by utilizing medicines or biological control technology terminator for controlling aphids, knotweed, Epicauta and scarabs. Harvesting and processing processes are performed by planting Polygonum cuspidatum during third year excavation, excavation in spring and autumn, and spring excavation of rhizome root section of the tooth point for propagation material backup.
NOVELTY - Preparation of moisturizing facial mask comprises taking rhizoma typhonii, Astragalus membranaceus, pearl barley, Poria, Codonopsis pilosula, Angelica and yam, placing in clean container, adding clean water, heating to 50-90 degrees C for 8-12 hours, separating the slag, taking extraction liquid, cooling to room temperature to obtain traditional Chinese medicine clear liquid, adding Tremella and clean water, stewing for more than 5 hours, adding honey and water, stirring and mixing , soaking the face mask, low temperature sterilizing and packaging.    USE - The method is useful for preparation of moisturizing facial mask (claimed).    ADVANTAGE - The method is simple, safe and environmentally friendly, and has economic and social benefits.    DETAILED DESCRIPTION - Preparation of moisturizing facial mask comprises taking rhizoma typhonii, Astragalus membranaceus, pearl barley, Poria, Codonopsis pilosula, Angelica and yam, placing in clean container, adding clean water, heating to 50-90 degrees C for 8-12 hours, separating the slag, taking extraction liquid, cooling to room temperature to obtain traditional Chinese medicine clear liquid, adding Tremella and clean water, stewing for more than 5 hours, removing when Tremella is not melted completely, adding honey and water, stirring and mixing uniformly to obtain face mask nutrient liquid, soaking the face mask in face mask nutrient liquid, low temperature sterilizing and packaging. The raw material comprises 7-17 pts. wt. rhizoma typhonii, 4-20 pts. wt. Astragalus membranaceus, 2-17 pts. wt. pearl barley, 1-5 pts. wt. Poria, 1-7 pts. wt. Codonopsis pilosula, 2-9 pts. wt. Angelica, 8-21 pts. wt. yam, 6-17 pts. wt. honey, 2-7 pts. wt. Tremella and 200-1100 pts. wt. water.
NOVELTY - A lake nitrogen-rich sewage aquaculture method comprises supplying oxygen to water body, introducing aerobic organisms and water born insects, monitoring dissolved oxygen and biochemical oxygen demand, and putting fish and shrimp.    USE - Lake nitrogen-rich sewage aquaculture method (claimed).
NOVELTY - Preparation of white crystalline alendronate sodium trihydrate powder, involves adding 4-aminobutyric acid, phosphorous acid and ionic liquid to reactor, adding phosphorus trichloride, while heating, cooling, adding deionized water, filtering, reflux-heating filtrate, cooling, adjusting pH and precipitating a solid, filtering, washing filter cake with deionized water and ethanol to obtain crude alendronate sodium, adding crude alendronate sodium to deionized water, heat-refluxing, hot-filtering, precipitating filtrate, filtering, washing cake, and drying.    USE - Preparation of alendronate sodium for drugs.    ADVANTAGE - The method enables simple preparation of alendronate sodium with high purity and yield, under mild reaction conditions, with easy separation and purification. The residual organic solvent content is less. The method uses environmentally-friendly ionic liquid, which serves both as reaction medium and catalyst.    DETAILED DESCRIPTION - Preparation of white crystalline alendronate sodium trihydrate powder, involves adding 4-aminobutyric acid, phosphorous acid and ionic liquid to reactor, adding phosphorus trichloride, while heating to 60-65 degrees C, cooling to 55-65 degrees C, adding deionized water at 20 degrees C, filtering insolubles, reflux-heating filtrate, cooling in ice bath, adding 50 %mass sodium hydroxide solution to adjust pH to 4.3 and precipitate a solid, filtering, washing filter cake with deionized water and twice the volume fraction of 95% ethanol to obtain crude alendronate sodium, adding crude alendronate sodium to deionized water in an amount of 15 g/1 L, heat-refluxing, hot-filtering, precipitating filtrate, filtering, washing cake with deionized water, and drying.
NOVELTY - Ultrasonic wave-assisted preparation of microalgae biodiesel oil is carried out by drying microalgae, crushing, grinding, sieving through 200-300 mesh sieve, adding ionic liquid composition to the sieved microalgae in extraction-reaction kettle, uniformly mixing, then adding methanol, ultrasonically treating at 60-110 degrees C and reacting for 1-5 hours; and cooling reaction liquid to room temperature for 1-1.5 hours, filtering to remove microalgae residue, standing filtered liquid, and decompressing distilling upper layer solution to obtain crude biodiesel oil.    USE - Method for ultrasonic wave-assisted preparation of microalgae biodiesel oil (claimed).    ADVANTAGE - The method is simple to operate and suitable for industrial scale production, can fast prepare biodiesel oil, and has increased production efficiency and reduced production cost.    DETAILED DESCRIPTION - Ultrasonic wave-assisted preparation of microalgae biodiesel oil comprises drying microalgae, crushing, grinding, sieving through 200-300 mesh sieve, adding ionic liquid composition to the sieved microalgae in extraction-reaction kettle, uniformly mixing, then adding methanol, ultrasonically treating at 60-110 degrees C and reacting for 1-5 hours; and cooling reaction liquid to room temperature for 1-1.5 hours, filtering to remove microalgae residue, standing filtered liquid, and decompressing distilling upper layer solution to obtain crude biodiesel oil. The ionic liquid composition comprises 90-98 mass% component A and rest component B. Component A is selected from 1-butyl-3-methylimidazolium chloride ((BMIM)Cl) or 1-allyl-3-methylimidazolium chloride ((AMIM)Cl). Component B is selected from 1-butyl-3-methyl morpholine salt (Hnmm)Im or 1-butyl-3-methylimidazolium hydrogen sulfate ((HMIM)HSO4). Mass ratio of ionic liquid composition to microalgae sieve is 1:10-1:40. Mole ratio of methanol and microalgae is 6:1.
NOVELTY - The marsh gas pool has a charging main pool (1), grooves (2) and float cylinder (3). The float cylinder is loaded with steel, iron, plastic and glass fiber reinforced plastic material. The outer wall of the charging main pool is provided with brick, stone and concrete.    USE - Float cylinder groove marsh gas pool used for biogas production.    ADVANTAGE - The marsh gas pool is featured with simple structure, convenient use and reduced cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of marsh gas pool.    Charging main pool (1)    Groove (2)    Float cylinder (3)    Vent tube (4)
NOVELTY - The iron casting structure anaerobic power generation gas station has a housing portion provided with an anaerobic tank, a purifying tower, an anaerobic tank heating system and a power generation unit. The anaerobic tank for iron casting is provided with a pig iron plate joint portion. A bearing beam support cover plate is connected with the anaerobic tank. A heating source is connected with the anaerobic tank.    USE - Iron casting structure anaerobic power generation gas station.    ADVANTAGE - The biogas production efficiency of the anaerobic power generation gas station is improved. The investment cost of the environmental-friendly anaerobic power generation gas station is reduced. The raw material required for the anaerobic power generation gas station is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the iron casting structure anaerobic power generation gas station.    Feed tube (1)    Insulating layers (2,3)    Outside wall (4)    Marsh gas outlet (8)    Overflow pipe (17)
NOVELTY - The steel film mixing structure has anaerobic tank that is provided with a purifying tower and anaerobic tank heating system. The power generation unit is provided with building material. The sealing door and material discharging pipe valve are closed and feedstock pipe valve is opened when biogas slurry is injected with high pressure pump into tank portion when time of material liquid in tank body portion reaches requirement volume.    USE - Steel film mixing structure for anaerobic power generation gas station.    ADVANTAGE - The biogas production efficiency is improved and the raw material resource is saved. The efficiency of the steel film mixing structure is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the steel film mixing structure.    Feed tube (1)    Ladder (2)    Insulation layer (3)    Gas outlet (10)    Ventilation channel (11)
NOVELTY - The plastic structure has an anaerobic tank, a purifying tower, an anaerobic tank heating system and a power generation unit that is composed of four major components. The anaerobic tank is made of plastic, and the rubber plate is assembled. The bottom end of anaerobic tank is provided with material pipe, distributor and sealing door. The upper portion of anaerobic tank is provided with feedstock pipe.    USE - Plastic structure of anaerobic power generation gas station.    ADVANTAGE - The plastic structure greatly increases the biogas production efficiency, saves investment cost, reduces raw material consumption, increases efficiency and enhanced environmental protection.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of plastic structure of anaerobic power generation gas station.    Insulating layer (3)    Outside wall (4)    Double-wall space (5)    Annular corridor (7)    Marsh gas outlet (8)
NOVELTY - The rubber structure has an anaerobic tank, a purifying tower, an anaerobic tank heating system, and a power generation unit that is composed of four major components. The anaerobic tank is composed of the building material and is casted with resin rubber wire plate. The bottom end of feedstock pipe is connected with anaerobic tank overflow pipe. The top end of anaerobic tank is provided with indoor sealing design power device.    USE - Rubber structure for anaerobic power generation gas station.    ADVANTAGE - The rubber structure is featured with low raw material consumption, increased efficiency, improved environmental protection and high biogas production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of rubber structure of anaerobic power generation gas station.    Insulating layer (3)    Outside wall (4)    Double-wall space (5)    Annular corridor (7)    Marsh gas outlet (8)
NOVELTY - Producing methane using cylindrical pressure extrusion methane slurry convection stirring methane generating system comprises e.g. pouring fermentation raw material into a fermentation system for producing methane by fermentation, collecting using a feedstock tube/discharging pipe side wall and forming a space between adjacent air blocking plates to obtain a fermentation zone, increasing methane gas pressure in the fermentation zone, promoting flow of fermented slurry in a pipeline of feeding tube, a discharging tube and a cloth strain device, and flowing in the discharge tube pipe in one-way.    USE - The method is useful for producing methane using cylindrical pressure extrusion methane slurry convection stirring methane generating system (claimed).    DETAILED DESCRIPTION - Producing methane using cylindrical pressure extrusion methane slurry convection stirring methane generating system comprises pouring fermentation raw material into a fermentation system for producing methane by fermentation, collecting using a feedstock tube/discharging pipe side wall and forming a space between adjacent air blocking plates to obtain a fermentation zone, increasing methane gas pressure in the fermentation zone, promoting flow of fermented slurry in a pipeline of feeding tube, a discharging tube and a cloth strain device, first flowing in the discharge tube pipe in one-way under hydraulic pressure, when the slurry reaches drainage pipe lowest position of the cloth strain device within a storing room, flowing the slurry through pipeline in unidirectional way into each room utilizing hydraulic pressure, using any one of methane fermentation zone, reducing the pressure within the fermentation zone, returning back the slurry into fermentation pipeline through the drainage pipe in one-way direction, completing methane slurry circulation, then using another methane fermentation zone, and circulating the marsh gas using the above mentioned steps.
NOVELTY - The method involves providing fermentation material into space within fermentation region to produce marsh gas. The fermentation region is formed between adjacent air resistance plates (36,38). The flow of fermentation marsh gas in feeding tube (10) and discharge tube (20) is promoted, when pressure of marsh gas fermentation region is increased. The drained marsh gas is flowed into cloth between strain separating units, when marsh gas strain level reaches lowest point of drain device.    USE - Method for producing marsh gas using liquid circulation flow marsh gas generating system.    ADVANTAGE - The marsh gas is produced effectively with uniform material distribution efficiency, high reliability and increased production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the liquid circulation flow marsh gas generating system.    Feeding tube (10)    Discharge tube (20)    Fermenting pipeline (30)    Air resistance plates (36,38)    Water pressure control unit (40)
NOVELTY - Degrading phenol-containing agent involves taking active sludge containing high salt. The obtained sludge is kept on a screening flat plate. The mixture is added with 5-15g yeast extract, 1-10g sodium chloride, 1-15g phenol and 0.1-0.2g feed water. The obtained mixture is sterilized for 20 minutes. The sterilized mixture is added with lysogeny broth. The mixture is cultured for 24-36 hours. The obtained cultured product is added with stabilizer and protective agent.    USE - Method for degrading phenol-containing agent (claimed).    ADVANTAGE - The method enables to degrade phenol-containing agent that has wide applicability.
NOVELTY - The method involves pouring the fermentation material into the fermentation system and gathering the biogas in the fermentation zone formed between the adjacent gas panel blocks. The pressure of the biogas fermentation zone is increased. The fermented biogas is flow within the feed tube (10) and the drain tube (44). The water pressure in the storage room of biogas is increased, and the biogas is flown back through feed tube and drain tube. The biogas slurry is recycled in other biogas fermentation zone.    USE - Method for generating marsh gas for increasing turbulence effect of pipe type fermentation system.    ADVANTAGE - The fermentation system is featured with reduced energy consumption, improved environment protection, increased yield and increased quality of crops and high gas production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fermentation system.    Feed tube (10)    Mounting pipe (30)    First plate (36)    Second plate (38)    Drain tube (44)
NOVELTY - The preprocessing method of corn stover involves adding corn stover and ethylenediamine to a closed reactor, uniformly mixing, heating the mixture at 120-200 degrees C, and reacting.    USE - The method is useful for preprocessing corn stover (claimed).    ADVANTAGE - The method is capable of preprocessing corn stover with high yield, high efficiency and reduced energy consumption, and without using high pressure equipment and equipment requirements in a simple manner.
NOVELTY - A nickel-aluminum catalyst comprises nickel-based ordered mesoporous aluminum oxide catalyst comprising amorphous aluminum oxide and nickel particle dispersed in cylindrical medium channel structure with ordered mesoporous structure of p6mm symmetry, Brunauer, Emmett and Teller surface area average pore diameter of 195-198 m2/g-1 average hole diameter of 5.0-5.5 nm and pore volume of 0.40-0.50 cm3.g-1.    USE - Nickel-aluminum catalyst.    ADVANTAGE - The catalyst has better catalytic activity and stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of nickel-aluminum catalyst comprising taking 2 pts. wt. poly(ethylene oxide)-poly(propylene oxide)-poly(ethylene oxide) block copolymers and 0.25-0.26 pt. wt. nickel(II) nitrate hexahydrate, adding 10 pts. wt. ethanol, stirring, 1.85-1.86 pts. wt. aluminum isopropoxide and 1.5-1.6 pts. wt. 67 wt.% nitric acid aqueous solution, adding 10 pts. wt. ethanol, stirring, adding prepared solution, mixing, drying at 50-60 degrees C for 24-48 hours, oven drying at 20-25 degrees C, raising temperature to 150oC for 2 hours, increasing temperature to 210 degrees C for 4 hours, heating at 320 degrees C for 2 hours, increasing heating temperature to 700 degrees C for 4 hours, and cooling; and    (2) application of nickel-aluminum catalyst comprising taking nickel-aluminum catalyst, putting in reactor, introducing 1:1.2 volume ratio of hydrogen and nitrogen mixed gas, reacting at 600-800 degrees C for 1 hour, regulating reactor internal temperature to 300-500 degrees C at 3000-60000 h-1 mixed gas space velocity of 1:1-4:1 volume ratio of hydrogen and carbon monoxide.
NOVELTY - A kitchen waste recycling protein foaming agent processing method involves adjusting water content in the kitchen waste to 80-90%, adding alkaline agent, heating to complete hydrolysis, cooling after carrying out solid-liquid separation, followed by centrifuging oil and to decant supernatant to obtain mixture of protein membrane concentration, cutting off protein molecules with molecule weight of 5-20 kDa from the protein concentrate i.e. foaming agent.    USE - Method for processing protein foaming agent for classification, processing and recycling kitchen waste (claimed).    ADVANTAGE - The method enables processing and recycling kitchen waste to high value-added products and more fully after use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for classification and processing kitchen waste resources by using protein foaming agent.
NOVELTY - The fixing box is rectangular in shape, and comprises a box main portion (5) and a box cover (1). The box main portion is provided with an inner fixing plate (7). The fixing plate is provided with several samples for ensuring a glass injector to pass through a hole that is in the form of a cylinder. The shape of two cylindrical holes of different diameter that are connected is in the form of an inverted convex. The fixing plates are enabled to be in any number.    USE - Fixing box for atmosphere sampling injector.    ADVANTAGE - The fixing box is made of environment friendly expanded polystyrene (EPS) foam. The fixation effect of glass injector is improved, measurement result is made accurate and life of injector is prolonged, and use is simplified, and manufacture cost is lowered.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fixing box for atmosphere sampling injector.    Box cover (1)    Box main portion (5)    Fixing plate (7)
NOVELTY - Extracting peanut oil and cake involves collecting high quality peanuts as raw material and pressing at high temperature to extract alcohol. Extracted alcohol is filtered and evaporated. Chinese herbal medicine comprising purslane, Houttuynia, fresh reed rhizome, radix scutellariae, Astragalus, licorice and rhizoma acori graminei is soaked, fermented, homogenized, and spray dried. Obtained mixture is soaked and fermented in presence of Aspergillus parasiticus, Aspergillus oryzae, wine yeast and Bacillus to obtain peanut cake.    USE - Method for extracting peanut oil and cake (claimed).    ADVANTAGE - The method enables to extract oil and cake that ensures high solubility, adsorption, utilization and enhanced growth of breeding animals. The method is eco-friendly that effectively controls variety of pests breeding.
NOVELTY - Preparing polyglutamic acid coated superparamagnetic ferric oxide nanoparticles involve dissolving iron salt with water and stirred. Nitrogen is introduced in the mixture, and then polyglutamic acid solution is added with dropwise. Aqueous solution of sodium sulfite is added in the product into a water bath, and then ammonia and water are mixed and stirred for 20-30 minutes. The product is centrifuged at room temperature for 0.5-1.5 hours, and then dialyzed.    USE - Method for preparing polyglutamic acid coated superparamagnetic ferric oxide nanoparticles used for liver tumor models for diagnosis and magnetic resonance imaging (all claimed).    ADVANTAGE - The method is safe, cost-effective and eco-friendly, and easy to operate, for preparing polyglutamic acid coated superparamagnetic ferric oxide nanoparticles that have improved colloid stability, biological compatibility and blood compatibility, and high relaxation rate.
NOVELTY - The generator has second electrode (2) formed of carbon nano material and adhered to surface in outer periphery of electrode material (11), while fixed gap is maintained with first electrode (1). The second electrode is provided for increasing contact area of water and electrode material. The first electrode is formed of carbon nano material, and is adhered to surface in inner periphery of electrode material. The first electrode is provided to increase the contact area of water and electrode material for making hydrogen oxygen mixing gas to electrolyze with water.    USE - Hydrogen-oxygen mixing gas generator of hydrogen-oxygen mixing gas generating system (claimed).    ADVANTAGE - The hydrogen-oxygen mixing gas generator is provided with simple structure bond between two electrode materials adhering to the carbon nano material, so that the supply quantity of the electricity applied to two electrode materials is reduced and producing amount of the hydrogen oxygen mixing gas is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen-oxygen mixing gas generating system.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective views and sectional view of the hydrogen oxygen mixing gas generator.    Electrodes (1,2)    Electrode material (11)    Hole (12)    Cylindrical electrode (21)    Insulator (22)
NOVELTY - Biofuel component composition comprises biologically-derived carbohydrate material separated from a quantity of water by fractional freezing methods.    USE - As biofuel component composition. The system is useful for producing a biofuel (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system comprising a fermentation vessel adapted to contain a biological organism, a first heat removal device in fluid communication with the fermentation vessel, and adapted to reduce a temperature of a substance to solidify at least one component of the substance, and a solid-liquid separation device in fluid communication with the fermentation vessel and/or the first heat removal device, and adapted to separate a solid portion from a liquid portion.
NOVELTY - Method for methane fermentation, involves (a) obtaining organic waste comprising litter and excrement, separating litter form organic waste (first separation process), and crushing litter separated from first separation process, (b) crushing organic waste, introducing crushed material into methane fermentation tank, and fermenting mixture, (c) collecting digested liquid from fermentation tank, separating litter from digested liquid (second separation process), and (d) adding litter obtained from second separation to organic waste to be processed.    USE - The method is useful for methane fermentation (claimed).    ADVANTAGE - The method is simple, and environmentally-friendly, and enables to increase volume of biogas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system, which comprises first litter separation unit, crushing unit, methane fermentation tank, and second litter separation unit.
NOVELTY - The device has hydrostatic maintenance unit (200) that maintains level of purified raw water. A hydrogen generation room is supplied with raw water. An anode plate is arranged in oxygen generating room, and cathode plate is arranged in hydrogen generating room. Fluid pump (400) supplies raw water from hydrogen generation room. An electric decomposition unit (300) performs electrolysis by electric power supply and hydrogen. A filter section (500) filters foreign substance from raw water. A flux detection sensor (700) senses power supplied to electric decomposition unit.    USE - Hydrogen water manufacturing device.    ADVANTAGE - The durability of all sorts of composition unit is improved. The water pressure of feedwater pipe directly does not work within the device. The hydrogen dissolved amount about the hydrogen water is enhanced through dissolution of hydrogen. The generated hydrogen water is rapidly supplied, and the effect of hydrogen water is maximized.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen water manufacturing device.    Hydrostatic maintenance unit (200)    Electric decomposition unit (300)    Fluid pump (400)    Filter section (500)    Flux detection sensor (700)
NOVELTY - An aerosol antiperspirant composition with decreased residue transfer to fabric comprises a propellant and active antiperspirant ingredient comprising at least one hydrophilic silica and triethyl citrate. Triethyl citrate interacts with silica to increase the viscosity of the antiperspirant composition upon volatilization of the propellant.    USE - Aerosol antiperspirant composition with decreased residue (claimed).    ADVANTAGE - The aerosol antiperspirant composition has favorable skin feel, high viscosity, and reduces discomfort and embarrassment caused by perspiration and generation of antiperspirant residue, thus increasing consumer acceptance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of aerosol antiperspirant composition, which involves adding concentrated antiperspirant to a container, separately adding a thickening agent to the container, and mixing the obtained mixture.
NOVELTY - A protein comprising (i) a 260 amino acid sequence (SEQ ID NO: 4) fully defined in the specification, (ii) amino acid sequence exhibiting at least 90% or more sequence identity to an amino acid sequence of SEQ ID NO: 4, where the protein having cutinase activity, or (iii) amino acid sequence of SEQ ID NO: 4 in which one or more amino acids are added, deleted, inserted or substituted, where the protein having cutinase activity, is new.    USE - The protein is useful for decomposing polyester or ester compound (claimed) and preprocessing biomass.    DETAILED DESCRIPTION - A protein comprising (a) (i) a 260 amino acid sequence (SEQ ID NO: 4) fully defined in the specification, (ii) amino acid sequence exhibiting at least 90% or more sequence identity to an amino acid sequence of SEQ ID NO: 4, where the protein having cutinase activity, or (iii) amino acid sequence of SEQ ID NO: 4 in which one or more amino acids are added, deleted, inserted or substituted, where the protein having cutinase activity, or (b) (i) a 304 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, (ii) amino acid sequence exhibiting at least 90% or more sequence identity to an amino acid sequence of SEQ ID NO: 2, where the protein having cutinase activity, or (iii) amino acid sequence of SEQ ID NO: 2 in which one or more amino acids are added, deleted, inserted or substituted, where the protein having cutinase activity, is new. INDEPENDENT CLAIMS are included for the following:    (1) gene encoding the above-mentioned protein;    (2) vector comprising the above-mentioned gene;    (3) transformant comprising the above-mentioned vector; and    (4) method for decomposing polyester or ester compound.
NOVELTY - Harmless treatment of animal feces involves pre-processing marsh gas and filtering faces through biological filter. Animal feces are collected and stirred in water to obtain mixed raw material having water content not less than 85%. Raw material is put in marsh gas pool under anaerobic conditions at temperature more than 20 degrees C. Obtained marsh gas is discharged from marsh gas pool. Marsh gas pool contains marsh gas and slag that are processed to obtain biological fertilizer. The obtained fertilizer is discharged through marsh gas discharge opening, where remaining liquid is flowed through filter.    USE - Method for harmless treatment of animal feces used for eliminating mosquito breeding, and removing more than 70% pathogen, parasite eggs and organic contaminants from wetland (claimed).
NOVELTY - A fermented bamboo shoot shell organic fertilizer is prepared by taking bamboo shoot shell, crushing, adding chicken manure and water, stirring uniformly, sterilizing, adding mushroom culture material, carrying out anaerobic fermentation, adding clinker and plant ash or pulverized coal ash, and mixing.    USE - Method for preparing fermented bamboo shoot shell organic fertilizer (claimed).    ADVANTAGE - The fertilizer is NY525-2012 standard. The method is environment-friendly.
NOVELTY - A sugar filter mud and bagasse organic fertilizer is prepared by taking 90.01-99.9 wt.% sugar filter mud and 0.1-9.99 wt.% bagasse, placing dynamic aerobic fermentation equipment, and composting.    USE - Method for preparing sugar filter mud and bagasse organic fertilizer (claimed).    ADVANTAGE - The method is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for components of dynamic aerobic fermentation equipment comprising closed fermentation chamber, belt conveyor, air inlet, dust and odor removing system, gas tank pulse bag-type dust remover, and UV photo-oxidation device or ozone oxidation device.
NOVELTY - Preparation of livestock manure-based fertilizer comprises adding fermentation liquid and Chinese herbal medicine in livestock manure, fermenting at room temperature for 15-20 days, and naturally drying to water content of 14-16%. The Chinese herbal medicine comprises 90 pts. wt. herba houttuyniae, 90 pts. wt. Eucommia ulmoides, 90 pts. wt. ginseng, 20 pts. wt. Salvia, 20 pts. wt. longan pulp, 50 pts. wt. hawthorn, 20 pts. wt. radix rehmanniae, 20 pts. wt. Angelica, 30 pts. wt. safflower, 30 pts. wt. licorice, and 90 pts. wt. Oldenlandia diffusa.    USE - Method for preparing livestock manure-based fertilizer (claimed).    DETAILED DESCRIPTION - Preparation of livestock manure-based fertilizer comprises adding fermentation liquid and Chinese herbal medicine in livestock manure, fermenting at room temperature for 15-20 days, and naturally drying to water content of 14-16%. The fermentation liquid comprises sodium carbonate, sodium chloride, sodium bicarbonate and potassium permanganate. The Chinese herbal medicine comprises 90 pts. wt. herba houttuyniae, 90 pts. wt. Eucommia ulmoides, 90 pts. wt. ginseng, 20 pts. wt. Salvia, 20 pts. wt. longan pulp, 50 pts. wt. hawthorn, 20 pts. wt. radix rehmanniae, 20 pts. wt. Angelica, 30 pts. wt. safflower, 30 pts. wt. licorice, and 90 pts. wt. Oldenlandia diffusa.
NOVELTY - Preparation of livestock manure-based fertilizer comprises adding fermentation liquid and Chinese herbal medicine in livestock manure, fermenting at room temperature for 15-20 days, and naturally drying to water content of 14-16%. The Chinese herbal medicine comprises 90 pts. wt. radix achyranthis bidentatae, 90 pts. wt. Eucommia ulmoides, 90 pts. wt. Cortex Acanthopanacis, 20 pts. wt. medlar, 20 pts. wt. longan pulp, 50 pts. wt. jujube, 20 pts. wt. radix rehmanniae, 20 pts. wt. Angelica, 30 pts. wt. safflower, 30 pts. wt. licorice, and 90 pts. wt. honeysuckle.    USE - Method for preparing livestock manure-based fertilizer (claimed).    DETAILED DESCRIPTION - Preparation of livestock manure-based fertilizer comprises adding fermentation liquid and Chinese herbal medicine in livestock manure, fermenting at room temperature for 15-20 days, and naturally drying to water content of 14-16%. The fermentation liquid comprises quicklime, straw ash, sodium bicarbonate and potassium permanganate. The Chinese herbal medicine comprises 90 pts. wt. radix achyranthis bidentatae, 90 pts. wt. Eucommia ulmoides, 90 pts. wt. Wu Chia Pi, 20 pts. wt. medlar, 20 pts. wt. longan pulp, 50 pts. wt. jujube, 20 pts. wt. radix rehmanniae, 20 pts. wt. Angelica, 30 pts. wt. safflower, 30 pts. wt. licorice, and 90 pts. wt. honeysuckle.
NOVELTY - Preparation of livestock manure-based fertilizer comprises adding fermentation liquid and Chinese herbal medicine in livestock manure, fermenting at room temperature for 15-20 days, and naturally drying to water content of 14-16%. The Chinese herbal medicine comprises 30 pts. wt. pig bone powder, 30 pts. wt. lily, 30 pts. wt. ginseng, 80 pts. wt. red ginseng, 80 pts. wt. longan pulp, 50 pts. wt. peanut, 80 pts. wt. radix rehmanniae, 80 pts. wt. Angelica, 30 pts. wt. safflower, 30 pts. wt. Cassia seed, and 30 pts. wt. Oldenlandia diffusa.    USE - Method for preparing livestock manure-based fertilizer (claimed).    DETAILED DESCRIPTION - Preparation of livestock manure-based fertilizer comprises adding fermentation liquid and Chinese herbal medicine in livestock manure, fermenting at room temperature for 15-20 days, and naturally drying to water content of 14-16%. The fermentation liquid comprises quicklime, sodium chloride, sodium bicarbonate and potassium permanganate. The Chinese herbal medicine comprises 30 pts. wt. pig bone powder, 30 pts. wt. lily, 30 pts. wt. ginseng, 80 pts. wt. red ginseng, 80 pts. wt. longan pulp, 50 pts. wt. peanut, 80 pts. wt. radix rehmanniae, 80 pts. wt. Angelica, 30 pts. wt. safflower, 30 pts. wt. Cassia seed, and 30 pts. wt. Oldenlandia diffusa.
NOVELTY - Preparation of livestock manure-based fertilizer comprises adding fermentation liquid and Chinese herbal medicine in livestock manure, fermenting at room temperature for 15-20 days, and naturally drying to water content of 14-16%. The Chinese herbal medicine comprises 45 pts. wt. incense ash, 45 pts. wt. tuckahoe, 45 pts. wt. ginseng leaf, 80 pts. wt. radix codonopsitis, 80 pts. wt. longan 400 pts. wt. peanut, 80 pts. wt. prepared rehmannia root, 80 pts. wt. Angelica, 25 pts. wt. safflower, 25 pts. wt. Cassia seed and 45 pts. wt. dandelion.    USE - Method for preparing livestock manure-based fertilizer (claimed).    DETAILED DESCRIPTION - Preparation of livestock manure-based fertilizer comprises adding fermentation liquid and Chinese herbal medicine in livestock manure, fermenting at room temperature for 15-20 days, and naturally drying to water content of 14-16%. The fermentation liquid is straw ash, sodium chloride, sodium bicarbonate or potassium permanganate. The Chinese herbal medicine comprises 45 pts. wt. incense ash, 45 pts. wt. tuckahoe, 45 pts. wt. ginseng leaf, 80 pts. wt. radix codonopsitis, 80 pts. wt. longan 400 pts. wt. peanut, 80 pts. wt. prepared rehmannia root, 80 pts. wt. Angelica, 25 pts. wt. safflower, 25 pts. wt. Cassia seed and 45 pts. wt. dandelion.
NOVELTY - Preparation of 4-(1-piperazinyl)benzo(b)thiophene (I) comprises in an inert solvent under the action of alkaline compound, reacting benzothiophene compound (3) and piperazine compound (4) to obtain (I).    USE - Preparation of 4-(1-piperazinyl)benzo(b)thiophene (I) (claimed).    ADVANTAGE - The method avoids the need of expensive palladium catalyst, thus more safe and environment-friendly.    DETAILED DESCRIPTION - Preparation of 4-(1-piperazinyl)benzo(b)thiophene of formula (I) or its salt comprises in an inert solvent under the action of alkaline compound, reacting benzothiophene compound of formula (3) and piperazine compound of formula (4) or its salt to obtain (I).    R1=H or protecting group; and    X1=leaving group.
NOVELTY - Preparing biodiesel involves crushing microalgae and then sieving through 200-300 mesh sieve to obtain powder. Ion liquid is added into powder and then methanol and lipase catalyst are added to obtain mixture. The mixture is heated on water bath to obtain hydrolyzed liquid. The hydrolyzed liquid is filtered and then distilled under reduced pressure to obtain the product. Ion liquid is selected from 1-butyl-3-methylimidazolium hexafluorophosphate, 1-methoxyethyl-3-methyl imidazolium, 1-ethyl-3-methylimidazolium dicyanamide or 1-butyl-3-methylimidazolium dicyanamide.    USE - Method for preparing biodiesel (claimed).
NOVELTY - Performing saccharification on herbaceous biomass involves crushing herbaceous biomass into particle size less than lcm, followed by addition of 10-30 filter paper cellulase units/ml cellulase and hydrothermal buffer solution to the obtained crushed herbaceous biomass particles. pH of the obtained enzymatic solution is adjusted using boric acid. Saccharification is then performed at 50 degrees C for 24-96 hours under inert atmosphere and 2-4 megapascals to collect hydrolyzate. The obtained hydrolyzate is filtered off to collect sugars.    USE - Method for performing saccharification on herbaceous biomass (claimed).    ADVANTAGE - The inexpensive method enables to perform saccharification on herbaceous biomass in an efficient manner.
NOVELTY - Extraction of lipids involves pre-treating the whole fermentation broth (10) by heating the broth to 90-150 degrees C, preferably 100-150 degrees C, more preferably 110-150 degrees C or 120-150 degrees C, most preferably 130-150 degrees C, and extracting a product from the oleaginous microorganisms. The broth contains oleaginous microorganisms.    USE - Extraction of lipids used for producing biofuel (claimed).    ADVANTAGE - The biofuel formed using the lipid is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for enzyme mixture for degrading microbial cell wall, which consists of amylase, 1-4 mannosidase and 1-3 mannosidase.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of aqueous extraction process using temperature pre-treatment.    Fermentation broth (10)    Base (12)    Vessel (14)    Acid (16)    Water vapor (22)
NOVELTY - Preparation o-aminophenol comprises using o-nitrophenol as raw material and ammonium thiosulfate as reducing agent.    USE - Method for preparing o-aminophenol (claimed).    ADVANTAGE - The method is simple, safe and environment-friendly and has low-cost raw materials.
NOVELTY - A ferrocene derivative (I), is new.    USE - New ferrocene derivative is used in reversible storage of hydrogen peroxide, carbon, methane, nitrous oxide, acetylene and Freon (RTM: refrigerant), and as hemilabile ligand in trnasition metal catalyst (all claimed). Can also be used for asymmetric synthesis, chemical materials, and therapeutic applications.    ADVANTAGE - The new ferrocene derivative can be prepared with high productivity.    DETAILED DESCRIPTION - A ferrocene derivative (I), is new.    R1=bulky group chosen from linear or branched, saturated or unsaturated 1-30C alkyl (preferably 1-10C alkyl and more preferably t-butyl) optionally containing at least one heteroatom chosen from N and O, and gem-dimethyl of formula (i);    R=R1;    R2=nucleophilic group;and    R3=electrophilic group.    INDEPENDENT CLAIMS are included for the following: (i)preparation of ferrocene derivative (I); (ii)ferrocene derivative of formula (Ic); (iii)ferrocene derivative of formula (Id); (iv)preparation of ferrocene derivative (Ic), which involves preparing ferrocene derivative of formula (Ia), preparing ferrocene derivative of formula (Ib) by reacting compound (Ia) with t-butyllithium in pentane in presence of N,N,N',N'-tetramethylethylenediamine, and brominating compound (Ib) in tetrabromoethane; (v)preparation of ferrocene derivative (Id), which involves reacting compound (Ic) with n-butyllithium; and (vi)use of ferrocene derivative (I) in reversible storage of hydrogen peroxide, carbon, methane, nitrous oxide, acetylene and Freon (RTM: refrigerant); and (viii)use of ferrocene derivative (I) as hemilabile ligand in transition metal catalyst including transition metals chosen from nickel, palladium, platinum, rhodium, iridium and ruthenium.
NOVELTY - The new type utility claims a. clean the manganese slag environment-friendly compound fertilizer production system, comprising a a compound fertilizer and compound fertilizer drying cooling exhaust pneuma processing system, a fertilizer production system comprises combustion furnace draught fan, a combustion furnace, weigh a burdening, mixing machine, raw material pulverizer, a granulator, dryer fertilizer, compound fertilizer cooling machine, cold air draught fan, a sieving machine, a coating machine and measuring machine, a compound fertilizer drying cooling exhaust pneuma processing system comprises settling chamber, a washing tower, a sediment and clear water tank. The utility model is new type of compound fertilizer production system using manganese slag as raw material, by adding each a nitrogen, phosphorus and potassium basic fertilizer prepare compound fertilizer product, it not only solves the problem of discharging the waste, and it fully using resource waste is; and the utility new type drying tail pneuma to carry out full processing, which can ensure the environment-friendly clean production.
NOVELTY - Preparation of environment-friendly flower growth promoter comprises dissolving chitosan in citric acid solution, adding hydrogen peroxide solution, stirring to obtain chitosan solution, processing fermented mycelium to obtain nucleic acid, adding alkali solution, stirring for 5-10 hours to obtain nucleotide and deoxynucleotide salt mixture, adding chitosan solution and surfactant and stirring.    USE - Method for preparing environment-friendly flower growth promoter (claimed).    ADVANTAGE - The growth promoter improves yield and quality of flowers, has no residue and has no toxic and side effects.
NOVELTY - Organic fertilizer, has organic matter content of greater than or equal to 40%, moisture content of less than or equal to 30%, total nitrogen (N) content of greater than or equal to 2%, total phosphorus (phosphorus pentoxide) content of greater than or equal to 3%, total potassium (dipotssium oxide) content of greater than or equal to 1.9%, and greater than or equal to 1x 108 functional microbial strains/g.    USE - As organic fertilizer for continuous cropping obstacles of Chrysanthemum (claimed).    ADVANTAGE - The organic fertilizer degrades toxic substances in soil, improves soil granule structure, prevents soil-borne disease, promotes plant growth, and increases plant stress resistance ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer which involves (a) taking livestock and poultry manure, and crop rice straw having 50-60% moisture content, and pH value of 6-7.5 in a ratio of 25-30:1, and fermenting the mixture continuously at 50-65 degrees C for 10-15 days, and (b) adding the functional microbial strains to the fermented mixture.
NOVELTY - Method for preparing sophoridine using microorganism involves preparing sophoridine from Sophora japonica using microorganism, preferably Escherichia coli (CCTCC NO: 2014659).    USE - The method is for preparing sophoridine using microorganism (claimed).    ADVANTAGE - The method enables to prepare product which is cost-effective, and environmentally-friendly, has mild reaction condition.
NOVELTY - This utility new type relates to small ball algae drying device, specifically a novel is a small ball algae mud multi-layer drying device, wherein a lengthways support frame (1), airing plate (2), a protecting cover (3) and the transverse support frame (4), the lengthways supporting bracket (1) has a transverse support frame (4), a lengthways supporting frame (1) lower end of set with wheel (5), a transverse support frame (4) is provided with a guide rail (401), and guide rail (401) by the lug boss and provided with two side (201) of the airing plate (2) activity connection, said lengthways supporting frame (1) between connection has at least one of the transverse supporting frame (4), and each of two transverse supporting frame (4) is set with lengthways mounted between the net (6), the intended effect, the the flies and other insects contact small ball algae mud, which avoids small ball algae mud a bacteria or other germs pollute the problem, make the separating the chlorella after drying mud is clean and sanitary, which is good for the user body health.
NOVELTY - A carbon nitride mesoporous graphite composite modified by graphene or its derivative is prepared by taking graphene or its derivative, adding mesoporous graphite phase carbon nitrogen, surfactant and deionized water, mixing, washing with deionized water, centrifuging, and drying.    USE - Method for preparing carbon nitride mesoporous graphite composite modified by graphene or its derivative (claimed).    ADVANTAGE - The method is simple, low-cost, has high product yield, short reaction course and environment-friendly.
NOVELTY - A fertilizer includes 15-20 pts. wt. urea, 15-20 pts. wt. ammonium sulfate, 20-30 pts. wt. ammonium chloride, 20-30 pts. wt. potassium chloride, 15-20 pts. wt. potassium sulfate, 20-30 pts. wt. monoammonium phosphate, 5-15 pts. wt. superphosphate, 15-20 pts. wt. calcium magnesium phosphate, 5-10 pts. wt. starch, 1-3 pts. wt. microorganism spore, 10-15 pts. wt. feather powder, 15-20 pts. wt. monosodium glutamate, 10-20 pts. wt. starch, and 5-15 pts. wt. sugar.    USE - Fertilizer for wheat (claimed).    DETAILED DESCRIPTION - Fertilizer comprises 15-20 pts. wt. urea, 15-20 pts. wt. ammonium sulfate, 20-30 pts. wt. ammonium chloride, 20-30 pts. wt. potassium chloride, 15-20 pts. wt. potassium sulfate, 20-30 pts. wt. monoammonium phosphate, 5-15 pts. wt. superphosphate, 15-20 pts. wt. calcium magnesium phosphate, 5-10 pts. wt. starch, 1-3 pts. wt. microorganism spore, 10-15 pts. wt. feather powder, 15-20 pts. wt. monosodium glutamate, 10-20 pts. wt. starch, 5-15 pts. wt. sugar, 1-3 pts. wt. tung oil, 2-6 pts. wt. disproportionated rosin, 3-5 pts. wt. lignosulfonate, 3-6 pts. wt. polyvinyl alcohol, 2-5 pts. wt. carboxymethyl cellulose, 15-25 pts. wt. active carbon, 20-30 pts. wt. organic carbon, 3-5 pts. wt. kaolin, 18-23 pts. wt. attapulgite powder, 15-20 pts. wt. weathered coal, 5-15 pts. wt. calcium bentonite, 5-10 pts. wt. activated clay, and 20-25 pts. wt. zeolite powder.
NOVELTY - Microbial organic fertilizer comprises 50-58 pts. wt. duck manure, 50-58 pts. wt. chicken manure, 32-38 pts. wt. bagasse, 18-20 pts. wt. fructus forsythiae residue, 12-15 pts. wt. rice bran, 31-35 pts. wt. water, 21-25 pts. wt. illite powder, 10-12 pts. wt. ammonium humate, 3-4 pts. wt. brassin, 1. 2-1.5 pts. wt. Bacillus subtilis, 0.4-0.5 pts. wt. Penicillium pinophilum, 1.5-1.8 pts. wt. Alcaligenes faecalis, 1.2-1.5 pts. wt. Bacillus circulans, 0.8-1 white Geotrichum candidum and 0.5-0.7 pts. wt. Bacillus thuringiensis.    USE - Microbial organic fertilizer.    ADVANTAGE - The microbial organic fertilizer increases soil activity, prevents soil plate structure, promotes cucumber yield and prevents Fusarium oxysporum infection in cucumber.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing microbial organic fertilizer, which involves:    (A) mixing bagasse, fructus forsythiae residue, rice bran and water;    (B) reacting obtained mixture with Bacillus subtilis and Penicillium pinophilum at 48-55 degrees C for 18-22 days;    (C) mixing duck manure, chicken manure, illite powder, Alcaligenes faecalis, Bacillus circulans, Geotrichum candidum, Bacillus thuringiensis at 30-32 degrees C for 20-25 days;    (D) reacting ammonium humate and brassin in obtained mixture at 48-55 degrees C for 3-5 days;    (E) mixing obtained mixtures; and    (F) granulating obtained mixture to obtain product.
NOVELTY - An organic/inorganic compound fertilizer comprises 10-15 pts. wt. lignite, 10-15 pts. wt. vermiculite, 10-15 pts. wt. filter mud, 10-15 pts. wt. pig manure, 2-3 pts. wt. potassium carbonate, 1-2 pts. wt. yeast concentrate-containing organic wastewater, 3-5 pts. wt. monoammonium phosphate, 3-5 pts. wt. potassium sulfate, 3-5 pts. wt. potassium chloride, 2-4 pts. wt. conditioning agent, 3-5 pts. wt. urea, 2-3 pts. wt. chitosan, 18-22 pts. wt. water, 1-3 pts. wt. glutathione, 2-5 pts. wt. composite fungus and 0.5-1.5 pt. wt. anti-propellant agent.    USE - Organic/inorganic compound fertilizer (claimed).    ADVANTAGE - The organic/inorganic compound fertilizer has improved soil structure, soil fertilizer-keeping property and nutrients property.    DETAILED DESCRIPTION - An organic/inorganic compound fertilizer comprises 10-15 pts. wt. lignite, 10-15 pts. wt. vermiculite, 10-15 pts. wt. filter mud, 10-15 pts. wt. pig manure, 2-3 pts. wt. potassium carbonate, 1-2 pts. wt. yeast concentrate-containing organic wastewater, 3-5 pts. wt. monoammonium phosphate, 3-5 pts. wt. potassium sulfate, 3-5 pts. wt. potassium chloride, 2-4 pts. wt. conditioning agent, 3-5 pts. wt. urea, 2-3 pts. wt. chitosan, 18-22 pts. wt. water, 1-3 pts. wt. glutathione, 2-5 pts. wt. composite fungus and 0.5-1.5 pt. wt. anti-propellant agent. The conditioning agent contains 5-10 pts. wt. attapulgite, 5-10 pts. wt. bentonite, 2-5 pts. wt. silicon, 2-5 pts. wt. sepiolite, 1-3 pts. wt. ammonium chloride, 1-3 pts. wt. ammonium sulfate and 2-5 pts. wt. peat. The composite fungus consists of 0.2-0.4 pt. wt. Escherichia coli, 0.6-0.8 pts. wt. Jelly-like Bacillus and 0.2-0.35 pt. wt. Pseudomonas fluorescens. The anti-propellant agent is dimethicone. An INDEPENDENT CLAIM is included for preparation of organic/inorganic compound fertilizer.
NOVELTY - Preparation of bio-methane involves boosting biogas, introducing boosted biogas into an absorption tower from lower portion of absorption tower until pressure in tower reaches 0.3-20 MPa, then continuously introducing biogas, spraying absorbent in tower by using spray nozzle on upper portion of absorption tower, and making biogas and adsorbent contact with each other to remove carbon dioxide in the biogas.    USE - Preparation of bio-methane by purifying biogas (claimed).    ADVANTAGE - The method efficiently and economically provides bio-methane with purity of 95% and regeneration efficiency of more than 95%.    DETAILED DESCRIPTION - Preparation of bio-methane involves boosting biogas, introducing boosted biogas into an absorption tower from lower portion of absorption tower until pressure in tower reaches 0.3-20 MPa, then continuously introducing biogas, spraying absorbent in tower by using spray nozzle on upper portion of absorption tower, and making biogas and adsorbent contact with each other to remove carbon dioxide in the biogas. The pressure in the absorption tower is 0.3-20 MPa. The flow ratio of the absorbent to the biogas is 8-100 kg/h to 1 Nm3/hour. The absorbent is an aqueous solution comprises choline eutectic solvent and/or imidazole ionic liquid as an active ingredient. The content of active ingredient is 5-90 %mass. An INDEPENDENT CLAIM is included for system for preparing bio-methane.
NOVELTY - Kitchen garbage processing system comprises pre-processing sub-system comprising storage device (4), spiral conveying device (30), primary sorting device (21), pre-crushing device, automatic crushing sorting device (28), homogenizing pre-heating device, dehydrating device (42) for separating waste into liquid and dry waste suitable for fermentation and a three phase separating device (49) which receives the liquid waste and separates it into water, oil and residues.    USE - Kitchen garbage processing system.    ADVANTAGE - The kitchen garbage processing system ensures low cost kitchen garbage processing in less time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for processing kitchen garbage using kitchen garbage processing system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of kitchen garbage processing system.    Storage device (4)    Primary sorting device (21)    Automatic crushing sorting device (28)    Spiral conveying device (30)    Dehydrating device (42)    Three phase separating device (49)
NOVELTY - Preparation of tolvaptan (III) involves amidating 7-chloro-2,3,4,5-tetrahydro-1H-1-benzazepin-5-ol (I) and 2-methyl-4-((2-methylbenzene)amido)benzoyl chloride (II).    USE - Preparation of tolvaptan (claimed).    ADVANTAGE - The method enables efficient preparation of tolvaptan with high yield and reduced emissions, by simple process.    DETAILED DESCRIPTION - Preparation of tolvaptan of formula (III) involves amidating 7-chloro-2,3,4,5-tetrahydro-1H-1-benzazepin-5-ol of formula (I) and 2-methyl-4-((2-methylbenzene)amido)benzoyl chloride of formula (II).
NOVELTY - The method involves reacting 2,6-di-tert-butylphenol, paraformaldehyde and reaction solvent in presence of catalyst, heating, adding water, cooling and then crystallizing, washing crystals with aqueous methanol and then drying to obtain intermediate including 3,5-di-t-butyl-4-hydroxybenzyl ether, adding isocyanuric acid and dimethylformamide to intermediate and then reacting, heating to obtain crude product, washing crude product, cooling, crystallizing, centrifuging, washing with methanol, crystallizing, and drying to obtain hindered phenolic antioxidant.    USE - The method is useful for preparing hindered phenolic antioxidant (claimed).    ADVANTAGE - The method is capable of preparing hindered phenolic antioxidant with improved purity of 99% and yield, and reduced waste discharge in a safe, economical and energy-efficient manner.    DETAILED DESCRIPTION - The method involves reacting 1.5-2.5% 2,6-di-tert-butylphenol, paraformaldehyde and reaction solvent in the presence of a catalyst under nitrogen atmosphere, heating for 5-8 hours to reflux the mixture, adding water to the mixture, cooling and then crystallizing, washing the crystals with aqueous methanol and then drying to obtain intermediate including 0.5-2.5% 3,5-di-t-butyl-4-hydroxybenzyl ether, adding isocyanuric acid and dimethylformamide reaction solvent to the intermediate and then reacting in the presence of a catalyst, heating the mixture at 120-140 degrees C for 4-5 hours, constantly removing negative byproduct of methanol to obtain crude product, washing the crude product and then filtering, cooling, crystallizing, centrifuging the obtained product, washing with methanol and then crystallizing, and drying to obtain hindered phenolic antioxidant.
NOVELTY - Removal of harmful gas in boiler flue gas comprises preparing chemicals; preparing biological agent, desulfurizing and denitrating; and preparing fertilizer.    USE - Method for removing harmful gas in boiler flue gas (claimed).    ADVANTAGE - The method is simple, effectively removes nitrogen oxide, and utilizes waste material to prepare fertilizer.
NOVELTY - The present invention is to provide a method of cyclic manufacturing of biodiesel, which includes: (a) performing an esterification reaction through using glycerol and free fatty acids under a high-temperature and low-pressure environment to obtain a glyceride mixture; (b) mixing the glyceride mixture with a lower alcohol and alkali catalyst for a transesterification reaction, and after the reaction, obtaining a biodiesel solution and a glycerin solution via a phase separation; (c) using an acidic solution to neutralize the glycerin solution and then produce a salt precipitate; (d) filtering the glycerin solution in step (c) to remove the salt precipitate; (e) heating the glycerin solution in step (d) to remove the lower alcohol and water, and obtain a purified glycerol. The present invention directly performs an esterification reaction without adding acidic catalyst, and recycles the glycerol product for a cyclic manufacturing of biodiesel in order to reduce production costs of biodiesel.
NOVELTY - The method involves constructing anaerobic and/or anoxic and aerobic tank adjacent to the wall of sewage treatment system. An exchange film is arranged on common wall of aerobic tank arranged close to anaerobic tank or oxygen-tank at one side of electrode as anode. The cathode and anode of microorganism fuel battery are connected to outside resistor through lead. The sewage water is entered into aerobic tank for processing, when the water is collected from anaerobic or anoxic tank.    USE - Method for treating sewage sludge in coupling microorganism fuel battery.    ADVANTAGE - The time required for sewage treatment process is reduced. The cost of the sewage treatment device is reduced. The product of sludge is reduced to 20-60 %.
NOVELTY - The reactor has pool main portion which is formed with first-stage anaerobic area, micro-aeration nitrification area and second stage anaerobic area. The first-stage anaerobic area is comprised with three reaction rooms. The micro-aeration nitrification area and second stage anaerobic area are respectively comprised with two reaction rooms. The reaction rooms of micro-aeration nitrification area are provided with micro-pore aeration pipe (9). A relux tube is set between reaction rooms of nitrification area and first stage anaerobic area.    USE - Short-range nitration and de-nitrification integrated ABR reactor used in sewage processing field.    ADVANTAGE - The problem related to loss of sludge is solved effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ABR reactor.    Biogas collection pipe (8)    Micro-pore aeration pipe (9)    Vent pipe (10)    Water outlet pipe (14)    Filler (17)
NOVELTY - The marsh gas fermentation system has a feedstock tube (11) and a discharging tube (12) which are connected through a vertical U-type fermentation pipeline (20). The feedstock tube and the discharging tube are formed with the drain holes respectively. One end side of the discharging tube is connected with a bacterial pipeline, and another end side is connected with a fixed water pipe. The biogas liquid is transferred into the feedstock tube with the operation of one-way valve.    USE - Marsh gas fermentation system.    ADVANTAGE - The efficient marsh gas fermentation process is promoted. The production rate of the marsh gas fermentation system is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the marsh gas fermentation system.    Feedstock tube (11)    Discharging tube (12)    Fermentation pipeline (20)    Vent (32)    Gas collecting pipe (40)
NOVELTY - A composting system includes a holding area (14) for compostable material. The holding area has a base (20) with permeable portion(s). Chamber(s) (22) is located below the holding area. The chamber has an inlet (32) for directing oxygen-containing fluid into the chamber, and an outlet for directing material outwardly from the chamber. The outlet opening is disposed lower in the chamber relative to the inlet opening.    USE - Composting system for treating organic material or biomass.    ADVANTAGE - The composting system facilitates efficient composting process stage(s) or phase(s) under conditions that assist optimization of composting process, and facilitates immediate removal or extraction of mature or usable portions of compost, following completion of respective composting process phases.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for aeration of compostable material by supplying oxygen-containing gas or air into compostable material at pressure above ambient air pressure.    DESCRIPTION OF DRAWING(S) - The drawing is a cross-sectional view of composting system.    Aeration bed (12)    Holding area (14)    Permeable base (20)    Chamber (22)    Inlet (32)
NOVELTY - The method involves pumping a first fluid with a first pump. A second pump is operated with the first fluid being pumped, and arranged within a replaceable cartridge (110). A flow of a reactant liquid is urged from the replaceable cartridge to a reaction area (130) in response to operation of the second pump. The hydrogen is generated in response to the flow of the reactant liquid entering the reaction area. The second pump is operated from within a liquid reservoir (120) configured to store the reactant liquid.    USE - Method for generating hydrogen for fuel cell system.    ADVANTAGE - The hydrogen generator system is provided to minimize the liquid and to minimize the number of valves and connections through which the liquid is flowed. The generator system is provided to minimize the number of connections through which the liquid can leak externally. The fluid is not harmful or corrosive and contains no ingredients that can solidify when the liquid dries is pumped by the external pump in order to avoid leakage of potentially harmful or corrosive liquids and prevent clogging of lines and valves.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen generator system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generator system.    Replaceable cartridge (110)    Liquid reservoir (120)    Reaction area (130)    Optional byproduct containment area (140)    Internal pump (150)
NOVELTY - The new type utility claims have a a pig farm waste water recycling processing system, comprising orderly connected a urine flushing unit, a processing unit and Anaerobic pool, provided with air outlet on upper part of the Anaerobic pool, the air outlet pipeline and a purification device connected, a purification device and marsh gas storage bag connection, provided with a liquid outlet in lower part of the Anaerobic pool, a liquid outlet through pipeline and a connected oxidation pond, the pond and a connection pool, filtering pool and the sterilizing pool connected, outlet and urine flushing unit and a sterilizing a connection. The utility model is new type sewage through filtering using a filter and sterilizing pool after sterilizing farm wash unit as the wash water, save have a water, a purification process for marsh gas and a marsh gas and removing vulcanization hydrogen, ammonia equal toxic and malodorous gas, increase have quality of marsh gas to prevent the vulcanization hydrogen, ammonia gas for surrounding human and animal and cause a dangerous.
NOVELTY - Purification of neutral human milk oligosaccharides (HMOs) in batch or continuous manner from fermentation broth comprising neutral HMO (of purity less than 80%), biomass, medium components and contaminants, obtained by microbial fermentation comprises (a) separating biomass from the broth, (b) cationic ion exchanger treatment for removing positively charged material, (c) anionic ion exchanger treatment for removing negatively charged material and (d) electrodialysis step for removing charged materials, where a purified solution contains neutral HMO has a purity of greater than or equal to 80%.    USE - The method is useful for purifying neutral human milk oligosaccharides, which is used in prophylaxis or therapy of a gastrointestinal disorder and as an additive in food, preferably as additive in human baby food (all claimed). No biological data given.    ADVANTAGE - The method: is simple; and provides neutral human milk oligosaccharides with greater than 75% yield and/or the purified solution is free of DNA, proteins, and/or recombinant genetic material (claimed).
NOVELTY - Refining biomass comprises a primary refining process including a treatment resulting in a size reduction of biomass material, and a secondary refining process including at least one conversion treatment resulting in at least one refined product. The primary refining process comprises a separation treatment for extracting fractions of different components from the biomass material, and at least one of the fractions of different components is irradiated for structural modification of the component of the fraction.    USE - The method is useful for refining biomass, preferably lignocellulosic biomass (all claimed).    ADVANTAGE - The method: allows for a simple and reliable process flow; reduces the need of additives such as enzymes; consumes less energy; is suitable for different kind of end products; and is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for biorefinery facility for refining biomass, comprising a primary unit for a primary refining treatment of a biomass and a secondary unit for a secondary refining treatment of the pre-treated biomass, where the primary unit comprises a separation unit for separating fractions of different components of biomass material, and at least one of the different component fractions is provided to an irradiation unit for irradiation of the component of the fraction.
NOVELTY - The utility model is new type relates to a methane production with a raw material processing device, specifically is a methane production with a chicken manure processing device, a sterilizing tank (1), a box (13), wherein the fermentation tank (13), the upper part set with sterilizing tank (1), and the lower part set with heating layer (10), a pedestal (11), the fermentation tank (13), its one end set with feeding port (9) and another end set with discharging mouth (12), and a discharging mouth (12) is set with sealing cover, the sterilizing tank (1), the upper part set with electric control box (2), one side equipped with enter port (3), the disinfecting tank (1), the internal set with ultraviolet sterilizing lamp (4), a conveying belt (5), a guide groove (7), the utility model is new type structure is simple, using suitable, use safe reliability, that have a raw material gas a process wastes time and labour, use rate of a problem.
NOVELTY - The utility model is new type belongs to biogas purifying to prepare vehicle fuel gas technology field, specifically is a gas film separating and purifying a carbon dioxide sum a heat pump system. The utility model is new type comprises water containing marsh gas compressing device, film separating a purification device, a heat pump a sum, center control device, through the marsh gas after pre-processing enter into water containing marsh gas compressing device, the marsh gas after compression by cooler after cooling, after entering into carbon dioxide sum a heat pump a cooling water enter into filter, then through a carbon dioxide sum a heat pump device and a water heating to fit temperature, enter into film separation device. The utility model is new type use have sum source carbon dioxide heat pump and a cold heat energy, the marsh gas cooling after heat pump evaporator and a cold energy for compression, a. comprising water, increase the product gas dew point. A heat pump of heat with a two way to film group by heating. The utility model is a novel a high cost, strong practicability, the utility model is new type fit in relative technology field and application.
NOVELTY - The utility model is new type relates to a water electrolysis hydrogen and a electrolysis unit, water electrolysis hydrogen belongs to technology field. The water electrolysis hydrogen the electrolysis unit comprises a rubber frame and set up a diaphragm pressure ring press have a membrane layer on a plate and a frame two side, in a rubber frame provided with an annular lug boss, the annular lug boss to two side provided with the network side, between the network side and a plate set with support network, a frame is also set with multiple outer edge. The electrolytic unit light weight, anti-" cavitation, simple structure and a single frame electrolytic unit.
NOVELTY - The method involves molding (S700) multi cell separator (70) in which conducting material (61) is injected in bridge hole (121). Mask film (60) and conducting material are coated (S600) on fluid path (13) of multi cell separator portion (10). Bridge hole is molded (S500) in insulation line (14). Exposure and phenomenon is performed (S400) in mask film (30) and insulation line (14) is molded in top/bottom of separator portion. Mask film is welded (S300) to top/bottom of light-sensitive dry film (20), and light-sensitive dry film is compressed (S200) in top/bottom of separator portion.    USE - Method for manufacturing fuel cell multi-cell bipolar plate.    ADVANTAGE - High voltage stack is lightened.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell stack.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the manufacturing process of multi cell separator.    Multi cell separator portion (10)    Fluid path (13)    Insulation line (14)    Light-sensitive dry film (20)    Mask films (30,60)    Conducting material (61)    Multi cell separator (70)    Step for compressing light-sensitive dry film in top and bottom of multi cell separator portion (S200)    Step for welding mask film to top and bottom of light-sensitive dry film (S300)    Step for performing exposure and phenomenon in mask film (S400)    Step for molding bridge hole in insulation line (S500)    Step for coating mask film and conducting material on fluid path of multi cell separator portion (S600)    Step for molding multi cell separator in which conducting material is injected in bridge hole (S700)
NOVELTY - Manufacture of sawdust complexing agent involves preparing sawdust, pulverizing mastic, adding 5-80% obtained powder to sawdust, shaping using hot hydraulic press, and mixing the resultant product with frankincense resin powder.    USE - Manufacture of sawdust complexing agent (claimed).
NOVELTY - The apparatus (100) has a sheet transfer unit that is provided for cyclically driving a belt element (112), such that the vacuum suction force is given to the top surface in which a first seat is raised. A robot arm (120b) is provided for operating a gripper (120a), so that the corner of predetermined target and corner of first seat and second sheet are recognized as image in a top surface of belt element. An align unit is provided to control the operation of robot arm and gripper, in order to laminate the first seat different from the second sheet in predetermined position.    USE - Apparatus for manufacturing laminate of fuel cell.    ADVANTAGE - Since the operation process for successively laminating the first and second sheet is performed during transferring process of sheet in lamination stage phase, the work productivity is improved. The position error and the product failure caused by the lamination position fault are prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the apparatus for manufacturing laminate of fuel cell.    Apparatus for manufacturing laminate of fuel cell (100)    Belt element (112)    Main frame (114)    Gripper (120a)    Robot arm (120b)
NOVELTY - The apparatus (100) has a sine wave generator (150) to generate a sine wave signal of the specific frequency, where a voltage calculation unit (120) produces a voltage of a fuel cell stack (110) using a stack voltage, which is applied from the fuel cell stack. A current calculating unit (140) is provided for producing the current of the fuel cell stack using the stack current, which flows toward a sinusoidal wave. A power transistor (160) is provided for amplifying the sine wave signal, and controls the current of the fuel cell stack of the sinusoidal wave.    USE - Apparatus for monitoring the fuel cell stack status.    ADVANTAGE - The sine wave generator is provided to generate a sine wave signal of the specific frequency, where a voltage calculation unit produces a voltage of a fuel cell stack using a stack voltage, and hence ensures obtaining the specific frequency signal without attenuation by controlling the value of the stack current in an effective manner and reduces the influence and the correlation of the noise in a reliable manner, and also produces the exact impedance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for monitoring the fuel cell stack status.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell stack status monitoring apparatus. (Drawing includes non-English language text).    Fuel cell stack status monitoring apparatus (100)    Fuel cell stack (110)    Voltage calculation unit (120)    Current sensor (130)    Current calculating unit (140)    Sine wave generator (150)    Power transistor (160)
NOVELTY - Recovery of organic compounds from wastewater for use in electricity generation in a microbial fuel cell, involves: (i) converting organic compounds from wastewater into a biomass; (ii) recovering the biomass from the wastewater; (iii) followed by substantially dissolving or breaking down the biomass to form a cell lysate; (iv) fermenting the cell lysate to form volatile fatty acids (VFA) in a broth; and (v) separating the VFA in the VFA broth to produce a clarified VFA stream.    USE - The method and VFA are useful for recovering organic compounds from wastewater for use in electricity generation in a microbial fuel cell (claimed).    ADVANTAGE - The method can effectively recover organic compounds such as volatile fatty acids from wastewater in high concentration and in a cost-efficient manner. Also, the method overcomes numerous technical issues in converting the biomass into volatile fatty acids, that is, as a readily biodegradable substrate, before the substrate is presented to the MFC.
NOVELTY - Process for preparation of amorphous form of dapagliflozin, involves (a) dissolving dapagliflozin in a solvent chosen from methanol, dichloromethane, acetonitrile, acetone, methyl isobutyl ketone, methyl ethyl ketone, 2-methyl tetrahydrofuran or their mixtures, (b) removing solvent from the solution obtained in step (a), and (c) isolating the amorphous form of dapagliflozin.    USE - The process is useful for preparation of amorphous form of dapagliflozin which is used in solid pharmaceutical formulation for treating type 2 diabetes (all claimed).    ADVANTAGE - The process is environmentally-friendly, stable, and cost-effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) amorphous solid dispersion of dapagliflozin together with one or more carriers; and    (2) process for preparation of amorphous solid dispersion of dapagliflozin together with one or more carriers, involves (a) dissolving dapagliflozin and carriers in a solvent, (b) removing solvent from the solution obtained in step (a), and (c) isolating the amorphous solid dispersion of dapagliflozin together with one or more carrier.
NOVELTY - A sex attractant pheromone is synthesized by producing aldehyde compound by oxidation reaction of alcohol compound producing halogenated alkoxy compound or alkylation reaction which produces alkenyloxy compound or reacting halogenated alkoxy compound with alkynyl compound and producing pheromone by reduction reaction and hydrolysis reaction on alkenyloxy compound.    USE - Synthesis of sex attractant pheromone for pest management.    ADVANTAGE - Method is efficient and environmentally friendly.    DETAILED DESCRIPTION - A sex attractant pheromone of formula R3-R7-R1-Y' (7) is synthesized by producing aldehyde compound of formula O=CH-(CH2)m-1X (2) by oxidation reaction of alcohol compound of formula HO-(CH2)m-X (1) producing halogenated alkoxy compound of formula CH(W)2-(CH2)m-1-X (3) or alkylation reaction which produces alkenyloxy compound of formula R3-R6-(CH2)m-1-CH(W)2 (6) or reacting compound (3) with alkynyl compound of formula R3-R5-R10-M (8b) and producing pheromone (7) by reduction reaction and hydrolysis reaction on compound (6).    X=halo;    Y'=(=O);    R1=(-CH2-)m;    R3=CH3-(CH2)n-;    R5=(-CC-)p;    R6=(-C=C-)q;    R7=-C=C-C=C-;    W=-O-R3;    R10=-CC;    M=metal, Na, Li, K or Mg;    m=5, 6, 7, 8, 9, 10, 11 or 12;    n=1, 2 or 3; and    p,q=1 or 2.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the synthetic scheme of sex attractant pheromone.
NOVELTY - The device has a heat exchange unit connected between a tar component and a gas dust-removing part. The heat exchange unit and the dust-removing part are connected with a fuel gas outlet and a fuel gas inlet. A cooling gas passes through an outer box body and an inner box body. The heat exchange unit is mounted with the tar component through the fuel gas outlet. The gas dust-removing part is formed with a cylindrical cavity body. The heat exchange unit is fixed with a water tank. A side wall of the fuel gas inlet is mounted on the cylindrical cavity body.    USE - Biomass fuel gas integrated processing device.    ADVANTAGE - The device has less volume, better biomass fuel gas processing ability, less biomass fuel gas processing time, and can improve processing efficiency so as to supply biomass fuel gas under qualified condition corresponding to required subsequent process and save occupied space of a square meter, so that tar water production and water treatment cost are reduced in an effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a front-sectional view of a biomass fuel gas integrated processing device.
NOVELTY - Feeding rabbit by: selecting mountain fog area, constructing indoor house, heating, dehumidifying, keeping room temperature at 15-35 degrees C, relative humidity at 50-70%, summer flow speed at 0.3-0.5 m/second and winter flow speed at 0.1-0.3 m/second; cultivating 10-15 times per month for 2-4 hours at area and grassland coverage at more than 70%, stocking density at 50-80/ mu ; feeding breast milk and feed; ad# taking and cleaning excrement, dry-wet separating to obtain dry and liquid materials, burning dry material, smoke dust purification treating, and anaerobic fermenting liquid material.    USE - Method for feeding rabbit (claimed).    ADVANTAGE - The method combines scientific cultivation and ecological cultivation, prevents generating of common disease, reduces death rate, and has economic benefit and ecological benefit.    DETAILED DESCRIPTION - Feeding rabbit by:    (A) selecting mountain fog area at altitude of 400-1200 m, annual average temperature of 14-18 degrees C, annual average rainfall of 1000-1800 mm and annual average relative humidity of 70-85%;    (B) constructing indoor house for 3-6 rabbit, heating, dehumidifying, keeping room temperature at 15-35 degrees C, relative humidity at 50-70%, summer flow speed at 0.3-0.5 m/second and winter flow speed at 0.1-0.3 m/second;    (C) cultivating 10-15 times per month for 2-4 hours at area and grassland coverage at more than 70%, stocking density at 50-80/ mu ;    (D) feeding breast milk and feed; and    (E) taking and cleaning excrement, dry-wet separating to obtain dry and liquid materials, burning dry material, smoke dust purification treating, and anaerobic fermenting liquid material.
NOVELTY - The new type utility claims a plant fibre reinforced plastic biomass pool, goal is a provide a seal performance is good, stable air pressure of glass steel marsh gas pool. A glass steel is made by sealing and the pool body, the pool body lower part provided with a feedstock and a discharge, the a body part provided with a sum guide pipe and air pipe, air inlet end of the gas-guide pipe provided with valve, an air outlet end of the air guide sub-pipe connected with collecting bottle. Along with the production of a body internal marsh gas, sum of a body internal pressure rise gradually, not using a sum of the following condition, gradually rise the sum voltage exceed a set value of pressure relief valve, relief valve open, inner gas from gas-guide pipe enter into bottle, a body internal sum pressure when reduce to set value, a relief valve is closed, the gas supply to a gas-guide tube following on from the steady pressure, to make the combustion efficiency of stove with stable.
NOVELTY - The utility model is new type provide a a portable dry germ ion analyzer, the analyzer comprises shell, upper shell setting display screen, a switch and a a a a a a housing inner panel, setting a module plate and control plate, a main control board and a switch plate module, display screen and switch electric connected with the module plate and a warm control electric connection, detecting a low setting drop-like a wall and dropping liquid a; a is set in a warm and electric connected with the control receiving a; a moving connection with a disposable piece, reagent paper, a disposable piece comprises a a a a a a a a a a further insert in a a, reagent paper and drop a toward a a sample. Directly taking blood sample drop on a reagent paper, which avoids the dilution caused by the measurement error, accuracy rate is high; a structure is simple, without need to maintenance, reduce the daily maintenance cost, a centrifugal pump and a pipeline to a container, which reduces the volume and analyzer, increase the portability and environmental protection.
NOVELTY - An integrated mobile toilet sewage purification and resource recovery device comprises mobile toilet (1), anaerobic tank (2), trickling filters (3), capacitor (4), stent (5), anaerobic bottom, overflow hole, orifices, activated carbon particulate fillers, empty tube, vent, drain, volcanic filler, anode, and cathode.    USE - Integrated mobile toilet sewage purification and resource recovery device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of integrated mobile toilet sewage purification and resource recovery device.    Mobile toilet (1)    Anaerobic tank (2)    Trickling filters (3)    Capacitor (4)    Stent (5)
NOVELTY - Promoting uniform bacteria strain in one-way flow biogas fermentation device comprises entering feedstock by feedstock pipe (11) into U-type pipe, fermenting, accumulating generated biogas into inner space of feeding pipe blocking plate and discharge pipe blocking plate, gathering biogas by gas collecting pipe (40), extruding bacteria strain in feedstock pipe, one-way flowing to discharge pipe water drainage hole (20) into lowest position of biogas liquid level, reducing pressure drop of methane fermentation pipeline, circulating slurry and repeating steps.    USE - Method for promoting uniform bacteria strain in one-way flow biogas fermentation device (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of promoting uniform bacteria strain in one-way flow biogas fermentation device.    Feedstock pipe (11)    Discharge pipe water drainage hole (20)    Hydraulic water pressure (30)    Vent (32)    Gas collecting pipe (40)
NOVELTY - Production of biogas by one-way flow lifting liquid turbulent flow fermentation device comprises entering feedstock by feedstock pipe into U-type pipe, fermenting, accumulating generated biogas into inner space of feeding pipe blocking plate and discharge pipe blocking plate, extruding bacteria strain in feedstock pipe, flowing to discharge pipe water drainage hole into lowest position of biogas liquid level, collecting biogas, one-way flow refluxing, reducing pressure drop of fermentation pipeline, circulating slurry and repeating steps.    USE - Method for producing biogas by one-way flow lifting liquid turbulent flow fermentation device (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of production of biogas by one-way flow lifting liquid turbulent flow fermentation device.    Feedstock pipe (11)    Discharge pipe water drainage hole (20)    Hydraulic water pressure (30)    Vent (32)    Gas collecting pipe (40)
NOVELTY - Preparation of organic fertilizer involves mixing 30-45 pts. wt. cow dung having moisture content of 20-50% with 60-70 pts. wt. corn straw, adding 10-15 pts. wt. beef bone, 10-15 pts. wt. filter mud and 2-5 pts. wt. tea, mixing, adding fungicide and metal deactivator, leaving still, adding fermentation agent and inoculant, mixing, adding resultant mixture to fermentation unit, fermenting for 15-20 days, performing secondary fermentation, adjusting water content of resultant material, pulverizing and sieving.    USE - Preparation of organic fertilizer is used for cultivating Eucalyptus.    ADVANTAGE - The method enables preparation of organic fertilizer having high nutrient content and reduced moisture content, with suppressed odor generation.    DETAILED DESCRIPTION - Preparation of organic fertilizer involves mixing 30-45 pts. wt. cow dung having moisture content of 20-50% with 60-70 pts. wt. corn straw, adding 10-15 pts. wt. beef bone, 10-15 pts. wt. filter mud and 2-5 pts. wt. tea, mixing, adding fungicide and metal deactivator, leaving still for 1-24 hours, adding fermentation agent and inoculant, mixing, adjusting moisture content of resultant material to 50-60%, adding resultant mixture to fermentation unit, fermenting for 15-20 days, performing secondary fermentation for 5-9 days, adjusting water content of resultant material to 20-30%, pulverizing and sieving.
NOVELTY - A molasses fermentation liquid water-soluble fertilizer comprises 20-30 %mass molasses fermentation liquid, 15-20 %mass amino acid powder, 5-10 %mass urea, 10-15 %mass monoammonium phosphate, 15-20 %mass potassium sulfate, 2-5 %mass calcium nitrate, 1-3 %mass trace elements, and 20-25 %mass water.    USE - Molasses fermentation liquid water-soluble fertilizer (claimed).    ADVANTAGE - The molasses fermentation liquid water-soluble fertilizer has excellent solubility with respect to water, improves the efficiency of soil and crops, crop quality, promotes growth of crops, and increases crop yield, and is rich in nutrients.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of molasses fermentation liquid water-soluble fertilizer, which involves adding raw materials and stirring uniformly.
NOVELTY - A flower garden fertilizer comprises fermented animal bone liquid, animal bone meal, vegetable dry powder, glucose, potassium permanganate solution, hydrogen peroxide, and mixture of potassium sulfate and ammonium hydroxide.    USE - Fertilizer is used for flower garden.    ADVANTAGE - The flower garden fertilizer has durability for 6 months, improves soil activity, enhances resistance of flowers, promotes nutrition, and can be economically prepared by simple, safe and environmentally-friendly process.
NOVELTY - Herb is crushed and sieved, and reflux-pretreated with ethanol, to obtain raw material. Enzyme is added to raw material, mixed with water mixture, and enzymolyzed for predetermined time. The obtained mixture is heated to reflux, extracted, cooled to room temperature and filtrated under reduced pressure, to obtain extract containing polysaccharide. The extracted solution is concentrated, and chitosan solution is added, stirred, flocculated, purified and centrifuged, to obtain purified polysaccharide solution. The polysaccharide solution is dried, to obtain herb-derived polysaccharide.    USE - Enzymatic extraction and purification of herb-derived polysaccharide used as flocculant and food additive.    ADVANTAGE - The method economically and environmentally-friendly provides herb-derived polysaccharide with high purity and extraction efficiency.
NOVELTY - Biomass refining device comprises biomass screening machine (1), first feeding machine (2), cutting machine (3), second feeding machine (4), grinding machine (5), high concentration pulping machine, slurry pump, water purification system, high concentration cleaner, preheater, two high pressure slurry pumps, supercritical water liquefaction reactor, cooler, subcritical water liquefaction reactor, distillation device, heavy organic matter storage tank, light organic matter storage tank, multi-carbon sugar storage tank, industrial ethanol storage tank, and operation control center.    USE - Biomass refining device (claimed).    ADVANTAGE - The device is suitable for industrial production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biomass refining device.    Biomass screening machine (1)    First feeding machine (2)    Cutting machine (3)    Second feeding machine (4)    Grinding machine (5)
NOVELTY - The system has a gasification furnace (1) fixed with a fuel gas boiler (3) that is arranged with a cold plate (64). A water tank is connected with a water circulation device (6). The gasification furnace and fuel gas boiler are fixed with an electric heat decoking unit (2). An outer part of the furnace is provided with a water jacket (12). A top part of the furnace is connected with the water pump (63). An air room (11) is fixed with the gas boiler that is formed with an inlet and an outlet. An air pipe (13) is fixed with the gas boiler. A heat recovery device is provided with a tail part (7).    USE - Biomass gasification furnace and fuel gas industrial boiler unit heat supply system.    ADVANTAGE - The system has high stability and high quality, and increases biomass fuel gas heating efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification furnace and fuel gas industrial boiler unit heat supply system.    Gasification furnace (1)    Electric heat decoking unit (2)    Fuel gas boiler (3)    Water circulation device (6)    Tail part (7)    Air room (11)    Water jacket (12)    Air pipe (13)    Water pump (63)    Cold plate (64)
NOVELTY - The device has feedstock tube (10), discharging tube (20), and straight pipe (30) whose two side top portions are provided with opening and detachably connected with biogas liquid surface of feedstock tube and discharge tube. Drain pipe (51) is provided between feedstock tube and discharging tube. Baffle is provided between side walls of feedstock tube and discharge pipe. A cell or space is formed between adjacent blocking plates formed between side walls of feedstock tube and feeding/discharging tube. A portion of cell is connected with gas-guide pipe that is set with valve.    USE - Methane generating device.    ADVANTAGE - The biogas slurry circulation flow stirring performance is improved using biogas liquid flow which is stirred to promote uniform distribution of strain and promote the fermentation raw material and thus the gas production is increased efficiently. The side wall of feedstock tube and the side wall of the discharge tube are replaced with the existing plate, so that the construction difficulty or difficulty of process is reduced. The methane generating device is disassembled suitably for industrial production.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of the methane generating device.    Feedstock tube (10)    Discharging tube (20)    Straight pipe (30)    Drain pipe (51)
NOVELTY - Producing methane by straight-type hydraulic pressure ultra-efficient methane fermentation system comprises pouring the fermentation raw material into a fermentation system to produce biogas by providing a space as fermentation area between the collection feed tube/discharge tube side wall and adjacent air resistance plate, passing the biogas into biogas feedstock flow tube, a discharge tube, a cloth device tube and into hydraulic pressure chamber in a unidirectional flow, decreasing the pressure of fermentation area using one biogas area, refluxing the biogas in fermentation pipeline.    USE - The method is useful for producing methane by straight-type hydraulic pressure ultra-efficient methane fermentation system (claimed).    DETAILED DESCRIPTION - Producing methane by straight-type hydraulic pressure ultra-efficient methane fermentation system comprises pouring the fermentation raw material into a fermentation system to produce biogas by providing a space as fermentation area between the collection feed tube/discharge tube side wall and adjacent air resistance plate, passing the biogas into biogas feedstock flow tube, a discharge tube, a cloth device tube and into hydraulic pressure chamber in a unidirectional flow, decreasing the pressure of fermentation area using one biogas area, refluxing the biogas in fermentation pipeline within the hydraulic pressure chamber through feedstock flow tube, discharge tube and cloth device tube, completing the biogas slurry circulation, repeating the step in other fermentation area.
NOVELTY - The system has fermentation feeding pipe (10) that is connected with gas discharge pipe (20) through fermentation pipeline (30). The fermentation pipeline is provided with gas feed pipe stopper plate (32) and gas discharge pipe stopper plate (34). The gas discharge pipe is arranged between air resistance plates (36,38). A space between adjacent air resistance plates is formed of fermentation region whose top portion is communicated with separate airway. A cloth fabric device is provided with several strains holes and center conduit pipe that is installed in fermentation pipeline.    USE - Linear marsh gas fermentation system for promoting uniform strain distribution to produce marsh gas.    ADVANTAGE - The linear marsh gas fermentation system is provided with improved stirring performance to promote uniform distribution of strain, improved fermentation efficiency and increased gas production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the linear marsh gas fermentation system. (Drawing includes non-English language text)    Fermentation feeding pipe (10)    Gas discharge pipe (20)    Fermentation pipeline (30)    Gas feed pipe stopper plate (32)    Gas discharge pipe stopper plate (34)    Air resistance plates (36,38)
NOVELTY - Hydraulic anaerobic stirring tank comprises a tank body, whose upper part is set with a supernatant liquid outlet pipe, while lower part is set with an anaerobic liquid inlet pipe. The bottom part of tank body is set with a sludge discharging device. The sludge discharging device and outside wall of tank body are surrounded with at least two water power stirring devices. The end part of water power stirring device is set with a stirring and pumping unit. The inner side of tank body is connected to a sludge pump by a stirring pipe. The sludge pump is connected to a rotational flow generator.    USE - Used as a hydraulic anaerobic stirring tank.    ADVANTAGE - The stirring tank facilitates anaerobic decomposition of organic matter which is completely adhered to the surface of anaerobic area, and thus it improves the efficiency of anaerobic process, where the reaction does not affect the state of acidification of the reaction zone, and facilitates the acidification reaction to proceed further; has simple structure; is easy to maintain; and improves the efficiency of gas output of anaerobic tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the hydraulic anaerobic stirring tank.
NOVELTY - Amphikrikos marinus (CGMCC NO: 9814) is new.    USE - The strain is used for producing biodiesel oil, feed or edible oil and studying the evolution of model organisms (all claimed).    ADVANTAGE - The strain has high oil content and growth rate and reduces the production cost of biodiesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for culturing Amphikrikos marinus.
NOVELTY - Complex microbial inoculums comprises 30-80% probiotic and 20-70% nutritional additive. comprising Bacillus subtilis, green nonsulfur bacteria, yeast, Lactobacillus acidophilus, Pseudomonas and Streptomyces.    USE - The complex microbial inoculum useful for manure fermentation (claimed).    ADVANTAGE - The microbial inoculum: is rich in Bacillus, actinomycete and more beneficial microorganisms, which can grow at different temperature areas; enables to reach logarithmic growth phase in a short time; and removes bad smell of the manure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparation of the complex microbial inoculum, comprising (a) mixing the components of the probiotics as mentioned above, mixing same amount of corn powder and rice hull powder, and diluting, uniformly mixing to obtain mixture I, (b) mixing the components of the nutritional additive except corn flour and rice hull powder, (d) mixing with the diluted corn powder and rice hull, mixing uniformly to obtain mixture II, and (e) mixing the mixtures I and II along with the remaining components of the additive.
NOVELTY - Microbial fertilizer comprises Bacillus flexus, Pseudomonas sp. and Azotobacter chroococcum in a ratio of 2.5-4x 109 colony-forming unit (CFU):1.2-3.5x 109 CFU:2-4x 109 CFU.    USE - The microbial fertilizer is useful for cultivating leafy vegetable (claimed), and promoting growth of the crop.    ADVANTAGE - The microbial fertilizer increases disease resistant ability in crop, and improves soil structure.
NOVELTY - Bacillus licheniformis UTM102 strain with the preservation number CGMCC No. 9508, is new.    USE - The strain: is useful for producing phytase, beta -endoglucanase, cellobiase and xylanase; composting and fermenting solid organic waste, preferably waste sludge, municipal solid waste, crop residue, animal carcasses and/or poultry manure; preparing organic fertilizer; and promoting plant growth (all claimed).    ADVANTAGE - The strain restrains plant pathogen, increases yield of crops, and has economic benefits.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for (1) preparing Bacillus licheniformis UTM102 strain-containing compost inoculating agent, comprising (i) inoculating activated Bacillus licheniformis UTM102 strain into glucose and peptone containing liquid culture medium and fermenting to obtain fermented liquid, and (ii) processing the fermented liquid to obtain liquid agent or dehydrating and drying to obtain powder; and (2) use method of the Bacillus licheniformis UTM102 strain in composting and fermenting solid organic waste, comprising (i) inoculating 0.1-0.5% Bacillus licheniformis UTM102 strain into organic solid waste, mixing uniformly, aerobic composting and fermenting, (ii) adjusting moisture content of the material to 45-65% using a conditioning agent, adjusting carbon to nitrogen ratio to 10-60:1, stacking and maintaining oxygen content to 8-15%, and (iii) stacking and fermenting for 12-20 days, terminating fermentation and land filling, incinerating or sieving the remaining material to obtain biological fertilizer.
NOVELTY - Method for fermenting molasses, involves (a) preparing fermentation medium containing sulfate, (b) inoculating activated marine microorganism in the test tube comprising the above-mentioned medium, incubating the culture, preparing seed culture, inoculating inoculum in seeding tank, incubating the culture, inoculating seed culture in fermentation tank and fermenting the culture, and (d) centrifuging the fermented culture, adding water to obtained precipitate, centrifuging the mixture, collecting supernatant and crude liquid, and purifying the crude liquid.    USE - The method is useful for fermenting molasses which is useful for biosynthesizing ectoine hydroxylase (claimed).    ADVANTAGE - The method is cost-effective.    DETAILED DESCRIPTION - Method for fermenting molasses, involves (a) preparing fermentation medium comprising molasses, soybean powder and sulfate, (b) inoculating activated marine microorganism in the test tube comprising the above-mentioned medium, incubating the culture for 18-26 hours, preparing seed culture, inoculating 3-5% inoculum in seeding tank, incubating the culture for 24 hours, inoculating 5-10% seed culture in fermentation tank and fermenting the culture for 36 hours, and (d) centrifuging the fermented culture, adding 20 times water to obtained precipitate, centrifuging the mixture for 2-10 minutes, collecting supernatant and crude liquid, and separating and purifying the crude liquid.
NOVELTY - Method for promoting marsh gas production, involves adding mannosyl glycerate in initial and middle stages of fermentation.    USE - The method is useful for promoting marsh gas production (claimed).    ADVANTAGE - The method increases yield of marsh gas, and is environmentally-friendly.
NOVELTY - The stove has a stove main body (1) fixed with a water tank (2), which is formed with a water inlet (12) and a water outlet (4). A fuel gas gatherer (3) is formed with a gas guide hole (13). A sum flow stopping cover (6) is formed with a heat preservation layer (7). A furnace core (16) is fixed with an ash chamber (21), which is fixed with a fan (20). A movable bolt (19) is fixed with a top end of another ash chamber (22), which is formed with a water seal groove (14) and the heat preservation layer. A gas pipe (18) is connected with an upstream gas flow-rate adjusting valve (17).    USE - Lignocellulose biomass anti-tar gasification stove.    ADVANTAGE - The stove is easy to block, and has high utilization rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a lignocellulose biomass anti-tar gasification stove. '(Drawing includes non-English language text)'    Stove main body (1)    Water tank (2)    Fuel gas gatherer (3)    Water outlet (4)    Sum flow stopping cover (6)    Heat preservation layer (7)    Water inlet (12)    Gas guide hole (13)    Water seal groove (14)    Furnace core (16)    Upstream gas flow rate adjusting valve (17)    Gas pipe (18)    Movable bolt (19)    Fan (20)    Ash chambers (21, 22)
NOVELTY - The recovery device has a pressurizing unit (2) fixed in left side of machine frame (1) and connected with reaction kettle (3). The transport pipe (4) is connected to upper end center of kettle. The transport pipe is welded with kettle. The decompression tank (5) is located at center of top portion of frame. The tank is connected with transport pipe. The waste liquid pool (6) is provided under tank. The waste liquid pool is welded with tank. The flare tower (7) is fixed in right side of machine frame top portion. The flare tower is connected with machine frame by screw thread.    USE - Flare gas recovery device used in chemical industry.    ADVANTAGE - The structure of flare gas recovery device is simplified. The device is featured with several functions. The methane gas is reused. The waste amount is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the flare gas recovery device.    Machine frame (1)    Pressurizing unit (2)    Reaction kettle (3)    Transport pipe (4)    Decompression tank (5)    Waste liquid pool (6)    Flare tower (7)
NOVELTY - A washing agent comprises 30-70 %mass isoparaffin, 10-30 %mass paraffin-type mineral oil and/or naphthene-type mineral oil, 5.5-8 %mass water, 1-10 %mass nonionic surfactant chosen from polyoxyethylene alkyl ether, sorbitan ester and fatty-acid methyl ester, 1-5 %mass dialkyl succinate sulfonate, 0.01-1 %mass monoester with 8-14C fatty acid, glycerol or polyglycerol, and/or ether of 7-9C alcohol and glycerol, and 0.01-3 %mass metal deactivator chosen from benzotriazole, benzothiadiazole and their amine neutralized material.    USE - Agent is used for washing blanket cylinder of offset printer.    ADVANTAGE - The washing agent does not clog piping in the printer, does not contain chlorinated solvent, is safe with respect to human body, and has reduced odors and excellent washability of blanket cylinder.    DETAILED DESCRIPTION - A washing agent comprises 30-70 %mass isoparaffin having dynamic viscosity at 40 degrees C of 1-3 mm2/second and boiling point of 150-260 degrees C, 10-30 %mass paraffin-type mineral oil and/or naphthene-type mineral oil having flash point of 70-100 degrees C and dynamic viscosity at 40 degrees C of 1-3 mm2/second, 5.5-8 %mass water, 1-10 %mass nonionic surfactant chosen from polyoxyethylene alkyl ether, sorbitan ester and fatty-acid methyl ester, 1-5 %mass dialkyl succinate sulfonate, 0.01-1 %mass monoester with 8-14C fatty acid, glycerol or polyglycerol, and/or ether of 7-9C alcohol and glycerol, and 0.01-3 %mass metal deactivator chosen from benzotriazole, benzothiadiazole and their amine neutralized material.
NOVELTY - Extracting litchi seeds involve pulping 50-100 pts. wt. litchi seed at liquid nitrogen temperature (-30 to -10 degrees C) to obtain litchi seed slurry. Litchi seed slurry is mixed uniformly with 20-40 pts. wt. 1-hexyl-3-methylimidazolium hexafluorophosphate by using a liquid-liquid extraction device to obtain extraction liquid. The extraction liquid is condensed by using microwave with power supply of 100-500 Watts, and then heated at 100-170 degrees C for 30-50 minutes to extract flavonoids. The extract is dried by using anhydrous sodium sulfate, and then refrigerated at 0-5 degrees C and sealed.    USE - Method for extracting litchi seeds (claimed).    ADVANTAGE - The method is eco-friendly, and enables to extract flavone from litchi seeds has wide industrial applicability.
NOVELTY - An anaerobic electrochemical membrane bioreactor comprises an anode electrode in the vessel suitable for supporting electrochemically active microorganisms that oxidizes organic compounds in the waste water; and a cathode membrane electrode in the vessel suitable for catalyzing the hydrogen evolution reaction to generate hydrogen and supporting hydrogenotrophic methanogens that anaerobically generates an energy containing gas.    USE - The anaerobic electrochemical membrane bioreactor is used for treating wastewater; and recovering energy from an anaerobic electrochemical membrane bioreactor (all claimed).    ADVANTAGE - The system can effectively and efficiently cultivate high cell numbers of microorganisms in a short period of time without the need for strictly anaerobic and sterile conditions would be of significant commercial interest for CO2 capture. The process for wastewater treatment is used to recover energy from low strength wastewaters in the form of biogas; treat wastewater; and reclaim water.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method of treating wastewater by introducing the wastewater through the inlet of the electrochemical membrane bioreactor above; passing the wastewater through the membrane electrode while retaining the electrochemically active microorganisms and the hydrogenotrophic methanogens in the vessel; and removing the treated solution through from the outlet; and    (2) a method of recovering energy from an anaerobic electrochemical membrane bioreactor by collecting biogas generated at the surface of the cathode membrane electrode.
NOVELTY - The injection current production apparatus (100) has a first DC-DC converter (120) which converts the direct current of the voltage into the direct current of the specific voltage. A second DC-DC converter (130) converts the direct current of the voltage generated in the high voltage portion due to the regenerative braking into the direct current of the specific voltage. A control unit (140) controls the operation of first and second DC-DC converter according to the power state of the high voltage portion.    USE - Injection current production apparatus for fuel cell stacks.    ADVANTAGE - The voltage is boosted corresponding to the battery for vehicle. Thus the fuel cell stacks is driven steadily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an injection current production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the injection current production apparatus. (Drawing includes non-English language text)    Injection current production apparatus (100)    Fuel cell stack (110)    First DC-DC converter (120)    Second DC-DC converter (130)    Control unit (140)
NOVELTY - The apparatus (200) comprises a control unit (210) for adding the phase current to a motor (270). An inverter (250) is provided for converting the power source generated from a fuel cell (220). An electrical field cooling system (260) is provided for cooling the inverter at on start-up stopped state sensing the temperature of the inverter. A temperature sensor (251) is provided for sensing the temperature of the inverter. The temperature sensor is negative temperature coefficient temperature sensor. A cluster (290) is provided for indicating the cooling failure by the error code.    USE - Apparatus for checking cooling fails of fuel cell.    ADVANTAGE - The apparatus comprises a control unit for adding the phase current to a motor, and thus enables reducing the cost generated in the diagnosis or disposition. The service cost down is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for checking cooling fails of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a cooling fails checking apparatus. (Drawing includes non-English language text).    Cooling fails checking apparatus (200)    Control unit (210)    Fuel cell (220)    Inverter (250)    Temperature sensor (251)    Electrical field cooling system (260)    Motor (270)    Cluster (290)
NOVELTY - The apparatus has a housing wall that is joined with polar plates for forming an electrolytic chamber containing an electrolytic solution. The housing wall has a hydrogen conduit arranged at a suitable position for collecting hydrogen generated during the electrolysis, and guiding hydrogen to an outside container through a hydrogen outlet. An oxygen conduit is arranged at a suitable position for collecting oxygen generated during the electrolysis, and guiding oxygen to an outside container through an oxygen outlet.    USE - Electrolytic apparatus for producing hydrogen and oxygen elements from water.
NOVELTY - Preparing a microbial organic fertilizer from agriculture waste and by-products using useful microorganism strains, involves (a) classifying agricultural waste and by-products for separating treatable organic waste substance, (b) composting and decomposing organic waste for obtaining organic humus using microorganism composition comprising a mixture of Bacillus and Streptomyces, and (c) producing a microbial organic fertilizer from the organic humus.    USE - The method is useful for preparing microbial organic fertilizer from agriculture waste and by-products using useful microorganism strains (claimed).    DETAILED DESCRIPTION - Producing a microbial organic fertilizer from agriculture waste and by-products using useful microorganism strains, involves (a) classifying agricultural waste and by-products for separating treatable organic waste substance, (b) composting and decomposing organic waste for obtaining organic humus using microorganism composition comprising a mixture of Bacillus and Streptomyces, and (c) producing a microbial organic fertilizer from the organic humus by blending it with a useful microorganism composition comprising mixture of free nitrogen fixing bacterial strain Azotobacter strain TN2, where the nitrogen fixing bacterial strain is symbiotic and generates a growth stimulator chosen from rhizobium DX2 and rhizobium DX6, and at least an insoluble phosphate bacterial strain chosen from B.pumilus PL1, B.pumilus PL2 and B.pumilus PL3, and macronutrients nitrogen (urea), phosphorus (phosphorus pentoxide) and potassium (potassium peroxide) at a suitable weight ratio.
NOVELTY - Manufacture of methane involves performing methanation reaction (S101), shift reaction (S102) and methanation reaction (S103) using catalyst comprising gas containing carbon dioxide and hydrogen.    USE - Manufacture of methane (claimed).    ADVANTAGE - The method provides methane with high yield and high purity by removing toxic carbon monoxide gas, by efficient process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) apparatus for manufacturing methane, which consists of heat exchanger, methanation reaction device (A), shift reaction device, and methanation reaction device (B); and    (2) gasification system, which consists of gasification unit containing gasifier, and methane production apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the method of manufacturing methane. (Drawing includes non-English language text)    Methanation reactions (S101,S103)    Shift reaction (S102)
NOVELTY - High purity protein preparation involves taking, pulverizing and crushing wild nettle into 20-40 mesh, and then degreasing with petroleum ether. The raw degreased material is placed into pressure extraction tank with alkaline as extraction solvent in a high-pressure pump to form an extract. The formed extract is centrifuged and then added with acidic aqueous solution with stirring for 30-60 minutes to form solid-liquid separation.    USE - Method for preparing high purity protein from wild nettle (claimed).    ADVANTAGE - The method prepares high purity protein at low or normal temperature with high extraction efficiency and high purity, and reduces extraction time and energy consumption in a simple and eco-friendly manner.    DETAILED DESCRIPTION - High purity protein preparation involves taking, pulverizing and crushing wild nettle into 20-40 mesh, and then degreasing with petroleum ether. The raw degreased material is placed into pressure extraction tank with alkaline as extraction solvent in a high-pressure pump to form an extract. The formed extract is centrifuged and then added with acidic aqueous solution with stirring for 30-60 minutes to form solid-liquid separation. The resulting solid-liquid separation is heated at 30-40 degrees C, and then washed, lyophilized, and freeze-dried at -50 to -30 degrees C for 6-8 hours to give a nettle protein powder.
NOVELTY - A nilotinib hydrochloride (I) having moisture content of 5-7 wt.%, is new.    USE - New nilotinib hydrochloride is useful in pharmaceutical composition (claimed), and as antitumor agent.    ADVANTAGE - The nilotinib hydrochloride is prepared with high yield and high purity, by efficient, economical and environmentally-friendly process.    DETAILED DESCRIPTION - A nilotinib hydrochloride of formula (I) having moisture content of 5-7 wt.%, is new. An INDEPENDENT CLAIM is included for pharmaceutical composition, which comprises nilotinib hydrochloride (I), diluent or carrier.
NOVELTY - An isolated yeast, preferably Saccharomyces cerevisiae (CNCM 1-4791, CNCM 1-4790 or CNCM 1-4792), is new.    USE - The isolated yeast is used for producing first generation ethanol (all claimed).    ADVANTAGE - The isolated yeast rapidly enables to produce ethanol compared to standard yeast.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for process for producing first generation ethanol, which involves fermenting biomass using yeast.
NOVELTY - Biological preparation is prepared by culturing Thiobacillus denitrificans, Bacillus cereus, Acinetobacter baumannii, Rhodococcus rhodochrous, and Pseudomonas fluorescens at concentration of 1x 108 cells/ml, mixing cultured bacteria in a volume ratio of 3:2:2:1:1, mixing mixture with carrier in a weight ratio of 1:2, stirring mixture at 100 revolution/minutes for 3 minutes, and drying stirred mixture at 20-22 degrees C, until moisture content reaches 6-8%.    USE - The biological preparation is useful for treating sewage wastewater in thermal power plant (claimed).    ADVANTAGE - The biological preparation reduces operation cost.
NOVELTY - Microbial agent is obtained by preparing adsorbent, microorganism carbon source, microbial support, and microorganisms.    USE - The microbial agent is useful for repairing sewage (all claimed).
NOVELTY - A fungicide-containing encapsulated plant tissue culture explants on clothes coating method involves immersing sterilized explants in clothing agent, where the agent comprises sodium alginate, fungicide, nutrient component, plant hormone, mucus-permeable clothing agent and ventilating agent, and the agent is basic, colorless and transparent, removing calcium chloride solution and inoculating the explants into culture medium.    USE - Method for coating fungicide-containing encapsulated plant tissue culture explants on clothes.    ADVANTAGE - The method enables coating fungicide-containing encapsulated plant tissue culture explants on clothes in simple and economic manner, with convenient popularization, prolonging bactericide effect for long duration of time, reducing pollution rate and killing bacteria on surface.
NOVELTY - A high dissolution medicine comprises active component nepicastat, water-soluble solid dispersion carrier, disintegrant, lubricant and additive.    USE - High dissolution medicine.    ADVANTAGE - The method is energy efficient. The medicine has 95% dissolution rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of high dissolution medicine comprising taking raw materials, preparing soft material, pelleting, drying, finishing, mixing, and tableting or capsulating.
NOVELTY - A circular particle potassium fertilizer is prepared by taking powdered potassium fertilizer, stirring, adding 2-3 wt.% atomized water, stirring, flaking, extruding, sieving, polishing, roughening, injecting 1-3 wt.% low viscosity adhesive aqueous solution, drying, and screening.    USE - Method for preparing circular particle potassium fertilizer (claimed).    ADVANTAGE - The fertilizer has good fluidity. The method is simple, environment-friendly and energy-efficient.
NOVELTY - Microbial technology treatment of kitchen garbage comprises taking kitchen garbage, draining, adjusting water content to 80%, adding rice husk and 0.1-0.5 wt.% liquid microorganism, mixing at 60 degrees C until water content of 45-65%, stirring at 20 revolutions/minute for 10 minutes, pausing for 10 minutes, and repeating for 4 hours.    USE - Microbial technology treatment of kitchen garbage used for preparing organic fertilizer (claimed).    ADVANTAGE - The fertilizer is NY515-2012 standard. The method is environment-friendly.
NOVELTY - A livestock manure-based fertilizer is prepared by taking fermentation broth comprising straw ash, lime, sodium bicarbonate and potassium permanganate, and Chinese herbal medicine comprising incense, tuckahoe, banana leaf, radix codonopsis, semen ziziphi spinosae, peanut shell, radix rehmanniae preparata, Angelica, green tea, Cassia seed and wormwood, adding livestock manure, fermenting at room temperature, and drying.    USE - Method for preparing livestock manure-based fertilizer (claimed).    DETAILED DESCRIPTION - A livestock manure-based fertilizer is prepared by taking fermentation broth comprising 70:10:1:0.1 mass ratio of straw ash, lime, sodium bicarbonate and potassium permanganate, and Chinese herbal medicine comprising 28 pts. wt. incense, 28 pts. wt. tuckahoe, 28 pts. wt. banana leaf, 65 pts. wt. radix codonopsis, 65 pts. wt. semen ziziphi spinosae, 10 pts. wt. peanut shell, 65 pts. wt. radix rehmanniae preparata, 65 pts. wt. Angelica, 25 pts. wt. green tea, 25 pts. wt. Cassia seed and 28 pts. wt. wormwood, adding livestock manure, fermenting at room temperature for 15-20 days, and drying until water content is 14-16%.
NOVELTY - A kitchen waste organic fertilizer is prepared by taking kitchen garbage, draining, adding detergent, stirring, emulsifying, adding rice husk, mixing, adding Bacillus culture medium at pH value of 7.5, fermenting at 60 degrees C for 48 hours, adding water, regulating water content, stirring at 60 degrees C, reacting for 12 hours, adding water, stirring, reacting for 24 hours, adding water, stirring, and reacting for 48 hours.    USE - Method for preparing kitchen waste organic fertilizer (claimed).    ADVANTAGE - The method is short, energy efficient, environment-friendly and suitable for industrialization.    DETAILED DESCRIPTION - A kitchen waste organic fertilizer is prepared by taking kitchen garbage, draining, adding detergent, stirring, emulsifying, adding rice husk, mixing, adding Bacillus culture medium comprising 4 g/L disodium hydrogen phosphate, 1.2 g/L potassium dihydrogen phosphate, 2 g/L ammonium nitrate, 4 g/L ammonium chloride, 0.2 g/L magnesium sulfate, 10 g/L glucose and 1.5 g/L yeast powder at pH value of 7.5, fermenting at 60 degrees C for 48 hours, adding water, regulating water content, stirring at 60 degrees C, reacting for 12 hours, adding water, stirring, reacting for 24 hours, adding water, stirring, and reacting for 48 hours.
NOVELTY - A decomposed organic material is prepared by taking 90.01-99.9 wt.% sugar filter mud and 0.1-9.99 wt.% bagasse, piling, and carrying out aerobic fermentation for 10-35 days.    USE - Method for preparing decomposed organic material used for organic fertilizer, organic raw material processing nutrient matrix, plant nutrient element, microorganism microbial inoculum, biological organic fertilizer and organic-inorganic compound fertilizer (claimed).    ADVANTAGE - The method is environment friendly.
NOVELTY - A livestock and poultry manure decomposed organic material is prepared by livestock manure, conveying, carrying out aerobic fermentation for 5-20 days, and drying until moisture content of 50%.    USE - Method for preparing livestock and poultry manure decomposed organic material used for organic fertilizer, organic raw material processing nutrient matrix, plant nutrient element, microorganism microbial inoculum, biological organic fertilizer, organic-inorganic compound fertilizer and biological fuel (claimed).    ADVANTAGE - The method is simple and environment-friendly.
NOVELTY - Production of organic-inorganic compound fertilizer comprises crushing crop straw and carrying out hydrothermal pretreatment; adding biomass powder plant ash; and adding inorganic compound fertilizer and trace element, granulating, and packaging.    USE - Method for producing organic-inorganic compound fertilizer (claimed).    ADVANTAGE - The method can recycle waste.
NOVELTY - Liquid microorganism fertilizer comprises 30-50 pts. wt. Bacillus subtilis liquid, 25-40 pts. wt. Bacillus mucilaginosus liquid, 20-35 pts. wt. inorganic fertilizer, 15-30 pts. wt. livestock and poultry excrement, 5-15 pts. wt. malt oligosaccharides, 5-10 pts. wt. molasses, 1-5 pts. wt. magnesium sulfate, 2-6 pts. wt. borax, 4-8 pts. wt. zinc sulfate, 0.05-1 pt. wt. filler, 0.01-0.05 pt. wt. gibberellin, 0.01-0.05 pt. wt. cytokinin, and 40-55 pts. wt. water.    USE - Liquid microorganism fertilizer used for promoting growth and increasing yield of crop.    ADVANTAGE - The fertilizer is environment-friendly, has prolonged effective period, provides comprehensive plant nutrients, and maintains quality of soil.
NOVELTY - A cultivation substrate comprises 67.2-82.1 pts. wt. agriculture and forestry wastes, 6-10 pts. wt. soybean cake, 5-8 pts. wt. chicken manure, 5-7 pts. wt. slow-release organic fertilizer particles, 0.05 pt. wt. microbial fermentation agents, 0.01 pt. wt. cell division agent, 3.5-5.3 pts. wt. binders, 0.3-0.4 pt. wt. charcoal powder and 0.04 pt. wt. ammonium chloride.    USE - Cultivation substrate used for vegetables (claimed).    ADVANTAGE - The method is low-cost, energy-saving, and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cultivation substrate comprising crushing agriculture and forestry waste, screening to particle size of 2-1 mm, mixing agriculture and forestry wastes, soybean cake, chicken manure, slow-release organic fertilizer particles, microbial fermentation agents, cell division agent, binders, charcoal powder and ammonium chloride, pressing, rapidly heating to 80-90 degrees C, incubating for 30-60 minutes, and evaporating to remove remaining water.
NOVELTY - A citronella citronellal nitrile is prepared by taking hydroxycitronellal and isopropanol, mixing at - 5 to - 35 degrees C, adding 1-15 wt.% catalyst, 10-200 wt.% oxidizing agent and 100-300 wt.% ammonium hydroxide, reacting for 2-4 hours, carrying out solvent recovery, and purifying.    USE - Method for preparing citronella citronellal nitrile (claimed).    ADVANTAGE - The method is simple, has short reaction course, low-cost and environment-friendly. It has 83% product and product purity of 97%.
NOVELTY - Synthesis of vitamin E nicotinate comprises adding nicotinic acid and N,N'-carbonyldiimidazole into reaction system, carrying out first step reaction with organic solvent, carrying out second step reaction with tocopherol, and processing.    USE - Method for synthesis of vitamin E nicotinate (claimed).    ADVANTAGE - The method is easy, environment-friendly, and suitable for large scale industrial production.
NOVELTY - Synthesis of olanzapine intermediate comprises taking 2-(2-nitrophenyl-amino)-5-methyl-thiophene-3-carbonitrile (I) as raw material and reacting under acidic conditions with metal tin powder as reducing agent to give 4-amino-2-methyl-10H-thiophene(2,3-b)(1,5)-benzodiazepine hydrochloride (II).    USE - Method for synthesizing olanzapine intermediate (claimed).    ADVANTAGE - The method avoids using toxic stannous chloride solution, is environment-friendly and simple, uses only half mole of tin, avoids pollution, and has low cost.    DETAILED DESCRIPTION - Synthesis of olanzapine intermediate comprises taking 2-(2-nitrophenyl-amino)-5-methyl-thiophene-3-carbonitrile (I) as raw material and reacting under acidic conditions with metal tin powder as reducing agent to give 4-amino-2-methyl-10H-thiophene(2,3-b)(1,5)-benzodiazepine hydrochloride (II).
NOVELTY - Preparation of dihydrate amifostine comprises taking N-bromoethyl-1,3-propanediamine bis-hydrobromide salt molecules and sodium thiosulfate at molar ratio of 1:0.8-1.2, dissolving in 10-70% aqueous solution, reacting at 5-60 degrees C for 1.0-5.9 hours, adding dropwise methanol as accelerant, filtering, recovering methanol mother liquor by distillation and recycling.    USE - Method for preparing dihydrate amifostine (claimed).    ADVANTAGE - The green and environment-friendly method has easy operation, no organic solvent and increased pharmaceutical safety.
NOVELTY - Decoloring of dyeing gelatin hard capsule shell waste involves adding water to polyacrylamide, stirring and preparing polyacrylamide aqueous solution; taking dyeing gelatin hard capsule shell waste, adding water, standing, expanding, uniformly heating, completely dissolving and preparing dyeing gelatin hard capsule shell waste aqueous solution; adding activated coal to dyeing gelatin hard capsule shell waste aqueous solution, decoloring and filtering; and uniformly heating filtrate, stirring, adding adsorbent coagulant aid, continuously adding polyacrylamide aqueous solution and flocculating.    USE - Method for decoloring dyeing gelatin hard capsule shell waste (claimed).    ADVANTAGE - The method has simple, economical, practical and steady-quality process. It increases gelatin recovery rate, saves cost and protects environment.    DETAILED DESCRIPTION - Decoloring of dyeing gelatin hard capsule shell waste comprises:    (A) adding water to polyacrylamide, stirring to completely dissolve and preparing polyacrylamide aqueous solution;    (B) taking dyeing gelatin hard capsule shell waste, adding water, standing, expanding, uniformly heating at 35-85 degrees C, completely dissolving and preparing dyeing gelatin hard capsule shell waste aqueous solution;    (C) adding activated coal to dyeing gelatin hard capsule shell waste aqueous solution, decoloring and filtering to obtain milky white filtrate; and    (D) uniformly heating filtrate at 35-85 degrees C, stirring, adding adsorbent coagulant aid, continuously stirring, continuously adding polyacrylamide aqueous solution, flocculating, stopping adding polyacrylamide aqueous solution to obtain flocculating liquid, standing, performing sedimentation and separating supernatant.
NOVELTY - Magnetic carrier comprises 28-55% magnetic powder, 42-70.5% polyvinyl alcohol, 1-2% ethylenediamine and 1-2% polysiloxane.    USE - Magnetic carrier used for treating sewage (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing magnetic carrier, which involves:    (A) granulating polyvinyl alcohol and then mixing with magnetic powder to obyain mixture; and    (B) adding ethylenediamine and polysiloxane into mixture and then heating to obtain the product.
NOVELTY - Producing methane by bending pneumatic extrusion biogas generating system involves (a) adding raw material into feeding tube and fermenting raw material, collecting fermented slurry between discharge pipe and gas collecting pipe, extruding collected slurry, allowing slurry to flow through feeding tube, discharge pipe and cloth sieve, allowing slurry to flow through drain pipe in one-way, and storing slurry at lowest position of drain pipe, (b) reducing pressure of collected fermented slurry and circulating, and (c) collecting methane obtained in steps (a) and (b).    USE - Producing methane by bending pneumatic extrusion biogas generating system (claimed).    DETAILED DESCRIPTION - Producing methane by bending pneumatic extrusion biogas generating system involves (a) adding raw material into feeding tube (11) and fermenting raw material, collecting fermented slurry between discharge pipe (12) and adjacent gas collecting pipe (40), extruding collected slurry and allowing to flow through feeding tube, discharge pipe and cloth sieve, allowing slurry level to raise within pipeline, allowing slurry to flow through water pressure and drain pipe in one-way, and storing slurry at lowest position of drain pipe (50), (b) reducing pressure of collected fermented slurry, and circulating slurry, and (c) collecting methane obtained in steps (a) and (b).    DESCRIPTION OF DRAWING(S) - The drawing shows three-dimensional structure of system.    Feeding pipe (11)    Discharge pipe (12)    U-type fermentation pipeline (20)    Water pressure (30)    Discharge hole (32)    Gas collecting pipe (40)    Drain pipe (50)
NOVELTY - Method for improving yield of 5-aminolevulinic acid involves (a) regulating pH of organic wastewater to 6.5-7.5, adding ferrous ion and purple non-sulfur bacteria to organic wastewater, (b) fermenting mixture at 25-30 degrees C, illumination intensity of 1000-3000 1ux, and dissolved oxygen concentration of 0.5-1 mg/l, where the concentration of ferrous ion in mixture is 50-600 mu mol/l, and the organic wastewater has chemical oxygen demand (COD) of 6000-10000 mg/l, total nitrogen content of 400-800 mg/l and total phosphorus content of 20-60 mg/l.    USE - The method is useful for improving yield of 5-aminolevulinic acid (claimed).    ADVANTAGE - The method has high COD removal efficiency of 90%.
NOVELTY - Obtaining biogas involves pre-treating straw by first grinding straw in a mill to obtain crushed straw of particle size 0.1-2cm. Water is then added to the obtained crushed straw particles having content of 60-90%. The obtained mixture comprising 1.5-4% straw is uniformly mixed with 0.5-5% dry bacterial powder, and then performing fermentation at 20-60 degrees C for 1-30 days to obtain finished product.    USE - Method for obtaining biogas (claimed).    ADVANTAGE - The method enables higher production rate of biogas from straw in a short time.
NOVELTY - Preparation comprises 7-9 pts. wt. water lily extract, 5-7 pts. wt. chitosan, 10-12 pts. wt. polymeric guanidine, 8-10 pts. wt. plant polysaccharide, 1-2 pts. wt. alkaloids and 100 pts. wt. purified water.    USE - The preparation is useful for preventing spoilage in ginger (claimed). The ginger is useful for enhancing immunity.    ADVANTAGE - The preparation is nontoxic, and readily biodegradable, and avoids pollution, and enables to increase nutrient absorption rate up to 80%, and provides sterilization rate of 99.99%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the preparation, which involves (a) cleaning and washing water lily, and extracting water lily using supercritical extraction extractor, (b) adding polymeric guanidine and plant polysaccharide into reaction tank, mixing uniformly, adding purified water, stirring uniformly, until the mixture turns transparent, (c) adding water lily extract and alkaloids to the reaction tank, and mixing uniformly, (d) mixing chitosan and purified water in a ratio of 1:2, adding mixture into to reaction tank, and mixing uniformly, (e) adding purified water (100 unit), heating mixture at 30 degrees C for 15 minutes, and (f) cooling product and filling into bottles.
NOVELTY - Method for preparing sustained-release fertilizer, involves (a) preparing coating liquid by homogeneously mixing solute and solvent in a ratio of 1:17 plus minus 0.5, stirring the mixture, heating the mixture at 140-160 degrees C ad melting the mixture, (b) spraying the coating liquid on fertilizer feedstock by spray tower and spraying the coated liquid, (c) subjecting the coated fertilizer to exhaust gas treatment, and recovering and recycling the solvent, and (d) passing the processed coated fertilizer on conveyor belt and packing the obtained coated fertilizer.    USE - The method is useful for preparing sustained-release fertilizer (claimed).    ADVANTAGE - The method recycles waste bags, is environmentally-friendly and cost-effective, utilizes natural materials, and consumes minimal energy.    DETAILED DESCRIPTION - Method for preparing sustained-release fertilizer, involves (a) preparing coating liquid by homogeneously mixing solute and solvent in a ratio of 1:17 plus minus 0.5, stirring the mixture, heating the mixture at 140-160 degrees C ad melting the mixture, where the solute comprises polyethylene (PE), polypropylene (PP), polystyrene (PS), and cell opening agent in a ratio of 2:7:2:1, and the solvent is natural turpentine oil, (b) spraying the coating liquid on fertilizer feedstock by spray tower comprising circulating gas which is pre-heated at 90 plus minus 5 degrees C and spraying the coated liquid, (c) subjecting the coated fertilizer to exhaust gas treatment, and recovering and recycling the solvent, and (d) passing the processed coated fertilizer on conveyor belt and packing the obtained coated fertilizer.
NOVELTY - Salt of lesinurad (I) comprising a calcium salt, a potassium salt, a hydrochloride salt, an esylate salt, a mesylate salt, a 1,2-ethanedisulfonate salt, an isethionate salt or an arginine salt, and a cocrystal of (I) with proline or glycolic acid, are new.    USE - The salt and cocrystal of (I) are useful for: treating or delaying the progression or onset of a disease or disorder in a subject, where the disease or disorder is polycythemia, myeloid metaplasia, gout, a recurrent gout attack, gouty arthritis, hyperuricemia, hypertension, a cardiovascular disease, coronary heart disease, Lesch-Nyhan syndrome, Kelley-Seegmiller syndrome, kidney disease, kidney stones, kidney failure, joint inflammation, arthritis, urolithiasis, plumbism, hyperparathyroidism, psoriasis or sarcoidosis (all claimed); and preparation of solid dosage forms. No biological data given.    ADVANTAGE - The salt and cocrystal of (I): provide solid dosage forms owing to their ease of handling and superior pharmacological properties; are investigational agents in phase III clinical trial for treatment of gout; and can be prepared readily from environmentally friendly solvent systems using relatively simple processes.    DETAILED DESCRIPTION - Salt of lesinurad of formula (I) comprising a calcium salt, a potassium salt, a hydrochloride salt, an esylate salt, a mesylate salt, a 1,2-ethanedisulfonate salt, an isethionate salt or an arginine salt, and a cocrystal of (I) with proline or glycolic acid, are new. An INDEPENDENT CLAIM is also included for preparing the salt of (I) or the cocrystal of (I).
NOVELTY - A polymeric membrane is a plasma-treated polymeric membrane comprising polymeric blend containing intrinsic-microporous polymer (PIM) and polymer (B).    USE - Polymeric membrane is used for separating nitrogen from methane, hydrogen from methane, hydrogen from nitrogen, nitrogen from gaseous mixture including nitrogen and methane, hydrogen from gaseous mixture including hydrogen and nitrogen, and hydrogen from gaseous mixture including hydrogen and methane using separating device (all claimed). Can also be used for separating organic molecules e.g. ethanol, phenol, benzene and atrazine from water, and metal e.g. mercury(II) ion and radioactive cesium(I) ion.    ADVANTAGE - The polymeric membrane has excellent gas permeability and selectivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for separating component(s) from mixture of components;    (2) method of plasma-treating surface of polymeric membrane, involves subjecting at least a portion of polymeric membrane surface to plasma containing reactive species; and    (3) gas separation device.
NOVELTY - Method of determining degradation of cellulosic materials in real-time, involves (a) enzyme-mediating at least partial cleaving of the cellulosic materials to produce glucose monomers, (b) reacting the glucose monomers with glucose oxidase to produce hydrogen peroxide, (c) reacting the hydrogen peroxide with Fenton reaction catalyst to produce hydroxyl radicals, and (d) reacting the hydroxyl radicals with water-soluble monomer units having functional vinyl groups to produce polymeric coating on cellulosic materials.    USE - The method is useful for determining degradation of cellulosic materials in real-time which is useful for determining cellulolytic enzyme activity during biomass conversion, preferably biomass conversion for production of biofuel (all claimed).    DETAILED DESCRIPTION - Method of determining degradation of cellulosic materials in real-time, involves (a) enzyme-mediating at least partial cleaving of the cellulosic materials to produce glucose monomers, (b) reacting the glucose monomers with glucose oxidase to produce hydrogen peroxide, (c) reacting the hydrogen peroxide with Fenton reaction catalyst to produce hydroxyl radicals, where the reaction is performed at pH of less than 5.0, and (d) reacting the hydroxyl radicals with water-soluble monomer units having functional vinyl groups to produce polymeric coating on cellulosic materials, where the method does not perform external addition of glucose, and the polymeric coating is produced in spatially localized manner at site of enzyme mediated cleavage of the cellulosic material.
NOVELTY - Fertilizer comprises 50-70 wt.% mixture of fermented chaff and rice husk carbon, 10-18 wt.% nitrogen fertilizer, 8-15 wt.% phosphate fertilizer, 9-12 wt.% potassium fertilizer and 3-5 wt.% adhesive.    USE - Fertilizer used for planting rice (claimed).    ADVANTAGE - The fertilizer is nutritious, and ensures slow release property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) mixing and stirring 80-90 pts. wt. husk and 10-20 pts. wt. rice bran uniformly with 0.2-0.4 pts. wt. Bacillus subtilis liquid to obtain mixed material;    (B) performing fermentation by adding 60-70 wt.% water with mixed material for 5-7 days to obtain mixture of fermented chaff and rice husk carbon;    (C) mixing remaining components with mixture of fermented chaff and rice husk carbon, and then adding effective microorganisms broth and 40-50 wt.% water; and    (D) performing fermentation of the mixture in summer and autumn for 5-7 days, and in winter for 10-15 days to obtain final product.
NOVELTY - Preparing soil conditioner involves drying phosphogypsum at 40-55 degrees C for 1-2 hours. The dried gypsum is crushed and sieved. Phosphorus ore tailing and potassium feldspar are ground and sieved. The phosphogypsum powder, phosphorus ore and potassium feldspar are mixed to obtain mixture material that is mixed with water to obtain spherical or block-shaped material. The block material is sintered at 900-1050 degrees C for 0.6-1.3 hours. The sintering temperature is raised to 1050-1150 degrees C for 0.5 hours to obtain sintered clinker that is cooled to 20-50 degrees C, and then crushed and sieved to obtain product.    USE - Method for preparing soil conditioner (claimed).    ADVANTAGE - The method enables to prepare soil conditioner that ensures environmental protection, economic benefit and saving of water resource and drying energy.
NOVELTY - Fertilizing pseudoginseng seedling comprises (i) stirring a base fertilizer, sieving and applying the base fertilizer, and (ii) applying top dressing when the pseudoginseng germination rate is 10%.    USE - The method is useful for fertilizing pseudoginseng seedling (claimed).    ADVANTAGE - The method improves survival rate of pseudoginseng seedling.
NOVELTY - An amorphous nano-copper sulfide magnetic composite material comprises amorphous nano-copper sulfide:ferroferric oxide (Fe3O4) with mass ratio of 1:4-6. Amorphous nano-copper sulfide magnetic composite material is prepared by adding sodium sulfide nonahydrate (Na2S.9H2O) in water, adding Fe3O4, stirring to obtain 1st solution, adding copper(II) chloride dihydrate (CuCl2.2H2O) aqueous solution, reacting, standing, filtering precipitate, washing, and drying.    USE - An amorphous nano-copper sulfide magnetic composite material for removing antibiotic pollutants in water (claimed).    ADVANTAGE - Amorphous nano-copper sulfide magnetic composite material is easy to recover and regenerate and has strong antibiotic pollutant absorption ability, and preparation is simple, environment-friendly, and low-cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for removal of antibiotic pollutants in water which involves placing amorphous nano-copper sulfide magnetic composite material in antibiotic pollutant-containing wastewater, adsorbing, recovering adsorbed amorphous nano-copper sulfide magnetic composite material with magnet, and regenerating using hydrochloric acid and ethanol mixed solution.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the x-ray diffraction (XRD) pattern of amorphous nano-copper sulfide magnetic composite material.
NOVELTY - Seedling matrix comprises 15-45% peat soil, 10-20% expanded perlite, 3-11% pumice, 4-15% cinder, 5-15% timber wood, 5-25% carbonized rice husk, 0.5-2% sustained-release fertilizer, 0.5-2% water retention agent, and 10-30% bran.    USE - The seedling matrix is useful in nursery for cultivating purple cabbage, lettuce and leafy crops.    ADVANTAGE - The seedling matrix is prepared simply and cost-effectively, and environmentally-friendly, and utilizes waste materials.
NOVELTY - Preparation of 3-oxo-indoline compound (I) comprises taking N-Boc indole derivative (II) as raw material, carrying out oxidation-dearomatization reaction with ruthenium catalyst, organic solvents, and oxidizing agent at 25-150 degrees C for 12-36 hours in oil bath; and carrying out silica gel column chromatography separation, where molar concentration of organic solvent is 0.01-1 mmol/mL, molar ratio of N-Boc indole compound to ruthenium catalyst is 1:0.01-05, and molar ratio of N-Boc indole to oxidizing agent is 1:1-5.    USE - Method of preparing 3-oxo-indoline compound (claimed) used for organic synthesis of intermediate and in pharmaceutical field.    ADVANTAGE - The method is mild, has compatible functional group and substrate range and is environmental-friendly.    DETAILED DESCRIPTION - Preparation of 3-oxo-indoline compound of formula (I) comprises taking N-Boc indole derivative of formula (II) as raw material, carrying out oxidation-dearomatization reaction with ruthenium catalyst, organic solvents, and oxidizing agent at 25-150 degrees C for 12-36 hours in oil bath; and carrying out silica gel column chromatography separation, where molar concentration of organic solvent is 0.01-1 mmol/mL, molar ratio of N-Boc indole compound to ruthenium catalyst is 1:0.01-05, and molar ratio of N-Boc indole to oxidizing agent is 1:1-5.    R1=benzene, pyridine, cyclopropyl, cyclohexane, alkyl, or H; and    R2=alkyl, halo, or H.
NOVELTY - Use of Bacillus amyloliquefaciens in soil conditioner, is claimed.    USE - Use of Bacillus amyloliquefaciens in preparation of soil conditioner (all claimed).    ADVANTAGE - The environmentally-friendly soil conditioner obtained using the Bacillus amyloliquefaciens has excellent fertilizing effect, and effectively improves micro-ecological system of soil, stress resistance of crop, and quality and yield of crop, and decomposes pesticide residues.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (i) soil conditioner, which comprises Bacillus amyloliquefaciens, fertilizer and other components (c). The fertilizer comprises nitrogen, phosphorus and potassium. The component (c) comprises starch, talc, calcium carbonate, lime, gypsum, montmorillonite, kaolin, brucite, wood flour, straw, bentonite, fly ash, shell powder and carapace powder; and (ii) preparation of soil conditioner.
NOVELTY - Preparing bio-organic fertilizer involves grinding orange peel to obtain particles of size of 2-3 cm. Quick lime is used to adjust pH of orange peel powder to 7. Liquorice is pulverized to obtain the particle of 2-3 cm, and pulverized material is soaked to obtain liquorice powder. Orange peel powder, liquorice powder, rice husk, cake powder and chaff are mixed and stirred. Bacteria are added to the obtained mixture to decompose the obtained mixture. Decomposed product is covered with a plastic sheet.    USE - Method for preparing bio-organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare bio organic fertilizer that is and environment friendly, and saves resources. The method is easy to operate.    DETAILED DESCRIPTION - Preparing bio-organic fertilizer involves grinding orange peel to obtain particles of size of 2-3 cm. Quick lime is used to adjust pH of orange peel powder to 7. Liquorice is pulverized to obtain the particle of 2-3 cm, and pulverized material is soaked to obtain liquorice powder. Orange peel powder, liquorice powder, rice husk, cake powder and chaff are mixed and stirred. Bacteria are added to the obtained mixture to decompose the obtained mixture. Decomposed product is covered with a plastic sheet. Covered product is opened after six hours, where manure and fungus are added to the decomposed product to obtain a mixture. Obtained mixture is stirred and covered with plastic sheet to carry out fermentation. Fermentation mixture is stirred once in a day for six days. The fermented material is dried to obtain a bio-organic fertilizer.
NOVELTY - Buckwheat special composite fertilizer comprises 15-20 wt.% wheat straw, 10-15 wt.% peanut stem and leaves, 20-30 wt.% cattle and sheep excrement, 3-5 wt.% traditional Chinese medicine component, 5-20 wt.% urea, 1-10 wt.% calcium superphosphate, 1-10 wt.% bamboo carbon powder, 1-5 wt.% boric acid, 1-2 wt.% ferrous sulfate, 1-2 wt.% zinc sulfate, 1-2 wt.% sodium selenite and 0.5-2 wt.% monopotassium phosphate.    USE - Buckwheat special composite fertilizer used for inhibiting Rhizoctonia solani, Cercospora, Phyllosticta and Septoria and preventing buckwheat R. solani disease, leaf spot, brown blotch and Septoria disease.    ADVANTAGE - The buckwheat special composite fertilizer provides the nutrients needed for buckwheat growth and increases yield and quality of buckwheat.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of buckwheat special composite fertilizer comprising mixing wheat straw, peanut stem and leaves and cattle and sheep excrement, adding into a fermentation tank, fermenting for 30 days to obtain fermentation material, mixing the traditional Chinese medicine component raw materials, crushing, sieving by 150-mesh sieve to obtain traditional Chinese medicine component mixed powder, adding the fermentation material into a dryer, drying, adding urea, calcium superphosphate, bamboo carbon powder, boric acid, ferrous sulfate, zinc sulfate, sodium selenite, potassium dihydrogen phosphate, and traditional Chinese medicine component mixed powder, uniformly mixing and packaging to obtain the product.
NOVELTY - A pyrido(2,3-d)pyrimidin-2-amine derivative (I) is new.    USE - Pyrido(2,3-d)pyrimidin-2-amine derivative.    ADVANTAGE - The method is short, simple, convenient, safe, and environment-friendly.    DETAILED DESCRIPTION - A pyrido(2,3-d)pyrimidin-2-amine derivative of formula (I) is new. An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - This utility new type claims a closeness continuous feeding in A frequency biomass destructive distillation garbage heating furnace, comprising: a furnace body, a middle frequency heating system, a feeding system, a discharging system, a heat preservation insulation device one. This utility new type provide a non oxygen a indirect heating method, increase the efficiency of biomass dry distillation furnace, the biomass dry distillation furnace for biomass conversion for a use of a regeneration gas, oil and waste biomass carbon of velocity (efficiency), economical efficiency and environment-friendly. This utility new type adopt double-piston hydraulic pressure add material device. Feed and feeding piston is vertical to piston arrangement, a feeding piston has storage hopper, material feeding by pushing the piston to a receiving section before feeding piston and pushing head, a feeding piston travel , to form a closeness of section, when feeding to the furnace body inner pushing the feeding piston and the air. This utility new type finish the municipal domestic garbage treatment process without pollute, day the process domestic garbage, the domestic garbage is day more than 90% conversion is clean new energy.
NOVELTY - This new utility model claims of one of garbage and sludge and processing system, comprising: processing device for using protogenous rubbish pre pre-processing process of processing waste, obtaining device used for dehydrating for sludge dewatering, dryer for dehydration after the sludge and/or after waiting for disposing garbage drying to obtain waiting for processing raw material, extrusion forming device of receiving process for the raw material for extrusion molding and machining process, storage and extrusion forming device connected with the dry distillation furnace connected to make raw material dry distillation generating oil gas and solid product in downstream side of bin, condensing device connected downstream in the dry distillation furnace for oil gas product cooling, tar separating device and condensing device connected with and for cooling the oil gas product after separating to obtain carbonization, tar and sewage, air storage purification after the carbonization, after treatment device for sewage, tar and semi coke carry out follow-up treatment and recycling use. According to processing system of garbage and sludge of the new utility model, reducing of cost, and environment-friendly.
NOVELTY - This utility new type claims a a lower sucking type biomass gasification furnace, burning biomass raw material for a gas fuel, a furnace body, for containing biomass raw material, lower furnace body, the lower part is set with a furnace body, used for containing biomass raw material burning the product of the input device, and lower body connected, used for a biomass raw material after a reaction of gas fuel, ash, used for cleaning a lower inner furnace body is ash, comprising a, used for cleaning inner lower furnace body ash is ash removal mechanism, water groove of ash by removing ash removal mechanism is used for a lower furnace body and a cleaning channel of water groove. This utility new type by cleaning device equipped with a reservoir for the following at any time in a furnace body ash cleaning process, and the structure is simple, the mounting is convenient, using cleaning device of furnace ash directly entering into the water groove to middle, a ash scraping pollute around the environment, further below a furnace body through water seal, which avoids gas leakage of fuel.
NOVELTY - This utility new type claims a a lower sucking type biomass gasification furnace, burning biomass raw material for a gas fuel, comprising a, a furnace body, a side upper wall has equipped with multiple used for introducing combustion-supporting air of air inlet hole, lower furnace body, set at the lower part of a furnace body, a c, and lower body connected, output the biomass raw material after a reaction of gas fuel air supply device, used for a raw material of biomass combustion supply combustion-supporting gas, low device using steam separating device for biomass raw material in equipped with a steam isolation layer, a steam and separating steam combustion-supporting furnace waste heat of gas fuel or carry waste heat as a heat source of a production. This utility new type sideway by introducing combustion-supporting gas, solves the problem that the biomass material combustion uniformity problem is, by using combustion-supporting gas of a steam, reducing the nitrogen content in a gas fuel, using waste heat furnace a steam combustion-supporting, saves the energy, saves the device cost.
NOVELTY - This utility new type claims a biomass forming fuel automatic a complete device, comprising in turn a composed of a hopper, a feeding conveying with the sieving device, a feeding auger, a burner, a draught fan, a buffer, separator, separator has a dust remover and a hoisting machine, the hoisting machine has a feeding packing auger, the lower part feeding packing auger provided with welding table multi-particle machine, multi-exhaust port of grain machine welding table connected to smoke pipe, the smoke pipe has a second dust remover more discharge wherein a particle machine welding table by a conveyor with a cooler, the cooler has a side face has a third dust remover, a cooler by the second conveying with a packer has the lower part packer provided with conveying with finished product. Large amount of dust and fume This utility new type can adapt to large-scale production is needed, and a process for producing in a collective and then emptying after a treatment, to reduce atomphere pollute.
NOVELTY - This utility new type claims a biological diesel oil heating a flash device, comprising a middle three by one part, by a flange connection form one device, the upper part comprises liquid distributor mounted at upper end enclosure inner upper part is a plate pipe, as follows a plate located at the upper part of a pipe distributor under the falling film tubular heater mounted in the liquid inlet, the middle part comprises setting a tubular falling film heater lower part of a set, with gas-liquid separator is a network disk and setting a middle part of a plate tube between two two; the lower part height comprises a uniform arrangement of multi-block flash distribution plate, each block plate are provided with inner guide tube. The structure biology diesel oil heating evaporation device comprises pipeline and a cleaning labour intensity low when a biological diesel oil production, continuous production process, high-efficiency, energy-saving can is.
NOVELTY - Preparing imipenem antibiotic intermediates (I), comprises (i) reacting (3R,4R)-4-hydroxy-3-((R)-1-hydroxyethyl)azetidin-2-one compounds (II) with 2-diazo-3-oxopentanoate compounds (III) to obtain (R)-2-diazo-4-((2R,3S)-3-((R)-1-hydroxyethyl)-4-oxoazetidin-2-yl)-3-oxopentanoate compounds (XVI), and (ii) reacting (XVI) to obtain final product.    USE - The method is useful for preparing imipenem antibiotic intermediates.    ADVANTAGE - The method: shortens reaction period, reduces cost, reduces environmental pollution, and utilizes easily available raw materials; and has high product yield when compared to existing method.    DETAILED DESCRIPTION - Preparing imipenem antibiotic intermediates of formula (I), comprises (i) reacting (3R,4R)-4-hydroxy-3-((R)-1-hydroxyethyl)azetidin-2-one compounds of formula (II) with 2-diazo-3-oxopentanoate compounds of formula (III) to obtain (R)-2-diazo-4-((2R,3S)-3-((R)-1-hydroxyethyl)-4-oxoazetidin-2-yl)-3-oxopentanoate compounds of formula (XVI), and (ii) reacting (XVI) to obtain final product.    R1 = methyl, ethyl, p-nitrobenzyl, benzyl, allyl, 4-chlorobenzyl, 2-nitrobenzyl, 3-nitrobenzyl or 4-methoxybenzyl;    R2 = acetyl or benzoyl; and    R3 = trimethylsilyl or tert-butyldimethylsilyl.
NOVELTY - A potting process of tiamulin involves reacting truncated side pleuromutilin sulfonic acid ester, diethylamine and thioethane in ratio of 1:1.1-5:1-2, respectively at room temperature to 50 degrees C.    USE - A potting process of tiamulin.    ADVANTAGE - Method has simple operation, low cost, and is environment-friendly.
NOVELTY - The apparatus (1) has ammonia concentration-measuring device (5) and total nitrogen concentration-measuring device (7) that measures ammonia and total nitrogen concentration of treated water flowing out of biological reaction tank (3). A total phosphorus concentration-measuring device (8) measures total phosphorus concentration of treated water flowing out of tank. A control unit (9) adjusts range of atmosphere in adjustment region based on values measured by ammonia concentration-measuring device, nitrogen concentration-measuring device and phosphorus concentration-measuring device.    USE - Organic waste water treatment apparatus.    ADVANTAGE - The organic waste water treatment efficiency is improved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a processing method of the organic waste water; and    (2) a control program of organic waste water treatment apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the organic waste water treatment apparatus. (Drawing includes non-English language text)    Organic waste water treatment apparatus (1)    Biological reaction tank (3)    Ammonia concentration-measuring device (5)    Total nitrogen concentration-measuring device (7)    Total phosphorus concentration-measuring device (8)    Control unit (9)
NOVELTY - The method involves connecting a circulation fluidization bed combustion system with a fluidization bed gasification reactor system. An ash processing system is provided with a gasification process pneumatic purification system. A burner (1) is placed in a quadratic wind room (2). A flat orientation cap (4) is covered on a cold water level cloth air plate (3). A quadratic wind nozzle (5) is fixed in a return pipe (6) that is hinged in a returning device (7). A first cyclone separator (10) is connected with a second cyclone separator (12).    USE - Solid fossil fuel biomass gasification fine particles gasification method.    ADVANTAGE - The method enables reducing gasification cost, preventing water from sulphide and dust and avoiding waste heat problems.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a solid fossil fuel biomass gasification fine particles gasification method.    Burner (1)    Quadratic wind room (2)    Cold water level cloth air plate (3)    Flat orientation cap (4)    Quadratic wind nozzle (5)    Return pipe (6)    Returning device (7)    Cyclone separators (10,12)
NOVELTY - The furnace has a furnace main portion whose top end is closed. The side upper wall of the furnace main portion is equipped with multiple air introducing inlet holes. The bottom portion of the furnace main portion is comprised with a combustion-supporting steam input device, and a water jacket main portion (10) equipped with the side wall is located over the input hole of the grid type heat exchange device.    USE - Suction type biomass gasification furnace.    ADVANTAGE - The nitrogen content in the gas fuel is reduced, and reduced energy consumption is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the suction type biomass gasification furnace.    Pneumatic pump (7)    Water jacket main portion (10)    Steam-water separating device (11)    Furnace portion (101)    Grate (104)
NOVELTY - The device has spiral feeding device (3) arranged with feeding port (2) for conveying material to pyrolysis gasification chamber (4). The chamber inner portion is set with fire grate (5) and ash outlet (7). The chamber upper portion is set with smoke-pneumatic guide flow plate (8). A heat exchange tube (9) in arranged with pyrolysis pneumatic heat exchange pipe and air heat exchange pipe. A gas cooling purifier (13) is provided for discharging pyrolysis pneumatic gas through pneumatic outlet (14) to tar storing room (11) whose middle portion is set with oil guide plate (10).    USE - Suction-type fixed-bed household garbage gasification furnace waste heat recovery device.    ADVANTAGE - The suction-type fixed-bed household garbage gasification furnace waste heat recovery device is provided with improved waste heat recovery efficiency, high reliability and improved operation effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the suction-type fixed-bed household garbage gasification furnace waste heat recovery device.    Feeding port (2)    Spiral feeding device (3)    Pyrolysis gasification chamber (4)    Fire grate (5)    Ash outlet (7)    Smoke-pneumatic guide flow plate (8)    Heat exchange tube (9)    Oil guide plate (10)    Tar storing room (11)    Gas cooling purifier (13)    Pneumatic outlet (14)
NOVELTY - The method involves producing biomass pyrolysis gas and tar using solar energy biomass gasification device. The gasification kettle is heated. The gasification kettle is equipped with a stirrer connected with an inner power machine. The biomass raw material is stirred by the stirrer. The biomass raw material is the gasification kettle is uniformly heated. The spiral propeller is driven by the transmission for pushing a soften kettle, after tar by-product pre-heating and mixing processes.    USE - Method for gasification and pre-processing of biomass based on collection of solar energy, for agricultural production.    ADVANTAGE - The using rate of biomass is improved, and the energy consumption for gasification and pre-processing of biomass is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the process of gasification and pre-processing of biomass based on collection of solar energy.
NOVELTY - Safe disposal of dead animals involves collecting dead animals, crushing dead animals, sterilizing, finely pulverizing, cooling, adding additive and maggot-removing agent, removing maggot and residues, fermenting and adding organic fertilizer.    USE - Safe disposal of dead animal (claimed).
NOVELTY - Fertilizer comprises water retention agent, water, effective microorganism rejuvenation liquid and calcium nitrate in a mass ratio of 2-4:450-550:15-25:0.35-0.65.    USE - The fertilizer is useful for preventing and controlling rot disease of tomato (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing fertilizer, which involves (a) adding water retention agent to water, and (b) adding mixture to effective microorganism rejuvenation liquid and calcium nitrate.
NOVELTY - A composite microbial fertilizer comprises 20-32 pts. wt. microbial agent, 5-15 pts. wt. biochar, 20-30 pts. wt. nitrogen-phosphorus-potassium fertilizer, 1-5 pts. wt. trace elements, 3-10 pts. wt. nano titanium dioxide, 5-15 pts. wt. Chinese medicine composition, 12-20 pts. wt. silicon-calcium-magnesium fertilizer and 2-5 pts. wt. bamboo vinegar. The biochar is obtained by drying rice straw at 70 degrees C, crushing to length of 2 cm, heating under limited oxygen conditions at 10 degrees C/minute and 550 degrees C for 1 hour, cooling to room temperature, and sieving by 80 mesh sieve.    USE - Composite microbial fertilizer is used for rice.    ADVANTAGE - The economical and environmentally-friendly composite microbial fertilizer has excellent water-retention capacity, and improves physical and chemical properties, and aggregate structure of soil, and survival rate of transplanted rice, promotes rapid growth of rice roots, and reduces growth of weed and pest, use of pesticide, and occurrence of soil-borne diseases.    DETAILED DESCRIPTION - A composite microbial fertilizer comprises 20-32 pts. wt. microbial agent, 5-15 pts. wt. biochar, 20-30 pts. wt. nitrogen-phosphorus-potassium fertilizer, 1-5 pts. wt. trace elements, 3-10 pts. wt. nano titanium dioxide, 5-15 pts. wt. Chinese medicine composition, 12-20 pts. wt. silicon-calcium-magnesium fertilizer and 2-5 pts. wt. bamboo vinegar. The microbial agent is prepared by fermenting Bacillus amyloliquefaciens and Bacillus cereus, adsorbing using peat at adsorption ratio of 1:0.8, crushing, maintaining at less than 30% moisture, and obtaining microbial agent with effective viable count of 200 billon/g. The biochar is obtained by drying rice straw at 70 degrees C, crushing to length of 2 cm, heating under limited oxygen conditions at 10 degrees C/minute and 550 degrees C for 1 hour, cooling to room temperature, and sieving by 80 mesh sieve.
NOVELTY - A 2-(4-(4-chlorobenzoyl)phenoxy)-2-methylpropanoic acid polymorph having diffraction peaks in X-ray diffraction pattern at angle (2 theta ) of 5.5 plus minus 0.2, 7.9 plus minus 0.2, 15.9 plus minus 0.2, 22.2 plus minus 0.2, 22.6 plus minus 0.2, 23.1 plus minus 0.2, 27.9 plus minus 0.2 and 30.2 plus minus 0.2, is new.    USE - New 2-(4-(4-chlorobenzoyl)phenoxy)-2-methylpropanoic acid polymorph is useful in pharmaceutical composition for treating hyperlipidemia (all claimed).    ADVANTAGE - The 2-(4-(4-chlorobenzoyl)phenoxy)-2-methylpropanoic acid polymorph has excellent storage stability, and is prepared by simple and economical method using environmentally-friendly solvent, without using harsh operating equipment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of 2-(4-(4-chlorobenzoyl)phenoxy)-2-methylpropanoic acid polymorph, which involves mixing 2-(4-(4-chlorobenzoyl)phenoxy)-2-methylpropanoic acid with solvent, heating to dissolve all solids, cooling, crystallizing, filtering the precipitate, and drying the precipitate.
NOVELTY - Method for extracting mushroom polysaccharide from golden needle mushroom residue, involves using golden needle mushroom residue as raw material.    USE - The method is useful for extracting mushroom polysaccharide, which is useful for preventing and/or controlling viral diseases in tomato, pepper, tobacco, and cucumber (all claimed).    ADVANTAGE - The method is simple, cost-effective, and environmentally-friendly.
NOVELTY - Modified catalytic hydrogenation preparation of antioxidant 4010NA comprises preparing raw material solution from 4-amino-diphenylamine, acetone and ionic liquid modifier, conveying to fixed bed reactor with copper-based catalyst and catalytically hydrogenating to obtain antioxidant 4010NA. The ionic liquid modifier is 1-butyl-3-methyl-imidazolium tetrafluoroborate, 1-benzyl-3-methyl-imidazolium tetrafluoroborate, 1-(2-hydroxyethyl)-3-methyl-imidazolium tetrafluoroborate and/or 1-(2-hydroxyethyl)-3-ethyl-benzimidazolium tetrafluoroborate.    USE - Method for modified catalytic hydrogenation preparation of antioxidant 4010NA (claimed).    ADVANTAGE - The method has simple and convenient operation, high conversion rate, good selectivity, high yield, high product purity, reduced acetone consumption, reduced production cost and good implementation for industrial production.
NOVELTY - Preparing compound fertilizer involves dissolving monoammonium phosphate by steam heating at 50-80 degrees C to obtain slurry. Potassium hydrogen sulfate-containing sulfuric acid and solution of sulfuric acid and potassium chloride are reacted in tank at 100-150 degrees C with obtained slurry. The reaction mixture is neutralized with mixed acid and ammonia gas. The obtained mixture is granulated and spray-dried to obtain product.    USE - Method for preparing compound fertilizer (claimed).    ADVANTAGE - The method enables to prepare compound fertilizer that produces less phosphogypsum to ensure less environmental hazards.
NOVELTY - This utility new type provide the A a biomass granulator new ring mould structure, comprising ring mould main body, lower end of ring mould main body. b has fixed structure, b fixed structure is provided with uniform multi-polygonal mounting hole of regular hexagon fixing structure, regular hexagon fixing inner structure, inner polygonal mounting hole distribution and use is set with screw hole, the screw hole set with matching using a bolt, a bolt head less than polygonal mounted at the hole, polygonal mounting hole after bolt tightening spiral gap is provided with matched using of a mounting cover, a mounting cover provided with a multi-fastening button. This utility new type fixed structure through change the traditional ring mould is, it can further increase the ring mould of anti-extrusion ability and bolt loosing is not caused by a loose caused by a ring module, a mounting hole set into polygon structure, and provided with matched using a mounting cover, can preventing the bolt from the back wire of a phenomenon, and provided with matched using a mounting cover, which avoids a dust blocking bolt hole cause inconvenient dismounting equal.
NOVELTY - This utility new type relates to a treatment purification collagen protein is a positive ion exchange resin regeneration waste liquid of device, comprising in turn set, the first and second adjacent regeneration of a pool, mixing kettle, first, a reaction pool, a filter, a third, four reaction pool, a reaction pool equipped with sodium carbonate has the feeding port, the second reaction pool set has a ammonium bicarbonate, filtering a solid outlet and a third reaction pool is connected with a third reaction pool has set with caustic soda solution into wherein, a fourth reaction pool has set with calcium hydroxide solution into wherein, wherein liquid caustic soda storage tank and a fourth reaction pool are connected. A technology solution in, a valid process for carrying out a waste residue liquid in the acid leaching groove, and a product after processing a brine, ammonium chloride, sodium hydroxide, caustic soda and salt can used for other process a extract of deer-bone, ammonium chloride can as cultivating deer grass is fertilizer fertilizing, carrying out a waste is, use waste.
NOVELTY - Beside this utility new type claims a a biomass gasification furnace, comprising furnace body (11) and feeding device, a furnace body (11) is provided with furnace cover (12) and feeding port (14), a feeding port (14) a feeding device, a furnace body (11) is provided with (9), a furnace body (11) inner part provided with the following combustion furnace disk (10), a combustion furnace disk (10) is set with blowing device, a feeding port (14) is provided with a to combustion furnace disk (10) of the feeding pipe (13), the feeding pipe (13) is set with blowing radiating pipe (15). This utility new type comprises combustion efficiency and gasification speed is fast.
NOVELTY - Preparation of biological agent comprises drying alginate oligosaccharide waste liquid from processing seaweed to produce mannitol and sodium alginate, regulating the pH to 4-7 to obtain a concentrated biological liquid and drying.    USE - Method for preparing biological agent used for promoting crop growth (claimed).    ADVANTAGE - The method is simple and environment-friendly, and has small investment. The agent reduces organophosphorus pesticide residues.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the preparation of the agent which comprises processing the waste liquid with dilute nitric acid with pH 1-3, reacting at 10-35 C for 5-24 hours, adding acid or base to adjust the pH of the reaction solution to 4-7, filtering and concentrating or drying.
NOVELTY - Horizontal biomass granule granulator comprises power device (1), main machine, gear tank (2), granulating device, transmission shaft (3), drive shaft (4), driving shaft, pelleting device, machine shell (5), ring module, pressure roller, ring mold, annular mold insulating housing, outside material extrusion area and rotating drive shaft.    USE - Horizontal biomass granule granulator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of horizontal biomass granule granulator.    Power device (1)    Gear tank (2)    Transmission shaft (3)    Drive shaft (4)    Machine shell (5)
NOVELTY - Fertilizer comprises 11-13 pts. wt. nitrogen fertilizer, 9-11 pts. wt. phosphate fertilizer, 10-12 pts. wt. potassium fertilizer, 40-60 pts. wt. pig manure, 20-40 pts. wt. castor cake, 20-40 pts. wt. peat, 30-50 pts. wt. rock phosphate, 30-40 pts. wt. silkworm excrement, 12-14 pts. wt. mushroom residue, 10-12 pts. wt. cassava residue, 15-25 pts. wt. protein slag and 110-130 pts. wt. water.    USE - As fertilizer for Ulmus parvifolia (claimed).    ADVANTAGE - The fertilizer is cost-effective, increases quality and yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing the fertilizer, which involves crushing the above-mentioned materials except water, mixing with water, sealing, fermenting the mixture for 5-7 days, allowing the fermented product to stand for 15 hours and granulating the mixture.
NOVELTY - Dragon fruit fertilizer comprises 20-22 pts. wt. urea, 3-5 pts. wt. ammonium nitrate, 18-20 pts. wt. calcium superphosphate, 16-18 pts. wt. potassium sulfate, 13-15 pts. wt. potassium chloride, 4-6 pts. wt. monoammonium phosphate, 8-10 pts. wt. potassium humate, 0.2-0.4 pt. wt. magnesium amino acid chelate, 0.5-0.7 pt. wt. zinc chloride, 0.1-0.3 pt. wt. manganese sulfate, 0.7-0.9 pt. wt. ferrous sulfate and 20-30 pts. wt. bone meal.    USE - Dragon fruit fertilizer (claimed).    ADVANTAGE - The fertilizer has long-acting slow release effect, enhances early flowering, and early fruiting process, is rich in sugar and provides good taste to dragon fruit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing dragon fruit fertilizer, which involves (a) crushing the above-mentioned raw materials, (b) heating crushed raw materials at 80-100 degrees C and adding starch, fermenting mixture, and maintaining fermented mixture at 1-1.2 MPa, and (c) cutting and granulating product.
NOVELTY - Fertilizer comprises 70-90 pts. wt. dried chicken manure, 80-100 pts. wt. dairy manure, 20-30 pts. wt. sweet potato powder, 10-12 pts. wt. molasses, 5-7 pts. wt. yeast, 30-40 pts. wt. chlorobenzene, 15-17 pts. wt. radix isatidis, 13-15 pts. wt. pepper, 8-12 pts. wt. peanut, 15-17 pts. wt. monoammonium phosphate, 10-12 pts. wt. calcium powder and 180-200 pts. wt. water.    USE - Fertilizer (claimed).    ADVANTAGE - The fertilizer does not contain chemical additives, enhances soil durability, promotes leaves growth of crops and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing fertilizer which involves, (a) crushing the above-mentioned raw materials, (b) adding crushed raw materials to water and sealing mixture, fermenting sealed mixture for 6 days and maintaining for 8 hours, and (c) pelletizing fermented mixture.
NOVELTY - Preparation of nifuratel (I) comprises dissolving sodium methoxide in methanol, adding 3-methylthio-2-hydroxy-propylhydrazine (A), dripping dimethyl carbonate, and conducting cyclization reaction to obtain N-amino-5-methylthiomethyl-2-oxazolidinone (B); adding 5-nitro-furfural ethyl ester (C) with methyl alcohol, and under acidic condition, conducting catalytic hydrolysis reaction by heating at reflux to prepare 5-nitrofurfural (D); and dropping compound (B) reaction liquid to compound (D) reaction liquid, and conducting dehydration condensation reaction to obtain nifuratel crude product.    USE - Preparation of nifuratel (I) (claimed).    ADVANTAGE - The method provides nifuratel (I) having purity of more than 99.97% and yield of more than 96%, has a total yield of greater than or equal to 104% and convenient and easy operation, is simple and easy to implement and suitable for large-scale industrial production, uses raw materials, which have rich sources and are inexpensive and easy to obtain, and reduces environmental pollution.    DETAILED DESCRIPTION - Preparation of nifuratel of formula (I) comprises dissolving sodium methoxide in methanol, adding 3-methylthio-2-hydroxy-propylhydrazine of formula (A), dripping dimethyl carbonate, and conducting cyclization reaction to obtain N-amino-5-methylthiomethyl-2-oxazolidinone of formula (B); taking 5-nitro-furfural ethyl ester of formula (C), adding methyl alcohol, and under acidic condition, conducting catalytic hydrolysis reaction by heating at reflux to prepare 5-nitrofurfural of formula (D); and dropping compound (B) reaction liquid to compound (D) reaction liquid, conducting dehydration condensation reaction to obtain nifuratel crude product, cooling to room temperature, filtering, methyl alcohol washing the filter cake, spin-drying methyl alcohol, pure water washing the filter cake until washing water pH is greater than 6, pulping and washing with methanol, and drying to obtain (I).
NOVELTY - The system has a methane boiler nursing room whose inner part is fixed with a heating device. A marsh gas boiler passes hot water to a water heating device. The nursing room passes floor flushing waste water flow into a marsh gas pool. The marsh gas boiler is provided with a vertical furnace body. A furnace wall of the furnace body is fixed with an interlayer that is utilized for connecting a water outlet with the heating device. A water inlet is connected with a furnace head by using a pipeline. A top part of the furnace body is fixed with a chimney.    USE - Marsh gas pool comprehensive utilization system.    ADVANTAGE - The system increases biogas slurry usage rate, and is energy saving.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a marsh gas pool comprehensive utilization system.'(Drawing includes non-English language text)'
NOVELTY - Synthesizing highly purified keto acid salt involves reacting aldehyde derivative (1) and glycine in presence of L-threonine aldolase as catalyst to obtain 4-hydroxy-3-methyl-2-keto derivative. The obtained 2-keto acid derivative is reacted with L-threonine deaminase as catalyst to perform enzyme catalyzed reaction at 20-40 degrees C for certain duration to obtain 2-keto acid derivative (2).    USE - Method for synthesizing highly purified keto acid salt (claimed).    ADVANTAGE - The method enables to synthesize highly purified keto acid salt in a simple, eco-friendly and cost-effective manner.    DETAILED DESCRIPTION - Synthesizing highly purified keto acid salt involves reacting aldehyde derivative of formula (1) and glycine in presence of L-threonine aldolase as catalyst to obtain 4-hydroxy-3-methyl-2-keto derivative. The obtained 4-hydroxy-3-methyl-2-keto derivative is reacted with L-threonine deaminase as catalyst to perform enzyme catalyzed reaction at 20-40 degrees C for certain duration to obtain 2-keto acid derivative of formula (2). The obtained 2-keto acid derivative products are purified by chromatography using an alkali metal carbonate or alkali metal bicarbonate to adjust the pH to 4.0-8.0 in presence of activated carbon to obtain 2-keto acid salt derivative. The obtained 2-keto acid salt derivative is crystallized in vacuum to obtain highly purified keto acid salt of formula (3).    R=1-4C aliphatic hydrocarbon group; and    M=alkali metal ion.    .
NOVELTY - Producing biofuel and chemical intermediates involves adding 0.5- 5% (w/v) degradation solution into the large red algal biomass, and then vortexing the obtained mixture. The uniform mixture is then filtered to collect crude slurry, followed by removal of inhibitors. The crude slurry is then passed through molecular sieve adsorption column, an activated carbon column, ZSM-5 zeolite in fixed-bed columns, NaY zeolites, 13A type molecular sieve, or chitosan to obtain the desired product.    USE - Method for producing biofuel and chemical intermediates, which are used for degradation of organic matter (claimed).    ADVANTAGE - The biofuel is obtained in a simple, convenient and cost-effective manner by performing red algal biomass fermentation.
NOVELTY - A hydrogen generating device (100) comprises reformer (2) which generates hydrogen-containing gas through reforming reaction, raw material supplier (4), reaction gas supplier (6), hydro-desulfurizer (8) which removes sulfur compound in raw material, recycle flow passage (10) which supplies part of hydrogen-containing gas to hydro-desulfurizer, closing device (12) which closes recycle flow passage, and controller (14).    USE - A hydrogen generating device for fuel cell system (claimed).    ADVANTAGE - Hydrogen generating device reduces activity decrease in hydrodesulfurization catalyst and amount of water condensed in hydro-desulfurizer and suppresses carbon deposition in reformer.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) fuel cell system containing hydrogen generating device and fuel cell which generates electric power using hydrogen-containing gas;    (2) operation of hydrogen generating device which involves stopping operation by closing recycle flow passage and supplying raw material to hydro-desulfurizer and supplying raw material passed through hydro-desulfurizer and reaction gas to reformer to generate hydrogen-containing gas; and    (3) operation of fuel cell system which involves stopping operation by closing recycle flow passage and supplying raw material to hydro-desulfurizer and supplying raw material passed through hydro-desulfurizer and reaction gas to reformer to generate hydrogen-containing gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of hydrogen generating device.    Reformer (2)    Raw material supplier (4)    Reaction gas supplier (6)    Hydro-desulfurizer (8)    Recycle flow passage (10)    Closing device (12)    Controller (14)    Hydrogen generating device (100)
NOVELTY - Producing oxidation-stabilized biodiesel, comprises adding 0.005-0.5 wt.% composition comprising 40-60 wt.% mixture containing 1-4C alkylated mono- and 1-4C alkylated bisphenol, 0-5 wt.%, preferably 1-5 wt.% chelating agent, and 35-59 wt.% solvent including aprotic amides and/or cyclic ketals to biodiesel.    USE - The method is useful for producing oxidation-stabilized biodiesel as fuel (all claimed).    ADVANTAGE - The method produces biodiesel having high antioxidant concentration and anticorrosive properties.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) the oxidation-stabilized biodiesel produced using the above method; and    (2) the composition.
NOVELTY - A kind wifi a gas detector, comprising power supply, temperature detection module, formaldehyde detection module, a humidity module, carbon dioxide detecting module, a detecting a, a center and a wifi module, input end of center processing chip receiving temperature detection module, formaldehyde detection module, a humidity module, a carbon dioxide and a a a a a a a, a terminal and indicating lamp and the center processing chip connected with the display screen, the center processing chip wifi module and a bi-direction communication, and connected with RG45 wire interface. The utility model is new type can real time monitor and a numerical display air and particulate matter concentration, the formaldehyde gas concentration, air temperature humidity, carbon dioxide concentration and a concentration, and having RG45 wire interface and wifi a connection function, the user can according to the own requirement independently using a wired or wireless connection.
NOVELTY - The utility model claims a 30m3 raw material distribution slot, comprising a raw material groove, the lower part of the raw material groove through pipeline connected with a transport pump, left end of raw material groove through pipeline connected with a methanol pump and acetone pump, upper part of the middle groove through pipeline connected with the raw material with a raw material tank, a tank is outside coated with cooling liquid, the cooling liquid is freezing brine. The utility model is new type propane and a distillation using low temperature cooling vent 3 a recovery, a raw material without volatilization, zero discharge, to pollute air gradually reducing.
NOVELTY - This new utility model relates to one of continuous biomass carbonization device, comprising bracket and set on bracket of the carbonizing cylinder, wherein also comprises one grade spiral conveyer, carbon discharging chamber and combustion furnace, one grade spiral conveyer comprises one level out cylinder, one grade motor rotate at one level spiral shaft and one level out cylinder and drive one of spiral shaft and lever, one lever outside cylinder of one end set with feedstock wherein, after the other end through the carbonizing cylinder and the carbon discharging chamber connected, carbonizing cylinder and can carrying on heat pipe connect, heat from heat can for pipe can enter into carbonizing cylinder and the space between one level out cylinder, outlet coal chamber by smoke gas tube and the combustion furnace connected, connect the heat can for furnace tube, carbon discharging chamber has coal outlet port. This new utility model for producing carbonization smoke gas by the smoke gas pipe entering burning furnace and burning product and then enter into heat energy can for tube as carbonizing and energy, implementation of hot circulation can utilize, eliminate pollute discharge.
NOVELTY - The new type utility claims fluidization bed application field, specifically a kind of adjustable biomass fluidization bed gasification device, comprising a gasification furnace, the gasification reaction furnace middle part and a gasification reaction area, the upper part for reducing flow area, and the top has a air outlet pipe, lower part connected with air inlet pipe, the gasification reaction area is set with temperature sensor, in the gasification reaction area and a side connected with a feeding port, the feeding port set with a feedstock switch, another end air inlet pipe is connected with the storage cabin, and a air inlet pipe set with a control valve, another side bin is connected with the air pipe, the air pipe set with a vent switch. The utility model is new type of goal is providing a kind of adjustable biomass fluidization bed gasification device, can be a whole gasification reaction and control is carried out under a best temperature, the biomass is a full process, reducing impurity product, at the same time aiming at the different biomass provide the best of air flow, a reducing air flow out with the biomass content.
NOVELTY - The new type utility claims fluidization bed application field, specifically a biomass high use rate of a fluidization bed gasification device, comprising a gasification furnace, the gasification reaction furnace middle part and a gasification reaction area, the upper part for reducing flow area, and the top has a air outlet pipe, lower part connected with air inlet pipe, the gasification reaction area bottom is set with ventilating plate, the upper part a plate-reducing reducing flow separated and opened, a vent plate and down flow plate is provided with a vent hole, the gasification reaction area and one side connected with a feedstock, the air outlet pipe front end set with vent hole of baffle plate, and the air outlet pipe set with internal sum pump on back baffle plate. The utility model is new type of goal is fluidization bed gasification device providing a plant biomass using rate is high, structure is simple, a simple and convenient, can be reducing air flow takes away the biomass content, reducing to obtain the combustible gas in the biomass solid content, at the same time increase in the biomass utilization rate of fluidization bed gasification device.
NOVELTY - Biodiesel production involves performing transesterification of waste compatible with biodiesel production by using corona discharge plasma reactor. The corona discharge plasma reactor allows separate controlling of input and output of a gas flow and a stream of liquid material. The raw material is saturated frying oil or saturated fatty acid.    USE - Method for producing biodiesel.    ADVANTAGE - The method produces superior quality biodiesel in a simple, cost-effective and eco-friendly manner by using waste material and without generating acids, alkalis and glycerol as waste material, facilitates easier separation of biodiesel, and eliminates purification process.
NOVELTY - Preparation of a urea-sulfur fertilizer comprises supplying urea and sulfur to a dispersion mill where a rotor turns within a slotted stator, thus providing a dispersion of molten urea and molten sulfur; and supplying the dispersion of molten urea and molten sulfur to a forming unit to provide the urea-sulfur fertilizer. The solid sulfur, solid urea or solid urea-sulfur is supplied to the dispersion mill.    USE - Method for preparing a urea-sulfur fertilizer (claimed).    ADVANTAGE - The method is simple, has reduced energy requirements compared to conventional methods, and enables short residence times for melting and mixing the constituents, thus reducing the need for separate melters and reducing the risk of impurity formation.
NOVELTY - The method involves providing reinforcing elements (7) having reticular structure. The containing site (2) comprising base (3) and side wall (4) of ground is formed. The reinforcing elements are positioned on upper abutment surface of the first ground layer. The second ground layer is formed so that reinforcing elements are interposed between first and second ground layers. The upper abutment surface is extended around the base to define closed outline. The reinforced layer is overlapped to define the inner surface of side wall.    USE - Method for forming tank for biogas producing plants (all claimed) for producing biogas from urban organic waste and manure produced by farming and residuals of agro-industry.    ADVANTAGE - The tank for biogas plants is provided to reduce the installation and disposal costs of the structure. The tightness against leakages or seepages is ensured without causing undesired stresses to damage the membrane.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a tank for biogas producing plants; and    (2) the biogas producing plants.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the tank for biogas producing plants.    Tank for biogas producing plants (1)    Containing site (2)    Base (3)    Side wall (4)    Reinforcing element (7)
NOVELTY - The explosive device has steam generating module (1), gas storage module, explosive case and condensing module. The steam generating module generates overheat steam at more than 100 degrees C. The gas storage module is provided for storage of over-heat steam gas. The explosive case is provided with oil tea seed to which stored over-heat steam gas is supplied for explosion. The lower side of the explosive case is arranged with a condensing module for condensing the over-heat steam gas and sending again to the steam generating module.    USE - Explosive device for camellia seed shell.    ADVANTAGE - The lower side of the explosive case is arranged with a condensing module for condensing the over-heat steam gas and sending again to the steam generating module, such that the water gasification is performed efficiently. The uniform heating is realized. The noise is reduced. The energy saving is performed efficiently at short time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the explosive device.    Over-hot steam generating device (1)    Metal pipe (2)    Solenoid valves (3,4)    One-way valve (5)    Pressure sensor (7)
NOVELTY - Preparing bio-oil, comprises taking biomass as raw material, uniformly mixing by adding an additive into a microwave, carrying out first microwave pre-heating treatment, then carrying out microwave pyrolysis, pyrolyzing volatile content, condensing, and separating oil-aqueous phases, to obtain oil phase, namely heavy bio-oil, and aqueous phase, namely water-containing light bio oil, and taking out water by carrying out reactive distillation each time, to obtain light bio-oil having low water content.    USE - The bio-oil is useful as fuel oil.    ADVANTAGE - The method has high yield, and produces product with high calorific value.
NOVELTY - The new type utility claims one kind using microorganism to integrated sewage treatment device of sewage purification. A lifting a goal plant can increase sewage treatment efficiency and improves purification water out water quality glass steel integrated sewage treatment device. A glass steel is made by a tank body, a tank body by internal separate plate in turn is divided into a pre-processing, , aerobic room and machine room, the pre-processing room, , aerobic room through a water flow channel connected in sequence, the machine room and the aerobic room between a sealing clapboard, the pre-processing room provided with PH value regulating a, also comprising water heater, air inlet pipe of the water heater and the Anaerobic a connected, a water pipe and a water heater into the Anaerobic indoor. A can for pre-processing sewage, regulating PH value of sewage make it fit a. Anaerobic aerobic microorganism, increase temperature of Anaerobic indoor sewage, promote growing a. Anaerobic microorganism, accelerate speed of Anaerobic treatment, increase efficiency of sewage treatment, increase purification effect.
NOVELTY - This utility model belongs to energy production facility, especially relates to a vigetable greenhouse special air solar heating biogas digester, a lining plate support in a marsh gas pool insulating layer (7), (7-1) fixing one of marsh gas pool and insulating layer (7) is a shape of sealed lining plate (7-2), a lining plate (7-2) in space for marsh gas pool (7-4), a storage bag (3) fixing on greenhouse edge wall (2) and a greenhouse framework (6), a sun side outside a greenhouse (6) floor (12) on inclined fixing air solar energy heat collector (11), solar energy air heat collector (11) with hot air pipe (9) and marsh gas pool (7-4) is connected as follows, the upper part of heating furnace (10) with a hot air pipe (9) connected, a condition with the solar under the solar energy for marsh gas pool heating, in a marsh gas pool temperature not enough in a gas heating furnace through a hot air pipe for marsh gas pool heating, the whole structure is simple and practical, energy-saving, suitable use.
NOVELTY - Preparing petrochemical natural gas comprises (i) taking limestone and reacting at high temperature to obtain carbon dioxide, (ii) reducing carbon monoxide to obtain carbon monoxide, and (iii) reacting carbon monoxide and hydrogen in presence of catalyst.    USE - The method is useful for preparing petrochemical natural gas (claimed).    ADVANTAGE - The gas is green in color, satisfies energy requirements and replaces variety of energy resources.
NOVELTY - Biomass gasification furnace comprises a furnace body (1), a furnace grate (3), a feeding port, a fuel gas nozzle, an air inlet, and an ash room (5). The gas inlet is set with a nozzle. The feed inlet and gas nozzle is provided in the upper furnace body. The furnace body inner and outer liner is interlayered structure and is connected on the bottom. The feed inlet and fuel gas nozzle is connected with the furnace body inner liner. The air inlet and the furnace body outside container are connected to each other. The furnace grate is set in tank bottom of the furnace body.    USE - Used as a biomass gasification furnace.    ADVANTAGE - The furnace can achieve continuous thermal cracking gasification for many hours, can completely combust, has high thermal efficiency, is dust-free, can achieve continuous stable gas production, and is safe and stable to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the biomass gasification furnace.    Furnace body (1)    Sealing head (2)    Furnace grate (3)    Guide rail (4)    Ash room (5)
NOVELTY - The unit has a sealed infrared heating furnace (19), a cooling system, a discharging device and a cooling box unit. The cooling box unit periphery is equipped with a circulation water cavity (5). The heating furnace is connected with the box unit through a gas solid separator (2). A temperature control system is provided with a programmable logic controller. The infrared heating furnace is equipped with a feeding device. The cooling box unit is equipped with a discharging device.    USE - Infrared radiation type biomass thermo-chemical conversion unit.    ADVANTAGE - The large application area is achieved. The biomass feedstock can be heated with different temperature range environments with linear temperature to obtain different types of products. The heating and cooling process can be performed at the same time, without the need for lifting equipment and raw materials from the heating chamber into the crane hanging out for loading and unloading. Thus, the convenient control and reduction in the labor cost are achieved. The circulating water injection chamber is provided at the periphery of the three cooling chambers, to achieve the different components concentrated in the respective chamber after pyrolysis of biomass. The simple and compact structure with low production cost is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the infrared radiation type biomass thermo-chemical conversion unit.    Gas solid separator (2)    Circulation water cavity (5)    Oil condensing separator (6)    Oil liquid cooling chamber (7)    Sealed infrared heating furnace (19)
NOVELTY - The furnace has a furnace body (1) provided with a feeding port (8), a fuel gas nozzle (9), an air inlet (5) and a dust outlet (7). The feeding port is connected with a gasification room (11) that is fixed with an air inlet room (12). The fuel gas nozzle is matched with the gasification room. The air inlet is fixed with a conveying mechanism (4). The gasification room and the air inlet room are fixed on a conveying machine seat. The conveying mechanism comprises a guide wheel (42) and a reciprocating grate (43). The conveying mechanism is equipped with a cooling room (6).    USE - Horizontal biomass gasification furnace.    ADVANTAGE - The furnace is provided with the reciprocating grate so as to absorb the furnace heat due to hot air flow, thus cooling the furnace body. The furnace is safe and stable to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a horizontal biomass gasification furnace.    Furnace body (1)    Conveying mechanism (4)    Air inlet (5)    Cooling room (6)    Dust outlet (7)    Feeding port (8)    Fuel gas nozzle (9)    Gasification room (11)    Air inlet room (12)    Guide wheel (42)    Reciprocating grate (43)
NOVELTY - Non-explosive and non-flammable nitrogenous fertilizer based on ammonium nitrate is prepared using ammonium nitrate, urea and formaldehyde.    USE - The non-explosive and non-flammable nitrogenous fertilizer in form of granules, is used in agricultural soil for increasing assimilation of nitrogen content by plants (all claimed).    ADVANTAGE - The non-explosive and non-flammable nitrogenous fertilizer contributes nitrogen to agricultural soils, minimizes the use of fertilizers in the production of explosives for terrorism purposes, and does not release harmful gases and greenhouse gases e.g. ammonia and contamination water by its chemical ingredients, preferably nitrates.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the non-explosive and non-flammable nitrogenous fertilizer, which involves dissolving the ammonium nitrate, urea and formaldehyde in water, homogenizing until obtaining a uniform mixture, adding a catalyst, optionally homogenizing to perform a chemical reaction, granulating and drying product.
NOVELTY - A methane absorbent comprises 0.3-1.8% vegetable oil, 5-15% anionic surfactant, 0-4% decamethyl cyclopentasiloxane, 0-1% activated carbon and remainder of water.    USE - Absorbent is used for reducing concentration of methane in gas generated from coal mines.    ADVANTAGE - The absorbent is economical, increases solubility of methane, and rapidly and efficiently reduces concentration of absorbent in air.
NOVELTY - The apparatus (4) has a cathode compartment (400), an anode compartment (401), and a bridge. The cathode compartment retains a first electrolyte, and has a cathode (403) connected to a negative terminal of a direct current source and an outlet (405) to collect hydrogen produced during electrolysis. The anode compartment has retains a second electrolyte, and has an anode (402) connected to a positive terminal of the current source. The bridge has a first end immersed in the first electrolyte in the cathode compartment and a second end immersed in the second electrolyte in the anode compartment.    USE - Production apparatus for electrolytically producing hydrogen from sea water.    ADVANTAGE - Environment friendly method and apparatus for producing hydrogen is provided. Generation of chlorine in the production of hydrogen is prevented. Production method of hydrogen is made simple and cost effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a process for producing hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic sectional view of the production apparatus of hydrogen.    Production apparatus of hydrogen (4)    Cathode compartment (400)    Anode compartment (401)    Anode (402)    Cathode (403)    Outlet (405)
NOVELTY - The device has a bottom funnel (11) and a water tank (1). Center portion of the water tank is provided with bracket (2). The bracket is provided with a drain outlet (12) in the bottom of the water tank and a matching and filtering network (22). The bracket is provided with a water inlet through hole (21) in a side portion. The bracket is provided with a centre conduit (3). The centre conduit is provided with a radiant type jet hole (31) at a side portion. The centre conduit is provided with a trans-propeller (4).    USE - Radiant jet circulation type dirt collection device used in ocean fishing industry for prawn cultivation.    ADVANTAGE - The dirt collection device does not require any biochemical drugs. The residual bait and excrement is removed efficiently. The dirt is discharge automatically. The water changing amount is reduced effectively. The structure of the dirt collection device is simplified. The construction cost of the dirt collection device is reduced with efficiency. The cost saving and ecological friendly dirt collection device is obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the radiant jet circulation type dirt collection device.    Water tank (1)    Bracket (2)    Centre conduit (3)    Trans-propeller (4)    Bottom funnel (11)    Drain outlet (12)    Water inlet through hole (21)    Matching and filtering network (22)    Radiant type jet hole (31)
NOVELTY - Extracting litchi polyphenols involves drying litchi fruit peel at low temperature using liquid nitrogen. The dry litchi fruit is crushed and sieved to obtain litchi peel powder that is extracted using 60-80% ethyl alcohol and surfactant for 60-90 minutes at 50-70 degrees C. The obtained extract is purified with column chromatography using solvent. The pure extract is freeze-dried to remove powder.    USE - Method for extracting litchi polyphenols (claimed).    ADVANTAGE - The method enables to extract litchi polyphenols in efficient, eco-friendly and cost-effective manner.
NOVELTY - Obtaining yam total saponin involves extracting yam with 65% alcohol for 3 times, every time for 1.0 hour, where obtained extracts are concentrated. The obtained concentrate is purified using macroporous resin with separation column, ethyl alcohol and distilled water. The pure extract is concentrated and crushed to obtain product.    USE - Method for obtaining yam total saponin (claimed) used in food, medicine and chemicals.    ADVANTAGE - The method enables to obtain yam total saponin in simple manner without polluting environment.
NOVELTY - Composition is prepared by mixing and grinding 10 pts. wt. rhubarb, 10 pts. wt. purslane, 10 pts. wt. Phellodendron, 10 pts. wt. radix scutellariae, 12 pts. wt. toad, 8 pts. wt. honeysuckle, 8 pts. wt. ginger and 15 pts. wt. licorice.    USE - The composition is useful for preventing and treating gill rot disease, enteritis and red skin disease of grass carp (claimed).    ADVANTAGE - The composition is cost-effective and environmentally-friendly, and does not generate drug resistance.
NOVELTY - The utility model is new type claims a Chinese herbal medicine packaging bag, comprising a bag main body, a bag main body upper end and a side upper edge is set with opening, the bag main body upper end and another side edge and a notch corresponding to the position to install with hole, lower end of bag main body set with a concave groove. The packaging bag can be as one of stirring rod, stirring Chinese herbal medicine, accelerate the dissolution, at the same time it can avoid problem of tearing and deviation in tearing process, which avoids the separation of problem after packing bag tearing, reducing pollute environment.
NOVELTY - The new type utility claims a barn a fermentation bed padding with stirrer, comprising a machine, a machine frame mounted with the engine, the engine power with a stirring gearbox and walking gear box, the output shaft of the stirring gearbox connected with mixing stirring shaft and stirring mixing knife roller, output shaft of the walking gear box connected with the walking driving shaft and walking wheel, front end and rear end of the machine frame also respectively provided with back wheel cross sleeve, the back wheel cross sleeve moving sleeve is inserted with a back wheel connecting rod, each of the back wheel connected with outside end of transverse rod respectively provided with back wheel vertical sleeve, each of the back wheel vertical pipe moving sleeve is inserted in the wheel connected with vertical rod, each of the wheel connected with the lower end of the vertical rod connected with the walking wheel. The utility model is new type aiming at a low barn special design, not by a limit operation time, can be a full of a mattress material to carry out stirring barn, reduce the labour intensity of the worker is convenient for excrement for fast decomposing microorganism.
NOVELTY - This utility model claims a domestic garbage organic matter water concentration anaeration in normal temperature processing production line, comprising a crushing machine, beater, deploy sand removing tank, average regulating pool, heating device, Anaerobic reactor, wherein the crushing machine in turn through pipeline and beater, deploy sand removing tank, average regulating pool, Anaerobic reactor connected; the heating device is respectively connected with a uniform value regulating pool, Anaerobic reactor. The utility model with a small floor space, no pollute, fast processing, especially can satisfy the following existing conditions for organic matter garbage processing information.
NOVELTY - The utility model claims a novel biogas slurry filter type anaerobic fermentation tank, belonging to the field of device, wherein the device comprises a tank body, a driving device, a stirring device, a filtering device, a feeding port, a heating coil pipe, an exhaust port, stirring shaft and a stirring paddle leaf of a radial force, dispersing with strong cutting effect, causing large particle diameter of solid object and is a full mixture of biogas fermentation by a completely, at the same time the material crust, set with two of a discharging port, can be effectively and the biogas and slag discharge in a tank, increase the fermentation efficiency, a device can effective save the fermentation raw material, further reducing cost, the utility model is new type has simple structure and easy operation.
NOVELTY - The utility model claims a novel vertical anaerobic fermentation tank, belonging to a device, the device comprising: a tank body, a stirring shaft, paddle stirrer, baffle plate, a discharging mouth, heating coil, push type stirrer, a feeding port, an exhaust port, a driving device, set with a fermentation tank upper part and at a stirrer is paddle stirrer, with strong cutting a cause and a dispersing of biogas straw raw material is full mixing effect, and prevent a crust, installation to avoid a material, and a tank lower part and lower layer stirrer is type stirrer at a part of wall in the tank body baffle plate, cutting force weak and would not damage a fungus, stirring consume low power, and set with a diameter of tank body than is good for further reducing stirring consume large power, a more uniform stirring, carrying out the reaction is more complete, the utility model is new type structure is simple, the cost is low, and operation suitable and wide applicability.
NOVELTY - The utility model claims a novel push type stirring and filtering type fermentation tank, belonging to a device, the device comprises the tank body, a feeding port, a drive device, a stirring, a filtering device, a heating coil pipe, an exhaust port, a push type stirring leaf form axial force cutting effect is small, which avoids the damage to a fungus, paddle stirring leaves forming a radial force, with strong cutting effect, large particle diameter solid object of dispersing and a biogas slurry and full mixing, make a process completely, at the same time the crust material; the tank body equipped with a discharging port, a double in a tank of the biogas and slag discharge, increase fermentation efficiency, a device can save a raw material, further reducing cost, set with diameter longer than the tank body large, which is good for further reducing stirring consume power, a more uniform stirring, carrying out the reaction is more complete, the utility new type has simple structure, suitable operation, which is good for popularization.
NOVELTY - Preparing and separating biopolymers and biopolymer fractions from sewage sludge comprises (a) disrupting the bacterial cell walls of bacteria present in the sewage sludge by greater than or equal to 75% to release the intracellular contents of the bacterial cells; and (b) separating the biopolymers from any contaminants present.    USE - The method is used for preparing and separating biopolymers and biopolymer fractions from sewage sludge. The DNA or peptidoglycan isolated using the method above is use as flocculants and coagulants (all claimed).    ADVANTAGE - Provided is a new and improved method for the preparation and separation of biopolymers and biopolymer fractions from sewage sludge which is both effective and efficient and which may be applied to wastewater treatment applications. The method is suitable for large scale industrial biopolymer production in quantities commensurate with the operation of a municipal sewage treatment works and thus provides an answer to the problem of how to manage the ever increasing problem of sewage waste.Provided is a new and improved method for the preparation and separation of biopolymers and biopolymer fractions from sewage sludge which is both effective and efficient and which may be applied to wastewater treatment applications. The method is suitable for large scale industrial biopolymer production in quantities commensurate with the operation of a municipal sewage treatment works and thus provides an answer to the problem of how to manage the ever increasing problem of sewage waste.
NOVELTY - The system has a waste heat supply line to supply waste heat generated from a fuel cell unit. A solar energy generation unit produces electricity using radiant heat energy of sun. The fuel cell unit converts chemical energy generated in the oxidation process of hydrocarbon fuel into direct electric power with electrochemical reaction and produces electricity to the solar energy generation unit. An air supplying part supplies air to a fuel cell stack and produces electricity from the solar energy generation unit using a heat-receiving section.    USE - Renewable energy hybrid power system.    ADVANTAGE - The system degrades generated energy with waste heat of the fuel cell unit so as to continuously to generate develop power after sunset by using waste heat of the high temperature generated in the fuel cell unit, thus improving power generation efficiency and providing stable power generation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a renewable energy hybrid power system.
NOVELTY - Processing organic garbage includes injecting garbage in container (10) under stirring condition. Grass chips are introduced to form lowermost grass-chip layer (12) in container. Rice bran is mixed with fermentation bacteria, and bamboo powder is fermented on grass-chip layer by lactic acid bacteria. Fermentation layer (13) is mixed to obtain fermented material.    USE - Method for processing organic garbage (claimed).    ADVANTAGE - The method ensures easy and reliable treatment of organic garbage, and removal of unnecessary moisture from garbage. The method requires simple device that is implemented easily in home.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of organic garbage processor.    Container (10)    Container lid (11)    Grass-chip layer (12)    Fermentation layer (13)    Plastic sheet (17)
NOVELTY - An armillarisin injection comprises 0.005 weight/volume% armillarisin and 5 weight/volume% glucose.    USE - Armillarisin injection (claimed).    ADVANTAGE - The environmentally-friendly armillarisin intravenous injection has excellent storage stability and suppressed precipitation for long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of armillarisin injection.
NOVELTY - A microorganism sludge treatment method comprises taking dehydrated sludge, heating at 100-130 degrees C for 2-5 hours, adding lysogeny broth culture medium, seeding 1:1000-1100 mass ratio of microorganisms, adding 1-5 wt.% nutrient liquid, fermenting at 50-65 degrees C for 5-7 days.    USE - Microorganism sludge treatment method used for organic fertilizer production (claimed).    ADVANTAGE - The method promotes efficient aerobic fermentation.
NOVELTY - Preparation of organic fertilizer for rapeseed comprises taking 15-25 pts. wt. rapeseed powder, 12-17 pts. wt. rapeseed straw, 21-33 pts. wt. peanut vine, 13-21 pts. wt. soybean straw, 12-17 pts. wt. traditional Chinese medicine slag, 15-25 pts. wt. mushroom waste and 4-12 pts. wt. saccharide, fermenting at 55-65 degrees C for 24-48 hours, adding 7-13 pts. wt. medical stone, 12-17 pts. wt. feather dust and 12-17 pts. wt. bone powder, stirring, adding 0.1-0.5 pt. wt. composite microbial inoculum, fermenting at 38-45 degrees C for 24-48hours, drying, crushing and granulating at 2-8 mm particle diameter.    USE - Method for preparing organic fertilizer for rapeseed (claimed).    ADVANTAGE - The fertilizer is rich in nutrients and increases yield of rapeseed.
NOVELTY - A prilocaine hydrochloride is prepared by taking o-toluidine and methylene chloride, adding alpha -propionyl chloride, reacting at 15-25 degrees C for 2-3 hours, washing with acid and alkali solution, taking organic layer, adding water, filtering, adding propylamine, heating and refluxing for 5-7 hours, adding concentrated hydrochloric acid, adjusting pH to 1-2, filtering, adding 95 wt.% ethanol, and purifying.    USE - Method for preparing prilocaine hydrochloride (claimed).    ADVANTAGE - The method is nontoxic and environment-friendly.
NOVELTY - Preparing multi-layered metal hydroxide involves stirring heavy metal waste water containing cobalt, nickel and copper, and then adding sodium hydroxide to obtain mixture. The mixture is heated at 80 degrees C for 16-24 hours and then washed with deionized water at 60 degrees C. The mixture is dried to obtain the product. Methane bacteria are added into a culture medium and then multi-layered metal hydroxide is added into a culture medium. The culture medium comprises glucose, ammonium sulfate, dipotassium phosphate, monopotassium phosphate and water.    USE - Method for preparing multi-layered metal hydroxide used for promoting growth of methane bacteria for treating organic waste water under anaerobic biological process(claimed).    ADVANTAGE - The method enables to improve growth of methane bacteria by 15%.    DETAILED DESCRIPTION - Preparing multi-layered metal hydroxide involves stirring heavy metal waste water containing cobalt, nickel and copper, and then adding sodium hydroxide to obtain mixture. The mixture is heated at 80 degrees C for 16-24 hours and then washed with deionized water at 60 degrees C. The mixture is dried to obtain the product. Methane bacteria are added into a culture medium and then multi-layered metal hydroxide is added into a culture medium. The culture medium comprises glucose, ammonium sulfate, dipotassium phosphate, monopotassium phosphate and water. The culture medium is sterilized at 121 degrees C for 20 minutes.
NOVELTY - The new type utility claims a structure suitable for straw powder suspension liquid continuous fermentation tank feeding and discharging, which belongs to engineering field, the device comprises a tank body, a jacket, a water inlet, a water outlet, a tank feeding port, a discharging a tank, a tank wherein sampling. Comprising: a jacket water inlet set on the tank body side wall lower end, a water outlet set on the tank body side wall upper end of the fermentation tank a feedstock formed close to the tank bottom in the tank body side wall, a discharge formed in the tank body 3/5 of height a, sampling a set with a tank body 2/5 and a height, a feeding port, a discharging and sampling with a connect tank body internal steel pipe, the steel pipe protruding jacket 20 mm, a 55 degrees conical pipe outside screw thread structure. The utility model is new type reducing energy consume, shortens a feedstock, reducing production cost, a timing check and a, outside screw thread and a pipe diameter of inlet steel pipe combined transformer, change diameter and it is suitable for a continuous fermentation is different form the culture medium.
NOVELTY - One of tobacco hard tissue low temperature grinding device, comprising grinding tank, grinding pestle and upper cover, wherein the grinding tank is from and installed with the cold type cold accumulation groove tank and put in cold accumulation groove seat of the grinding tank liner composed of, formed with rubber pad at bottom of tank type cold accumulation groove tank. This new utility model the beneficial effect is: can be tobacco hard tissue sample to complete the grinding operation under low temperature condition, small volume, suitable operation, no safety hidden danger, low cost and change liner is very suitable, can carry out continuous grinding operation for the whole multi-sample, which avoids of continuous grinding is easy to generate the sample mutually pollute problem, no failure is grinding tool of biology sample laboratory one is necessary.
NOVELTY - Production (100) of bio oil involves providing (102) lignin, providing (104) lignocellulosic biomass, and pyrolyzing (106) the lignin and the lignocellulosic biomass.    USE - Production of pyrolytic bio oil used as renewable sources of energy of boilers, furnaces and engines, and chemical precursors.    ADVANTAGE - The method enables production of pyrolytic bio oil having excellent quality, pH value, viscosity, cold flow property and energy content.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of production of pyrolytic bio oil.    Production process (100)    Provision of lignin (102)    Provision of lignocellulosic biomass (104)    Pyrolization process (106)
NOVELTY - A methane gas generating amount is increased by collecting pig manure fermentation raw liquid, placing in water collecting pool, weighing 1-9 mg ferric trichloride hexahydrate, 0.1-1.5 mg cobalt chloride hexahydrate, 0.2-3 mg nickel chloride hexahydrate, and 150-250 mg yeast extract, adding additive in water to obtain 1% aqueous additive solution, adding to water collecting pool, controlling carbon and nitrogen content in raw liquid to 20-35:1 and solid concentration at 6-15%, pumping raw liquid in methane gas fermentation tank, and fermenting at normal temperature to collect methane gas.    USE - Increase of methane gas generating amount.    ADVANTAGE - The process increases gas production rate and yield, provides good activity environment, and is safe and environment-friendly.    DETAILED DESCRIPTION - A methane gas generating amount is increased by collecting pig manure fermentation raw liquid, placing in water collecting pool, weighing 1-9 mg ferric trichloride hexahydrate, 0.1-1.5 mg cobalt chloride hexahydrate, 0.2-3 mg nickel chloride hexahydrate, and 150-250 mg yeast extract in which amount of each additive is according to 1 L fermentation raw liquid, adding additive in water to obtain 1% aqueous additive solution, adding to water collecting pool, controlling carbon and nitrogen content in raw liquid to 20-35:1 and solid concentration at 6-15%, pumping raw liquid in methane gas fermentation tank, and fermenting at normal temperature for 15 days to collect methane gas.
NOVELTY - Method for producing butanol, involves (a) cleaning cassava and crushing cassava, performing catalyst reaction using solvent, removing solvent, and drying processed mixture, and (b) inoculating strain to mixture, fermenting mixture, performing distillation to obtain crude butanol, and extracting mixture to obtain butanol.    USE - The method is useful for producing butanol, which is used as fuel.
NOVELTY - Method for preparing biodiesel, involves (a) coculturing hydrogen producing algae and oil producing algae in medium, (b) inducing hydrogen and oil production, collecting oil and hydrogen, and performing purity analysis for hydrogen and quantitative analysis for oil, and (c) subjecting the obtained oil to direct hydrogenation using the obtained hydrogen.    USE - The method is useful for preparing biodiesel (claimed).    ADVANTAGE - The method prepares biodiesel which has excellent quality, is cost-effective, consumes minimal energy, and does not require any additional agent.
NOVELTY - Method for extracting lipids from population of microorganisms, involves contacting the population of microorganisms with one or more enzymes under conditions that cause disruption of the microorganisms, where the contacting is performed in the absence of surfactant, and extracting lipids from the disrupted microorganisms in the presence of reduced amounts of organic solvent or in the absence of organic solvent.    USE - The method is useful for extracting lipids from population of microorganisms (claimed), which is useful as nutritional oils and/or lipid biofuels.    ADVANTAGE - The method is cost-effective, and saves energy.
NOVELTY - Manufacture of ( alpha ),( beta )-unsaturated carbonyl compound involves reacting allyl alcohol and hydrogen peroxide using picolinic acid chosen from 2-picoline acid and 2-picoline acid of 6-1-4C alkyl in ratio of 1:1-1:4, and iron(II) or iron(III) salt soluble in water or an organic solvent as a reaction catalyst, and carbonylating an alcohol site.    USE - Manufacture of (alpha),(beta)-unsaturated carbonyl compound e.g. (alpha),(beta)-unsaturated aldehyde and (alpha),(beta)-unsaturated ketone (all claimed). Uses include but are not limited to manufacturing polymer, pharmaceuticals, fragrance and sweetener.    ADVANTAGE - The method enables environmentally-friendly, efficient and economical manufacture of (alpha),(beta)-unsaturated carbonyl compound by a safe process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for catalyst used for reaction of allyl alcohol and hydrogen peroxide, which comprises a complex of formula (I) or (II).
NOVELTY - A fertilizer composition comprises 5-7 pts. wt. fermentation filtrate, 0.5-1 pt. wt. photosynthetic bacteria, 2-3 pts. wt. lactic acid bacteria, 0.5 pt. wt. calcium superphosphate and 0.5 pt. wt. molasses.    USE - Fertilizer composition (claimed).    ADVANTAGE - The fertilizer composition provides fast and durable effect, promotes growth of beneficial algae, promotes farming animal growth when absorbed by animals, utilizes waste material e.g. molasses and fermentation filtrate, and can be prepared by cost-effective and simple method in large scale.
NOVELTY - Organic fertilizer comprises 3-5 pts. wt. nutrient liquid, 20-25 pts. wt. organic composite raw material, 70-75 pts. wt. water medium and 3-5 pts. wt. antimanganese composite microorganism microbial inoculum.    USE - Organic fertilizer used for repairing manganese ore polluted soil (claimed).    ADVANTAGE - The fertilizer reduces root heavy metal toxicity, increases survival rate of plant, promotes plant growth, relieves plant rhizosphere soil manganese element, and strengthens plant repairing ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of organic fertilizer comprising mixing nutrient liquid, organic composite raw material and water medium, adding antimanganese composite microorganism microbial inoculum, and fermenting at 30 degrees C for 15 days.
NOVELTY - Modification of solid fuel (d) involves contacting the solid fuel having moisture content with a dry vaporization gas (a) obtained by vaporizing liquefied natural gas, supplying an exhaust heat from heating apparatus (3), obtaining a moisturized vaporization gas (b) containing absorbed moisture, performing heat exchange of moisturized vaporization gas with liquefied natural gas, vaporizing the liquefied natural gas, separating fuel gas (c) and water by dehumidifying the moisturized vaporization gas, burning fuel gas using the heating apparatus, and obtaining exhaust heat.    USE - Modification of solid fuel e.g. wood coal (claimed), lignite, sub-bituminous coal, peat, and biomass-type recycle solid fuel.    ADVANTAGE - The method enables efficient modification of solid fuel, by simple and economical process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid fuel modifier, which consists of liquefied natural gas vaporizer (2), drying apparatus (1), heating apparatus, heat exchange unit (21), dry vaporization gas path (L2), solid fuel supply unit (13), dry vaporization gas supply unit, solid fuel exhaust passage (L8), fuel gas path (L4), drainage channel (L5), and combustion unit (31).    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of solid fuel modifier. (Drawing includes non-English language text)    Drying apparatus (1)    Liquefied natural gas vaporizer (2)    Heating apparatus (3)    Solid fuel supply unit (13)    Heat exchange unit (21)    Combustion unit (31)    Dry vaporization gas path (L2)    Fuel gas path (L4)    Drainage channel (L5)    Solid fuel exhaust passage (L8)    Dry vaporization gas (a)    Moisturized vaporization gas (b)    Fuel gas (c)    Solid fuel (d)
NOVELTY - An articaine hydrochloride preparation involves taking sodium methoxide, adding methyl thioglycolate, cooling to 3-5 degrees C, adding alpha -methacrylonitrile, reacting for 6-8 hours, adding concentrated hydrochloric acid, adjusting pH to 3-5, adding methanol, concentrating, precipitating, adding alkali solution and dichloromethane, cooling to 2-6 degrees C, adding alpha -propionyl chloride, reacting for 2 hours, standing, taking organic layer, drying with sodium sulfate, filtering, cooling to 3-8 degrees C, adding n-propylamine, refluxing for 2 hours, and adding 2 wt.% sodium bicarbonate aqueous solution.    USE - Articaine hydrochloride preparation method (claimed).    ADVANTAGE - The method is environment-friendly and suitable for industrialization.    DETAILED DESCRIPTION - An articaine hydrochloride preparation comprises taking sodium methoxide, adding methyl thioglycolate, cooling to 3-5 degrees C, adding alpha -methacrylonitrile, reacting for 6-8 hours, adding concentrated hydrochloric acid, adjusting pH to 3-5, adding methanol, concentrating, precipitating, adding alkali solution and dichloromethane, cooling to 2-6 degrees C, adding alpha -propionyl chloride, reacting for 2 hours, standing, taking organic layer, drying with sodium sulfate, filtering, cooling to 3-8 degrees C, adding n-propylamine, refluxing for 2 hours, adding 2 wt.% sodium bicarbonate aqueous solution, standing, taking organic layer, drying with sodium sulfate, filtering, concentrating, dissolving in ethanol, adding concentrated hydrochloric acid, adjusting pH to 3-4, cooling to 3-5 degrees C, and precipitating.
NOVELTY - Preparation of epigallocatechin gallate involves mixing green tea and distilled water, heating to 60-80 degrees C, obtaining green tea extract, absorbing using hydrogen-bonding-adsorption-type macroporous resin, eluting using 10-20% aqueous ethanol and 30% aqueous ethanol, concentrating the resultant eluate, freeze-drying and recrystallizing.    USE - Preparation of epigallocatechin gallate (claimed).    ADVANTAGE - The method efficiently provides epigallocatechin gallate with high purity, by economical and environmentally-friendly process. The hydrogen-bonding-adsorption-type macroporous resin used in the method has excellent recyclability.
NOVELTY - The system has a standardized compressed gas tank equipped with a system gas pressure regulator with a working standard low. A first stage gas compressor (17) and a second stage gas compressor (22) are connected with an intermediate gas tank (21). A third stage gas compressor (26) and a high pressure gas storage tank (27) are equipped with an intermediate pressure reducer (28) and connected to pipelines. Control valves are equipped with control and measuring device.    USE - System for conservative acceptance, standardization and storage of gas obtained in low-pressure pyrolisis installations such as rubber waste and biomass gasification.    DESCRIPTION OF DRAWING(S) - The drawing shows sectional view and schematic views of a system for conservative acceptance, standardization and storage of gas obtained in low-pressure pyrolisis installations.    Stage gas compressors (17, 22, 26)    Intermediate gas tank (21)    High pressure gas storage tank (27)    Intermediate pressure reducer (28)
NOVELTY - Probiotics composition comprises 106 colony forming units (cfu)/ml Lactobacillus alimentarius, 106 cfu/ml L.fructivorans, 106 cfu/ml L.buchneri, 105 cfu/ml Bacillus pumilus, 105 cfu/ml B.polymyxa, and 105 cfu/ml B.coagulans.    USE - The probiotics composition is useful for processing straw (claimed) for producing silage which is used for livestock production.    ADVANTAGE - The probiotics composition enables to produce silage having improved quality and aerobic stability, reduced pH, protein degradation and weight loss during fermentation process, and slow decaying rate in an open pit, and hence is highly significant for livestock production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation method of the above-mentioned probiotics composition, which involves (a) identifying the above-mentioned Lactobacillus sp. from silage fermentation system, and obtaining mixed culture of identified Lactobacillus sp., (b) filtering cells from the mixed culture, inoculating filtered cells on inclined surface of slant culture medium containing skim milk, activating cells at 37 degrees C, inoculating a loop of liquid culture in BLB culture medium, performing shaking culture at 37 degrees C and 150 revolutions per minute (rpm) for 24 hours, inoculating 10% corresponding liquid culture inoculum in an anaerobic reactor, and incubating culture medium for 24 hours, (c) obtaining mixed culture of B.pumilus, B.polymyxa and B.coagulans, (d) screening resulting cells, filtering cells, activating filtered cells in inorganic salt based medium at 30 degrees C, inoculating a loop of cells in liquid culture medium, performing shaking culture at 30 degrees C and 150 rpm for 24 hours, inoculating 10% corresponding liquid culture inoculum in an anaerobic reactor, and incubating culture medium for 24 hours, and (e) mixing bacterial cultures obtained in the steps (b) and (d), and inoculating 1 l probiotics composition per 1 ton of straw.
NOVELTY - A 2,2'-dibenzoyl-diaminodiphenyl disulfide is prepared by performing step (1) of adding sulfide and o-halobenzene in solvent, adding alkaline solution, adding oxidizing agent after reaction completion, separating solid product, and obtaining 2,2'-diphenylamine disulfide and performing step (2) of subjecting 2,2'-diphenylamine disulfide and benzoyl chloride to acylation reaction and obtaining product.    USE - Preparation of 2,2'-dibenzoyl-diaminodiphenyl disulfide (claimed).    ADVANTAGE - The preparation process is short, inexpensive, and simple, generates small amount of waste, produces product in high yield, and uses simple equipment.
NOVELTY - Organic fertilizer is prepared by (a) using sisal waste residue, microbial strain, mud, urea, potassium sulfate, diammonium phosphate and alcohol residue, (b) filtering sisal waste, adding microbial strain to filtrate, adding mud, urea, potassium sulfate and diammonium phosphate, and performing fermentation, (c) controlling temperature of fermentation at 50-60 degrees C for 8-20 hours to obtain fermented product, and (d) drying and crushing fermented product, adding crushed product to alcohol residue, mixing materials, and granulating mixture.    USE - As organic fertilizer for rice (claimed). The organic fertilizer is useful for improving soil quality.    ADVANTAGE - The organic fertilizer increases yield and quality of crop, and reduces environmental pollution.    DETAILED DESCRIPTION - Organic fertilizer is prepared by (a) using 100-200 pts. wt. sisal waste residue, 5-7 pts. wt. microbial strain, 10-20 pts. wt. mud, 3-5 pts. wt. urea, 2-4 pts. wt. potassium sulfate, 10-30 pts. wt. diammonium phosphate and 10-20 pts. wt. alcohol residue, (b) filtering sisal waste, adding the microbial strain to filtrate, then adding mud, urea, potassium sulfate and diammonium phosphate, and performing fermentation, (c) controlling temperature of fermentation at 50-60 degrees C for 8-20 hours to obtain fermented product, (d) drying and crushing the fermented product, adding crushed product to alcohol residue, mixing materials, and granulating mixture, and (e) detecting quality of granules, and packing qualified granules.
NOVELTY - The utility model is new type relates to biomass energy use field, specifically a rice hull. decomposing the spray cooling device after gasification, a rice hull. decomposing the spray cooling device after gasification, comprising pyrogenation, oxidation, reduction, wherein the lower part of the regenerator formed oxidation below the oxidation zone formed with the reducing area, a reducing area connected with sum solid-liquid separating chamber, a sum solid-liquid separation chamber A side is connected with air outlet pipe; the solid liquid separation chamber below the sum with a solid-liquid collecting clined surface, a liquid collecting clined surface is fixedly connected with the lower part solid-liquid outlet, the sum solid liquid separation chamber side set with spray shower nozzle. The utility model is new type of goal is providing a rice hull resolve after gasification of a spray cooling device, a rice hull heat decomposing gasification can be a mixture of a sum solid-liquid separating, at the same time to separate the opened a combustion gas for primary purification, also can prevent the separation from the solid and liquid substance to mix together.
NOVELTY - Strain of green microalga Acutodesmus obliquus Syko-A Ch-055-12 with the ability to reduce the content of polluting substances in sewage is deposited in the Collection of Microseaweed of IPPAS under the registration number IPPAS S-2016. The strain of green microalga Acutodesmus obliquus IPPAS S-2016 can be used for cleaning of waste treatment facilities of municipal services and the pulp-and-paper enterprise from polluting substances (ammonium nitrogen, suspended substances, iron) at high temperatures.    USE - Biotechnologies.    ADVANTAGE - Improvement of strain properties.1 dwg, 2 ex
NOVELTY - The apparatus (1) has a container that is positioned at an upper portion and configured to store water. A hydrogen generating unit is positioned at a lower portion of the container, and configured to dissolve hydrogen generated by electrolyzing the water stored in the container water in the water stored in the container, and convert the water in the container into hydrogen water. A power supply unit applies power to the hydrogen generating unit.    USE - Portable apparatus for producing hydrogen water.    ADVANTAGE - The apparatus for producing hydrogen water includes the battery embedded inside the case, so that apparatus is independently operated without depending on an external power supply. The apparatus for producing hydrogen water has a small structure of generating hydrogen by the electrode unit embedded inside the case, in order to achieve very excellent portability and use convenience. The internal pressure of the container is increased while the hydrogen enters the container, but gas forming the increased internal pressure is discharged to the outside of the container through the thin film of the cap, so that the internal pressure applied inside the container naturally decreases, in order to prevent a leakage phenomenon inside and outside the container.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the portable apparatus for producing hydrogen water.    Portable apparatus for producing hydrogen water (1)    Case (10)    Insertion opening (20)    Switch (30)    Display unit (40)
NOVELTY - The apparatus has electrodes provided in a first compartment such that the electrodes pass through an interface between a side of a diaphragm and a facing edge of a first hemi-enclosure (110). A first pipe allows gas within a second compartment to escape. A second pipe allows gas within the first compartment to escape. A fastener fastens a second hemi-enclosure (105), the diaphragm the electrodes and the first hemi-enclosure together, where electrical contacts receive energy from an external source and deliver the energy to the electrodes.    USE - Electrolysis apparatus for splitting water into hydrogen and oxygen gases in a hydrogen and oxygen production apparatus (claimed) utilized in petroleum refining field, fertilizer production field and glass manufacturing field.    ADVANTAGE - The apparatus comprises an electrical conductor passing from outside to inside of the second fluid-tight compartment in a leak tight manner and in electrical contact with the electrodes in the first compartment. The apparatus maintains equal pressures in the first and second compartments, so that purity of the hydrogen and oxygen gases produced can be improved. The apparatus recovers expended energy from kinetic energy and momentum of the hydrogen and oxygen gases that are flowing in gas removal pipes, thus improving the efficiency of the electrolysis.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an electrolyzer apparatus comprising remotely controlled pressure regulators.    Hemi-enclosures (105, 110)    Top plates (114, 115)    Remotely controlled pressure regulators (120, 125)
NOVELTY - The gasifier (100) has a pyroreactor (200) whose first end (250) defines a biomass inlet and second end (260) defines a pyroreactor outlet (220). A reduction basket is arranged proximal to the pyroreactor outlet, where the reduction basket comprises a basket opening opposing a closed end (310) of the reduction basket. A set of air manifolds (400) is fluidly connected to an interior lumen (214) of the pyroreactor through a set of air inlets (270) arranged between the ends. A gasifier housing (500) encloses the pyroreactor, reduction basket, and air manifolds within a housing lumen (510).    USE - Downdraft gasifier for receiving biomass in bulk.    ADVANTAGE - The gasifier allows a char to additionally fall out top of the reduction container when reduction container volume is exceeded such that excessive char buildup is prevented. The gasifier allows the reduction container including a predefined height and arranged a predetermined distance away from the pyroreactor such that a gap is defined between the reduction container walls and the pyroreactor body and gap enables the char that rises above the reduction container height to spill out of the reduction container, so that the char does not build up and rise into the first gas manifold section, thus preventing char accumulation and packing by predefining the height of the reduction bed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gasification system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a variation of a downdraft gasification system.    Downdraft gasifier (100)    Pyroreactor (200)    Interior lumen (214)    Pyroreactor outlet (220)    Ends of pyroreactor (250, 260)    Air inlets (270)    Closed end (310)    Air manifolds (400)    Gasifier housing (500)    Housing lumen (510)
NOVELTY - Heat transfer pipe (1) comprises an inner layer (2) contacting with a medium, and a diffusion barrier layer (3) for preventing permeation of molecules of a substrate into the medium. The diffusion barrier layer comprises ethylene-vinyl alcohol or ethylene vinyl alcohol, and has ethylene content of greater than 32%. The heat transfer pipe transfers heat between a medium flowing in the heat transfer pipe and the substrate at least partially surrounding the heat transfer pipe.    USE - The heat transfer pipe is useful for a biogas plant fermenter (claimed).    ADVANTAGE - The heat transfer pipe can be connected in easy and quick manner, and transfers heat in accurate manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biogas plant fermenter comprising the above heat transfer pipe, and substrate at least partially surrounding the heat transfer pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the heat transfer pipe (Drawing includes non-English language text).    Heat transfer pipe (1)    Inner layer (2)    Diffusion barrier layer (3)    Adhesive layer (4)    Outer protective layer (12)
NOVELTY - The detector has a detection unit that detects a to-be-detected gas. A main-case portion is provided to incorporate detection unit. A lamp portion is light-emitted when provided in main-case portion and detection unit detects to-be-detected gas. A nozzle portion is formed at a front-end, and connected to a main-case portion so that a gas introduction port introduces a detection target gas into the detection unit. A light-emitting unit is provided in the nozzle portion so as to emit light based on the detection result of detection unit.    USE - Portable gas detector for detecting gases such as combustible gas such as methane, carbon monoxide, hydrogen sulfide, and smell and poisonous gas.    ADVANTAGE - The nozzle portion is formed at a front-end, and connected to a main-case portion so that the gas introduction port introduces a detection target gas into the detection unit and the light-emitting unit is provided in the nozzle portion without positioning in the main-case portion gripped with fingers at the time of use so as to emit light based on the detection result of detection unit. Thus, the to-be-detected gas is detected and recognized reliably and visually by user irrespective of the time of non-driving at the time of drive of illumination unit by varying the light emission mode of light-emitting unit in the time of drive of illumination unit, and non-driving.
NOVELTY - Recovery of coal from waste involves subjecting the waste to physical and chemical reactions, processing in powder machine, separating coal and shaping resultant product to predetermined shape.    USE - Recovery of coal from waste (claimed).    ADVANTAGE - The method enables recovery of coal from waste by simple, economical and environmentally-friendly process. The recovered coal has high quality.
NOVELTY - The system has a methyl alcohol water storage container for storing water raw material methyl alcohol while driving a conveying pump. A conveying pipeline conveys the methyl alcohol to a methanol hydrogen production system for generating reforming reaction prepared hydrogen. A hydrogen gas supply generates electrochemical reaction producing electric energy to a fuel cell. A heat pump device is connected with a water circulation cooling system for absorbing warm water and heat into a high warm heat source and the conveying pump in the methyl alcohol raw material heating water.    USE - Methyl alcohol water hydrogen generation system.    ADVANTAGE - The system has high reliability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a methyl alcohol water hydrogen generation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a methyl alcohol water hydrogen generation system. '(Drawing includes non-English language text)'
NOVELTY - A porous material supported nano alloy catalyst comprises supercritical carbon dioxide as fluid medium, metal compound as precursor, porous material as carrier, borane-based substance as reducing agent, and binary or multi-element nano alloy particles as nano alloy. Nano alloy has particle size of 1-2 nm. Nano alloy particles are distributed on surface and pores of the porous material.    USE - Porous material supported nano alloy catalyst is used for preparing supercapacitor, fuel cell catalyst, lithium battery, dye battery, photodegradation catalyst, hydrogen, oxygen catalyst, hydrogenation reaction catalyst, hydrogen storage material, Raman reinforced matrix, biomaterials, optical material, plastic composite and antimicrobial material (all claimed).    ADVANTAGE - The porous material supported nano alloy catalyst has excellent activity and stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of porous material supported nano alloy catalyst.
NOVELTY - The utility model is new type of design for the Anaerobic fermentation biogas slurry is of a CO2 absorption and storage using system, a three-way valve pipeline, biogas liquid conveying pump carbon, carbon-rich biogas liquid mixture storage device, regeneration carbon-rich biogas liquid conveying pump, lean and fat heat exchanger, biogas liquid carbon CO2 regeneration device, a pipe in turn connected the fresh biogas slurry storage device, a device, concentration equipment, mixing equipment, heater, CO2 absorption device. The utility model is new type. Anaerobic fermentation of organic matter and low production cost, weak alkaline, and rich in plant nutrition component and a biogas slurry is medium, a CO2-rich gas and CO2 absorption and storage application is integrated, taking CO2 from gas transfer to plant body or soil and water layer and greatly reduce the CO2 absorption and storage using cost, realize a CO2 absorption and storage using cost is low.
NOVELTY - Preparing biofertilizer involves performing solid state fermentation of enzymes and plant nutrients. Enzymes are subjected to immobilization and then nanoparticle of allophones are added to carry out fermentation in presence of microorganisms.    USE - Process for preparing biofertilizer used for growth, height, performance and development of plants (all claimed).    ADVANTAGE - The process enables to prepare biofertilizer that improves quality of biofertilizer through development of microorganisms.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biofertilizer composition, which comprises biofertilizer encapsulated enzymes, enzyme-nanoparticle aggregates mainly phosphatases, sulfatases, asparaginase or glutaminases, encapsulated organic substrates, plants growth hormone, fulvic acid and humic acid, organic molecules and beneficial microorganisms to plant.
NOVELTY - The water electrolyzer (100) has a stack of electrode plates (101) that are arranged in alternate polarities. The electrode plates are separated by dividers and arranged between two end plates (107,108) in which one of the end plates is an anode terminal and the other is a cathode terminal. The stack of plates is provided with a hollow center portion for electricity connection. The apertures (113,114) are formed around the hollow center for forming channels for distribution of electrolyte and collection of electrolytic products.    USE - Water electrolyzer for producing hydrogen gas for hydrogen refueling system for vehicle.    ADVANTAGE - The demister eliminates liquid vapor to obtain pure gas with approximately zero humidity, so the remaining oxygen atom in the output gas is removed in deoxidizer to ensure high purity of hydrogen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the water electrolyzer.    Water electrolyzer (100)    Electrode plates (101)    End plates (107,108)    Apertures (113,114)    Electrode connection (120)
NOVELTY - A redox catalyst comprises an oxygen carrying material, a mixed ionic-electronic conductive (MIEC) support, and a catalytically-active surface.    USE - Redox catalyst for use as core-shell redox catalyst and mixed-conductive redox catalyst for converting biomass to syngas, for generating syngas from methane (all claimed), and for cyclic redox conversion of commodity fuels such as natural gas, coal and biomass into value-added, environmentally friendly products such as hydrogen, synthesis gas, electricity, and other chemicals or fuels, oxidation of syngas into carbon dioxide and splitting of water to form hydrogen.    ADVANTAGE - The redox catalyst has better thermal stability, better mechanical strength, increased resistance to agglomeration, improved reactivity, selectivity, recycleability, structural and chemical stability, tunable thermodynamic properties and/or redox activity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a core-shell redox catalyst    (2) a mixed-conductive redox catalyst    (3) method for converting biomass to syngas    (4) a method for generating syngas from methane.
NOVELTY - Method for exterminating insect produced from fermentation processed materials such as an organic refuse in fermentation, and livestock dung, involves covering surface of fermentation processed material containing a container with burnt ashes as layer, and allowing burnt ashes to stand for predetermined period.    USE - The method is useful for exterminating insect produced from fermentation processed materials such as an organic refuse in fermentation, and livestock dung (claimed).    ADVANTAGE - The method is simple and convenient to perform at home, and reduces pollution.
NOVELTY - Converting hydrogen and carbon dioxide into methane by culturing methanogenic microorganisms in a reaction vessel by contacting the methanogenic microorganisms with an in-gas comprising hydrogen and carbon dioxide.    USE - The method is used for converting hydrogen and carbon dioxide into methane.    ADVANTAGE - Provided is a high yielding methane production process by the culture of Methanobacterium subterraneum or any other methanogenic bacterium having the same physiological growth properties, under particular conditions and a high gas transfer velocity. The process involves the cultivation of the above bacteria continuously within a controlled culture medium and a high transfer rate of gas. In this way, by ensuring a high gas transfer velocity the efficiency of the methane production is maintained.
NOVELTY - Method for producing a sugar solution from cellulose-containing biomass involves (a) hydrolyzing cellulose-containing biomass using filamentous fungi derived cellulase, and (b) filtering the obtained hydrolyzate through an ultrafiltration membrane to recover the filamentous fungi derived cellulase as a non-permeate, and sugar solution as permeate, where the cellulose-containing biomass is processed by at least one enzyme chosen from pectinase, glucoamylase, and lipase.    USE - The method is useful for producing sugar solution (claimed), which is useful as fermentation raw material for producing various chemical products.    ADVANTAGE - The method improves quantity of saccharogenic amylase recovered.
NOVELTY - Enzymatic process for reducing carbon dioxide to methanol comprises: (a) exposing carbon dioxide to at least one formate dehydrogenase (FDH) enzyme; and (b) exposing formaldehyde produced from carbon dioxide to at least one alcohol dehydrogenase (ADH) or methanol dehydrogenase (MDH) enzyme. The electron donor for reduction of carbon dioxide to formaldehyde is NADH or NADPH and amount of FDH enzyme in (a) is greater than the amount of any formaldehyde dehydrogenase (FaIdDH) and/or aldehyde dehydrogenase (AIdDH) enzyme which is optionally present or FaIdDH and/or AIdDH enzyme is absent in (a).    USE - The process is useful for reducing carbon dioxide to methanol.    ADVANTAGE - The process: is simple and economical; and allows the production of methanol using formate dehydrogenase and alcohol dehydrogenase, instead of three enzymes (formate dehydrogenase, formaldehyde dehydrogenase and aldehyde dehydrogenase).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) use of a FDH enzyme to catalyze reduction of formate to formaldehyde;    (2) use of a dehydrogenase enzyme combination comprising FDH, ADH and/or MDH enzyme, to catalyze reduction of carbon dioxide to methanol;    (3) a matrix comprising the dehydrogenase enzyme combination; and    (4) a kit comprising FDH, ADH and/or MDH enzyme for simultaneous or sequential use in the reduction of carbon dioxide to methanol by the above process.
NOVELTY - A methane production under induced or naturally occurring reducing conditions is inhibited by contacting methanogen with composition comprising red yeast rice which is sufficient to cause inhibition of methane production in which methanogen is resulted into constrainment of biomethylation of heavy metals present in contaminated media.    USE - Inhibition of methane production under induced or naturally occurring reducing conditions for inhibition of methylmetal(loid) production (claimed).    ADVANTAGE - Process reduces nucleophilicity of lone electron pair on arsenic to inhibit reaction, effectively uses naturally-occurring statin, and decreases overall toxicity of site.
NOVELTY - A genetically modified bacterium capable of producing an organic molecule, comprising a heterologous nucleic acid encoding a heterologous enzyme or an enzyme natural to the species of the bacterium, is new. The bacterium is capable of using hydrogen sulfide as an electron donor, carbon dioxide as a carbon source, and nitrate as an electron acceptor. The organic molecule is heterologous or the modified bacterium overproduces the organic molecule compared to the unmodified bacterium.    USE - The genetically modified bacterium is useful for producing an organic molecule. The organic molecule is a methyl ketone or a biofuel (all claimed).    ADVANTAGE - The genetically modified bacterium is produced cost-effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of growing a host cell or bacterium, which involves (a) providing the genetically modified bacterium, and (b) culturing the host cell or bacterium in a liquid comprising hydrogen sulfide and carbon dioxide, and optionally nitrate, where optionally the bacterium produces the organic molecule that the unmodified bacterium does not produce or overproduces the organic molecule when compared to an unmodified host cell or bacterium.
NOVELTY - Producing fermentable sugars from cellulosic biomass comprises providing a feedstock comprising cellulosic biomass; optionally pre-steaming the feedstock; and extracting the feedstock with liquid hot water under effective extraction conditions to produce cellulose-rich solids and an extract liquor containing dissolved solids.    USE - The method is used for producing fermentable sugars from cellulosic biomass.    ADVANTAGE - Provided are improved lignocellulosic biomass processes to economically produce fermentable sugars from both the cellulose and hemicellulose fractions.    DETAILED DESCRIPTION - Producing fermentable sugars from cellulosic biomass comprises (a) providing a feedstock comprising cellulosic biomass; (b) optionally pre-steaming the feedstock; (c) extracting the feedstock with liquid hot water under effective extraction conditions to produce cellulose-rich solids and an extract liquor containing dissolved solids, where the dissolved solids include hemicellulosic oligomers and lignin; (d) washing the cellulose-rich solids to produce a washed cellulose-rich solids stream comprising glucan; (e) hydrolyzing the hemicellulosic oligomers to hemicellulosic monomers by contacting the extract liquor with an acid catalyst or enzymes possessing hemicellulase activity; (f) hydrolyzing the glucan to glucose by contacting the cellulose-rich solids stream with an acid catalyst or enzymes possessing glucanase activity, where step (f) includes removing the glucose in situ by microfiltration and/or ultrafiltration; and (g) recovering, fermenting, and/or further processing each of the hemicellulosic monomers and the glucose, separately or in combination.
NOVELTY - Energy saving exhaust heat involves feeding natural gas desulfurizing and tail gas into hydrogen combustion furnace, heating, entering hydrogenation reaction furnace, generating reduction reaction with catalyst, reducing sulfide and elemental sulfur into hydrogen sulfide, entering entrance of condensing tower, cooling with water, driving into conveying pump, air cooling machine and cooler, entering into recondensing tower, cooling into absorbing refrigerator machine with waste heat or low pressure steam as heat source, entering into cooling tower, and absorbing hydrogen sulfide.    USE - Method for energy saving exhaust heat (claimed).    ADVANTAGE - The method reduces temperature of condensing tower out air, fuel dosage, gas water content and corrosion effect to conveying pipe, increases hydrogen sulfide absorption rate, and improves temperature of gas entering into tail gas burner.    DETAILED DESCRIPTION - Energy saving exhaust heat involves feeding natural gas desulfurizing and tail gas into hydrogen combustion furnace, heating, entering hydrogenation reaction furnace, generating reduction reaction with catalyst, reducing sulfide and elemental sulfur into hydrogen sulfide, entering entrance of condensing tower, cooling with water, driving into conveying pump, air cooling machine and cooler, entering into recondensing tower, cooling into absorbing refrigerator machine with waste heat or low pressure steam as heat source, entering into cooling tower, absorbing hydrogen sulfide with methyl diethanolamine, entering into tail gas burner, forming fume, orderly flowing through waste heat boiler and fume heat exchanger, water heating, discharging, and flowing water into gas preheater.
NOVELTY - Nutritional soil comprises 2-3 pts. wt. humus, 2-3 pts. wt. mud, 1-1.5 pts. wt. burned soil, 2-3 pts. wt. furnace residue and 2-3 pts. wt. rice husk powder. Humus comprises 33 wt.% mushroom residue, 33 wt.% straw, 33 wt.% manure, 0.3 wt.% urea, 0.6 wt.% calcium fertilizer and 0.1 wt.% potassium fertilizer.    USE - Nutritional soil used for plant flower (claimed).    ADVANTAGE - The nutritional soil is prepared in a simple and cost-effective manner, and ensures growth of flower.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing nutritional soil, which involves:    (A) crushing and mixing mushroom residue, straw, manure, urea, calcium fertilizer and potassium fertilizer, and then adding tap water;    (B) stirring the mixture uniformly, and then packaging in a plastic film;    (C) stacking the packed mixture for 32 days and naturally drying for 4 days;    (D) composting the mixture in a vent tube for 12 days, and then crushing and drying it to obtain sludge soil; and    (E) adding and stirring remaining components uniformly with the sludge soil, and then drying for 1 days.
NOVELTY - Nutritional soil comprises 40-50 pts. wt. straw, 40-50 pts. wt. peat, 10-20 pts. wt. microorganism, 20-30 pts. wt. plant ash, 15-20 pts. wt. perlite, 10-15 pts. wt. river sand, 10-15 pts. wt. plant fiber, 30-40 pts. wt. nutrient liquid and 20-40 pts. wt. water retention agent.    USE - Nutritional soil used for Houttuynia cordata (claimed).    ADVANTAGE - The nutritional soil pH is 6-7 and humidity is (50-70%), and has improved ventilation property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing nutritional soil, which involves:    (A) mixing potassium fertilizer, phosphorus fertilizer, nitrogen fertilizer, calcium fertilizer and magnesium fertilizer with water, and stirring uniformly;    (B) adding plant extraction liquid with the mixture, adding crushed straw and microorganism, and then remaining components to carry out fermentation at 50-60 degrees C for 6-8 days to obtain fermented product; and    (C) sterilizing the fermented product at high pressure, adding water retention agent, and then regulating pH value of soil.
NOVELTY - Methanol fuel comprises 75-95 pts. wt. methanol, 3-7 pts. wt. aromatic hydrocarbon, 3-5 pts. wt. methyl tert-butyl ether, 2-6 pts. wt. refined benzene, 0.01-0.4 pt. wt. tetraethyl lead, 0.5-1 pt. wt. octane fuel and 0.1-0.3 pt. wt. anticorrosive agent.    USE - Methanol fuel.    ADVANTAGE - The methanol fuel has simple and convenient operation. It is safe and has good combustion performance.
NOVELTY - Fertilizer comprises 20-70 pts. wt. amino acid, 40-90 pts. wt. urea, 10-30 pts. wt. seaweed, 5-25 pts. wt. rare earth element, 10-20 pts. wt. fermentation residue, 5-20 pts. wt. micro-organism composite, 5-15 pts. wt. chelating agent, 20-70 pts. wt. slow release fertilizer and 10-100 pts. wt. water.    USE - Fertilizer used for planting leafy vegetable (claimed).    ADVANTAGE - The fertilizer ensures absorption of nutrient element, and enhances immunity leafy vegetable and increases yield and quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves;    (A) stirring amino acid, urea and sodium alginate in water at 70-80 degrees C;    (B) mixing chelating agent with obtained mixture to obtain solution;    (C) adding slow release fertilizer and rare earth element to obtain another mixture that is fermented with micro-organism composite to obtain solution;    (D) heating and stirring obtained solutions for 15-20 minutes; and    (E) cooling obtained mixture to room temperature to obtain product.
NOVELTY - Elevation of hydrogen gas in garbage biomass, involves saturating waste biomass to obtain saturated gas, saturating gas with carbon monoxide and water with sulfur tolerant conversion catalyst at 180-480 degrees C to generate hydrogen gas, performing methanation of raw exhaust gas and cooling.    USE - Method for elevating hydrogen gas in garbage biomass.    ADVANTAGE - The method is simple, inexpensive, safe and environmental-friendly.
NOVELTY - The new type utility claims one kind of earthworm ecological filter pool, a filter pool main body, n also comprises solar panel, storage battery and switch, storage battery and solar energy energy plate, a filter chamber body bottom in turn the humus soil layer including earthworm living area, a layer, a guide layer and water collecting area, a humus layer and earthworm living area formed between the first guide has a filter screen, a guide a filter network through lead and switch, a storage battery, a guide and a collecting area set between has a filter screen, a filter on a main body of a water inlet pipe, a water outlet of the water inlet pipe provided with a water distributor, water distributor set with a filter chamber body in the humus soil layer, the bottom filter pool main body has... a. The utility model is new type has simple structure, capacity of organic matter under common effect in earthworm and microorganism, increase the decomposing filter chamber, increase the processing capacity of sewage filter chamber, at the same time a. increase in sewage organic matter and nutrient substance removing rate.
NOVELTY - A biodiesel oil solid alkali catalyst is prepared by taking 100 pts. wt. Chinese medicinal herb waste solid residue and 100 pts. wt. substance A, uniformly stirring, pouring into pulverizer, crushing, adding 100-200 pts. wt. substance A, stirring uniformly, and stand cooling.    USE - Method for preparing biodiesel oil solid alkali catalyst (claimed).    ADVANTAGE - The method has rational process, rich raw material, low cost, wide popularization and application value, and is simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of biodiesel oil solid alkali catalyst comprising taking 100.0 g animal and vegetable oil, 3.0 g biodiesel oil solid alkali catalyst and 30.0 ml methanol, putting into container, heating to reflux, reacting for 1.0-2.0 hours, stirring, heating to remove catalyst, filtering, standing, dividing upper and lower layer, water bath distilling upper layer, and removing methanol.
NOVELTY - The machine has an extracting system for extracting water of straw. A smashing system smashes the straw. Smashing straw is inserted into a pressing system for performing tableting process. The extracting system is formed with a groove. The smashing system comprises a smashing roller. The pressing system comprises a pressing mold and a storage hopper, where size of an edge part of the pressing mold is about 40 mm. A spring is fixed at a bottom part of the pressing mold. A motor i.e. electrical machine, drives a machine body.    USE - Corn straw stick pressing machine.    ADVANTAGE - The machine is compact in structure and inexpensive, and has prolonged service life and better pressing efficiency. The machine increases corn straw processing efficiency so as to reduce working time consumption. The machine reduces smoke dust generation to increase application prospect range in an environment-friendly manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a corn straw stick pressing machine.
NOVELTY - Biological processing of sludge involves maintaining moisture content of fresh sludge to 76-84%. Fresh sludge and water are taken as base material in a ratio 1:1.4-1.6 to maintain water content to 28-32%. The base material is mixed. Microbial inoculum (2-2.5 wt.%) is added to the obtained material and mixed. The mixed material is heaped and fermented in reactor. The fermented material is dried.    USE - Method for biological processing sludge used for supplementary land, manufacturing of brick raw material, or production of energy product (claimed).    ADVANTAGE - The method is economical, energy-saving and environmental friendly.
NOVELTY - Preparation of biological organic fertilizer includes taking weeds, crop straw and garbage, crushing, and grinding; taking biogas produced compost, adding resulting mixture, adding chicken manure, soil and human waste, composting, maintaining air heap, and aerobically decomposing organic matter; mixing, adding composite microbial inoculum and nitrogen fertilizer, stirring, and adding water; composting and aerobically fermenting to form humus; separating, removing water, and separating into biogas; piling, drilling with sharp stick, covering with plastic; piling with gap, and ventilating.    USE - Method for preparing biological organic fertilizer (claimed).    ADVANTAGE - The method improves soil physical and chemical properties, soil fertility and high recovery and reduces pollution. The fertilizer has less organic matter, nitrogen, phosphorus and potassium loss.    DETAILED DESCRIPTION - Preparation of biological organic fertilizer comprises taking weeds, crop straw and garbage, crushing, and grinding into 15-20 mm length; taking biogas produced compost, adding resulting mixture, adding chicken manure, soil and human waste, composting, maintaining air heap, and aerobically decomposing organic matter; mixing, adding composite microbial inoculum and nitrogen fertilizer, stirring, and adding water; composting and aerobically fermenting to form humus; separating, removing water, and separating into biogas; piling, drilling for 4 weeks every 20 cm with sharp stick, covering with plastic, piling with 10 cm gap, and ventilating; adding phosphate powder and humic acid; adding rhizobium in biogas, adding phosphate solubilization agent, dissolving in phosphorus, adding Bacillus, dissolving in potassium, adding thiooxidans, and dissolving in sulfur; purging, dehydrating, desulfurizing, and storing; and adding into disk granulator and packaging.
NOVELTY - Production of organic fertilizer comprises taking dehydrated sludge and sterilizing at 121 degrees C for 3 hours; mixing with rice husk, processing at high temperature, mixing, and adding nutrient solution; and adding municipal sewage, adding into aeration sewage tank, adjusting water content to 55%, turning once a day until water content of 55-60%, and decomposing for 20 days.    USE - Method for producing organic fertilizer (claimed).    ADVANTAGE - The method increases degradable organic matter content and promotes aerobic composting.
NOVELTY - Mushroom cultivation matrix comprises 30-50 g soybean meal, 10-20 g rapeseed meal, 100-150 g wheat bran, 10-20 g corn powder, 0.5-1 g fermentation silkworm manure, 2-3 g sulfuric acid, 5-7 g ammonium sulfate, 1.5-1.7 mg vitamin B2, 3-5 mg vitamin B1, 0.5-0.7 mg triacontanol, 0.5-1 g sodium humate, and sawdust, per 1 kg matrix.    USE - Mushroom cultivation matrix.    ADVANTAGE - The scientific matrix has low cost, nutrient balance, simple process, good homogeneity, and strong operability. It increases yield, and fits industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of mushroom cultivation matrix comprising taking raw materials, and mixing uniformly.
NOVELTY - Preparation of livestock manure organic fertilizer comprises taking 50-70% dairy manure, 20-25% plant ash, 15-25% waste bran and balance water, uniformly mixing, adding into plastic greenhouse fermentation facility, adding effective microorganisms strain, fermenting at 40-50 degrees C, drying to water content of 13%, mixing, cooling, crushing to 60-80 mesh, adding water-retention agent and synergistic agent, completely mixing, adding adhesive, granulating, cooling and packaging.    USE - Method for preparing livestock manure organic fertilizer (claimed) used for vegetable and flower.    ADVANTAGE - The good-quality fertilizer greatly reduces odor, holds nutrients and preserves water.
NOVELTY - Straw raw materials are cut to 2-5 cm without crushing to obtain fragments. Preset amount of water and microbial agent are added to fragments, and fermentation is carried out under aerobic or anaerobic conditions for 10-30 days. The resulting material and water are added to acidification tank, acidification process is carried out by passing air, and stirred for 1-2 days. The resulting product from acidification tank is passed to methane fermentation tank and fermented to obtain biogas.    USE - Production of biogas (claimed).    ADVANTAGE - The method provides biogas without discharging wastewater within a short period of time, by efficient process.    DETAILED DESCRIPTION - Straw raw materials are cut to 2-5 cm without crushing to obtain fragments. Preset amount of water and microbial agent are added to fragments, and fermentation is carried out under aerobic or anaerobic conditions for 10-30 days. The resulting material and water are added to acidification tank, acidification process is carried out by passing air, and stirred for 1-2 days. The resulting product from acidification tank is passed to methane fermentation tank and fermented to obtain biogas. The portion of slurry from fermentation tank is subjected to solid-liquid separation, solid phase is used as organic fertilizer, and liquid phase is recycled and added to acidification tank.
NOVELTY - The method involves pouring fermenting material into a fermentation system. A space is formed between a feeding pipe (10) and a discharging pipe (20) and the adjacent side walls of an air resistance plate (36). The gas pressure in a cell is increased in the liquid flow to a feed pipe (30). The marsh gas sum pressure in the cell is reduced. The biogas slurry feed pipe is connected to a pipe by a one-way reflux pipe to finish the circulation flow of slurry. The circulation of gas is performed using the marsh gas in other cell.    USE - Method for generating methane using partition type methane biogas turbulence promoting effect generator.    ADVANTAGE - Since biogas slurry circulation flow stirring performance is improved, the gas production is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process for generating methane.    Feeding pipe (10)    Discharging pipe (20)    Feed pipe (30)    Air resistance plate (36)    Drain pipe (51)
NOVELTY - Device comprises solar cell panels (1,2), an electrolytic cathode (4), and an electrolytic anode (5), where the solar cell panel is connected to an electrolytic tank comprising electrolytic cathode, which is capable of generating hydrogen and electrolytic anode capable of generating oxygen on receiving sun light. The generated hydrogen is stored in an inverted U-shaped container (3). The electrolytic tank has a temperature sensor (11) for measuring temperature of electrolytic solution (11). The temperature sensor is connected with an automatic alarm protection device (12).    USE - Device used for producing hydrogen.    ADVANTAGE - The device effectively utilizes solar energy to generate hydrogen, the device also comprises hydrogen storing unit. The device has simple structure, and is capable of self-regulating hydrogen flow without utilizing pressure equipment in a secured and convenient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of hydrogen generating device.    Solar cell panel (1,2)    Inverted U-shaped container (3)    Electrolytic cathode (4)    Electrolytic anode (5)    Electrolytic solution (11)    Temperature sensor (11)    Automatic alarm protection device (12)
NOVELTY - A multi-trace drug simultaneous detection method in drinking water involves pretreating collected water samples, filtering water, and adding sodium EDTA to water sample. The water sample is subjected to solid phase extraction with methanol, transferred to ultrapure water pipes installed with hydrophilic-lipophilic balance (HLB)-solid phase extraction column, followed by subjecting the sample to HPLC-mass spectrometry for quantitative detection of pharmaceuticals and personal care products (PPCPs).    USE - Method for simultaneous detection of multi-trace drug, preferably PPCPs chosen from ibuprofen, ketoprofen, bezafibrate, nadolol, disopyramide and diltiazem in drinking water.    ADVANTAGE - The method enables simultaneously detecting multi-trace drugs in drinking water with high sensitivity and excellent repeatability in a simple and environmentally-friendly manner.    DETAILED DESCRIPTION - A multi-trace drug simultaneous detection method in drinking water involves pretreating collected water samples by adding 2.5 g ascorbic acid, determining chlorine content in water sample, filtering the water in glass fiber membrane to remove suspended solids, adding 0.5 g sodium EDTA to water sample, and adjusting pH of water to 2 with hydrochloric acid. The water sample is subjected to solid phase extraction with methanol, transferred to ultrapure water pipes installed with hydrophilic-lipophilic balance (HLB)-solid phase extraction column, activated with 6 ml methanol, 6ml sodium EDTA solution and 6 ml ultrapure water, column eluted with 10 ml methanol as eluent, utilizing 2 mg/l atrazine mixed with 0.1 %mass formic acid in a volume ratio of 1:9 as internal standard, adjusting solution volume to 1 ml, followed by subjecting the sample to HPLC-mass spectrometry for quantitative detection of pharmaceuticals and personal care products (PPCPs).
NOVELTY - Method for capturing and releasing acid gas(es) in a composition involves contacting at least one gas with capture composition, releasing acid gas(es) by adding at least one protic solvent (a) or agent to the composition, and regenerating the capture composition by partial or complete removal of protic solvent from the composition. The capture composition contains salt(s) of carboxylic acid and water-miscible nonaqueous solvent(s).    USE - Method for capturing and releasing acid gas e.g. carbon dioxide and sulfurous gas generated from submarines or spacecraft, natural gas sweetening, power stations, cement manufacture, steel manufacture, glass making, brewing, syngas process, natural gas and biogas purification, ammonia production and acid gas producing industrial processes (all claimed). Can also be used for absorption in chemical solvents, adsorption using solid adsorbent, membrane separation and cryogenic processes, post-combustion capture of carbon dioxide from thermal power plants.    ADVANTAGE - The method enables operating at lower temperatures by reducing atmospheric emissions and degradation. The method is capable of increasing carbon dioxide uptake capacity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the use of an aqueous composition.
NOVELTY - The utility model claims a methylal refining process equipment producing glyphosate by glycine method, wherein the device comprises a dehydration tower, methanol removing tower, a pressurizing tower and a methanol relux tower, wherein the dehydration, methanol removing tower, pressurizing tower and the tower top of methanol reflux tower are connected with a condenser and relux tank through pipelines, and a relux pump and tower top connected form relux, at the same time each of tower bottom are set with reboiler; bottom of the dehydration discharge pipe and a discharge pump and a methanol removing tower is connected with the bottom of the methyl alcohol removing tower is provided with a discharging pipe and a discharging pump and methyl alcohol tower in material wherein a relux, relux pump outlet and the tower top is set with branch pipe, a pressurizing tower and the material wherein a, the pressurizing tower and bottom of relux methyl alcohol tower are provided with product outlet. The utility model is novel effective refining a glyphosate product and methylal, reducing waste discharge and pollute environment, and increase the production benefit and greatly improves the glyphosate product added value, change waste as treasure.
NOVELTY - A. grinding device, a box body, a separating plate, a stirring mechanism, a grinding mechanism and grinding motor. The box body has water inlet is opened, a discharging and wherein. Separating plate fixedly holding box body. b, and a box form in stirring and grinding cavity, a water inlet and material inlet are connected a stirring cavity, a discharge wherein a grinding cavity connected, separating plate is provided the material has hole, in stirring and grinding in feed by a connected. Stirring machine equipped with box body b, and relative water inlet, a feed port and a feed set. Grinding machine equipped with grinding cavity in b, c and a connected and a feeding and discharging wherein. A grinding device formed by box body, separating plate, a stirring mechanism, a grinding mechanism and grinding motor, a simple and compact. In addition, by stirring machine for washing sewage, sewage and food waste as mixed pre-processing, which not only can increase fluidity of food waste, more preferably of a converying, grinding mechanism is a grinding operation.
NOVELTY - This utility model claims a domestic garbage treatment device, comprising a bowl washing entrance, washing entrance, sewage entrance washing food garbage entrance, the excretion entrance, smashing pre-processing device, a storage, grinding mixing device, mixing stirring device, heating device, marsh gas fermentation pool and gas stove. Bowel entrance and pre-process crushing device connected, storage pool and food waste entrance are connected and mixed grinding device, the excrement entrance, pre-process crushing device and mixing grinding device are connected and mixing stirring device, heating device and mixing stirring device connected, heating device and marsh gas fermentation pool connected. The domestic garbage treatment device using bowl washing waste, food waste, sewage and washing sewage characteristic and rich in organic matter, at the same time, adding large amount of Anaerobic fungus comprising the excrement, these garbage and waste water for processing unified Anaerobic fermentation process, to obtain the decomposition can entirely use as fuel gas and fertilizer.
NOVELTY - A. stirring device, comprising tube, stirring motor, the stirring main shaft and a stirring. Tube has set the first inlet, the second inlet bus and wherein, inside tube set with a mixed cavity, the first inlet and the second inlet are connected and mixed in, bus bar, wherein a tube is located far away from a terminal in the mix. .. b stir tube. A stirring shaft and a stirring motor connected rotating shaft, stirring shaft and b containing a body. A fixed stirring b. stirring main shaft, stirring a and b containing tube. A stirring device formed by tube, stirring motor, the stirring main shaft and a stirring, a simple and compact structure, and by stirring motor, stirring shaft and stirring a can for stirring bowl washing pre-processing garbage, excrement pre-processing food waste and mixing uniform, after a stirring device can stir to obtain the mixed pre-processing domestic garbage at the same time into a rich in organic substance and large amount of Anaerobic a, which is good for subsequent process Anaerobic fermentation process.
NOVELTY - A methane fermentation tank comprises the main cell body, liquid seal tank, exhaust pipes, the pressure control chamber, drain pipes, broken shells and broken shell tapered grille. The main cell body, respectively, liquid seal tank and pressure control chamber communicates liquid seal pool set on top of the main cell body, the main cell body is provided with a guide port and discharge port. Exhaust pipe at the junction with the main pool was closed cell body, and an exhaust pipe communicating with the main cell body. Pressure mediation room set up an overflow port. Drain pipe is provided at the junction with the main pool was closed cell body, and drain pipe in fluid communication with the main pool. Break shell cone sleeve is set on drainage tube, and break shell cone containing in main pool body. Broken shell sleeve is placed on the drain pipe, and broken shell tapered body housed in the main pool. Said methane fermentation tank by setting the main cell body, liquid seal tank, exhaust pipes, the pressure control chamber, drain pipes, broken shells and broken shell cone grille, compact simple, avoid encrustation, meanwhile, said methane the higher the efficiency of the anaerobic fermentation tank fermentation, a higher biogas production.
NOVELTY - A one heating device, comprising pipe body, the first heating pipe, the second heating pipe and the can mechanism. Pipe body is hollow rectangular-shaped structure, two end tube body of a set has a liquid inlet and a liquid outlet, pipe body form inner heating cavity, liquid inlet and liquid outlet are connected and wherein heating cavity, the pipe body inner side wall comprises the first mounting face and the second mounting face is relative. The first heating pipe. b the first mounting face, a heating pipe set b the second mounting face. Can supply mechanism respectively and the first heating pipe and the second heating pipe connect, for the first heating pipe and the second heating pipe. A heating device formed by tube body, the first heating pipe, the second heating pipe and the can mechanism, thus to pre-processing domestic garbage can is a heating operation so as to pre-processing domestic garbage subsequent Anaerobic. provide a good condition.
NOVELTY - One of mixing stirring device, comprising barrel, stirring motor, stirring shaft and stirring frame. Barrel is provided with the first inlet, the second inlet and collecting port, inner barrel comprises one mixing cavity, the first inlet and the second inlet are connected and mixed in the bus port of the tube far from one end in the mixture. Stirring motor is provided with tube. Stirring main shaft and rotary shaft of stirring motor connected with the stirring main shaft and contained in the cylinder body. Stirring frame fixedly set on stirring main shaft, a stirring frame and in the containing barrel. The mixing stirring device through is set with barrel, stirring motor, stirring shaft and stirring frame, structure is simple and compact, and by stirring motor, stirring shaft and stirring frame is for stirring bowl washing pre-processing garbage, excrement pre-processing food waste and mixing uniformly, later can be for mixing stirring device mixing stirring to obtain the pre-processing domestic garbage at the same time induce abundant of organic substance and large amount of Anaerobic fungus, facilitate follow-up by Anaerobic fermentation process.
NOVELTY - The utility model claims a countryside efficient digester, comprising fermentation tank, the fermentation tank sides are respectively provided feed pool and spent fuel pools, ponds between the inlet and the fermentation tank with a feed inlet between the fermentation tank and the spent fuel pools has a discharge port; the fermentation tank includes biogas fertilizer area and the communication area of the biogas fertilizer biogas areas; end including the airway, the airway into said biogas fermentation tank area, the other end of the guide tube extending the use of biogas fermentation tank communication device; a fermentation tank with a pneumatic stirrer. The utility model through the air mixing means not only conducive to the promotion of biogas decomposition and fully fermented, thereby improving the utilization of biogas, and the air mixing means easy installation and maintenance, long service life, which will help reduce production costs, suitable for a wide range of application.
NOVELTY - The utility model claims a closed circulation alga culture and marsh gas generating device, belonging to the technical field of biological energy source. The device comprises collecting a stillage, circulation pump, a timing controller, feedstock pipe, marsh gas pool, valve I, a valve II, a valve III, IV, discharging valve, an air guide pipe I, a guide pipe II, and biogas liquid circulation pipe, alga culture of alga culture liquid circulation pipe and a marsh gas pool connected phase, collecting a stillage and alga culture phase connected, stillage collect a feedstock tube and a circulation pump connected, circulation pump and a lower end a feedstock tube and a connected marsh gas, marsh gas pool is at a top end of a gas-guide pipe II and phase collecting tank connected, upper end is set with the sum pipe II, a bottom marsh gas pool is provided with the slag, and a circulation pump connected, the utility model is new type may implement a self-supply of raw material oxygen marsh gas fermentation system, good stability and a high efficiency.
NOVELTY - Supercritical hydrolysis of biomass involves size-reducing lignocellulosic biomass raw material to form lignocellulosic biomass having particle size less than 500 mu m, mixing size-reduced lignocellulosic biomass and water to form mixture, and contacting water (1) with mixture at 375 degrees C or more under pressure of 221 bar to form 5-6C saccharide such that the mixture is free of exogenous acid.    USE - Supercritical hydrolysis of biomass e.g. switch grass, corn stover and cobs, wheat straw and softwood.    ADVANTAGE - The method enables efficient supercritical hydrolysis of biomass using water at elevated temperatures and pressures in short period of time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of supercritical hydrolysis system.    Water (1)    Quench pump (2)    Condensate (3)    Cooling water supply (4)    Exhaust to roof (5)
NOVELTY - System comprises a conveying unit (100) provided with a first hollow portion formed inside a conveying passage of raw material, a raw material supplying unit for supplying raw material and is arranged on one side of the conveying unit, a first transferring unit of screw shape for providing conveying driving force of the raw material by the shaft rotation and is placed on the first hollow portion, and a discharge port for discharging the raw material arranged on the other side of the conveying unit.    USE - The system is useful for preprocessing biomass (claimed).    ADVANTAGE - The system continuously supplies bulk amount of fermentable sugars under high pressure conditions.    DETAILED DESCRIPTION - System comprises a conveying unit (100) provided with a first hollow portion formed inside a conveying passage of raw material, a raw material supplying unit for supplying raw material and is arranged on one side of the conveying unit, a first transferring unit of screw shape for providing conveying driving force of the raw material by the shaft rotation and is placed on the first hollow portion, and a discharge port for discharging the raw material arranged on the other side of the conveying unit. One side of the a first hollow portion crushes and extrudes the raw materials and is parallelly arranged with the first transferring unit and a second first transferring unit (120) of screw shape.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the conveying unit of the system.    Conveying unit (100)    First transferring unit (110)    Screw thread (111)    Disconnecting unit (112)    Second transferring unit (120)
NOVELTY - Stimulating and maintaining the activity of a microbial consortia within a subterranean solid carbonaceous medium to produce methane comprises: (a) dosing a first nutrient composition into the microbial consortia environment; (b) monitoring (140) the microbial consortia environment, including the generation of methane; (c) dosing a second nutrient composition into the microbial consortia based upon the results of step (b); (d) repeating steps (b) and (c) and, if required; and (e) dosing a further nutrient composition into the microbial consortia environment based upon the results of step (d).    USE - The method is useful for stimulating and maintaining the activity of a microbial consortia within a subterranean solid carbonaceous medium to produce methane.    ADVANTAGE - The method: utilizes the second nutrient composition that comprises substantially no nitrogen (claimed), thus avoiding the excessive dosage of at least one nutrient component including nitrogen; provides the stimulation that encourages the consortia to grow better and to generate higher levels of methane in gases produced; enables better management of the sustainable production of biogenic methane, as well as facilitating the accuracy/predictability of adaptive algorithm calculations; and improves the efficiency and sustainability of coal seam methane recovery.
NOVELTY - An isolated codon optimized nucleic acid sequence that encodes a xylose isomerase protein or enzymatically active fragment, comprising a nucleic acid sequence selected from SEQ ID NOS: 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, and 13, sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication, or a variant, is new.    USE - The isolated codon optimized nucleic acid sequence that encodes a xylose isomerase protein or enzymatically active fragment, cell and method are useful for processing of lignocellulose material for producing fuels and/or chemicals (claimed).    ADVANTAGE - The isolated codon optimized nucleic acid sequence that encodes a xylose isomerase protein or enzymatically active fragment, cell and method can be effectively used in the conversion of xylose to desired chemicals and fuels.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) an isolated polypeptide encoded by the codon optimized nucleic acid sequence;    (2) an expression construct comprising the isolated codon optimized nucleic acid sequence;    (3) a cell comprising the expression construct; and    (4) a method for processing of lignocellulose material, comprising: (a) treating the lignocellulose material to produce lignocellulosic biomass hydrolysate containing glucose, xylose, galactose, mannose, and arabinose; (b) contacting at least one cell with the lignocellulosic biomass hydrolysate; and (c) culturing the at least one cell under conditions where the substrate is catabolized to one or more fuels and/or chemicals.
NOVELTY - Manufacture of polyurethane involves forming an initial emulsion (e1) by mixing a mixture (A) comprising a monomer (a) and water immiscible organic solvent with a mixture (B) comprising water and surfactant, mixing initial emulsion (e1) and mixture (C) comprising water and monomer (b), and reacting monomer (a) and monomer (b) of obtained emulsion (e2) by interfacial polymerization. The obtained polyurethane has a number average molecular weight (Mn) of 30000-80000. The monomer (a) comprises two or more pentafluorophenyl carbonate (PFPC) groups having a structure (I).    USE - Manufacture of polyurethane. Uses include but are not limited to carrier for drugs e.g. insulin, glucagon, parathyroid hormone, calcitonin and vasopression, and for thermoplastics, surface coatings, textile coatings, adhesives, elastomers, foams and dispersions.    ADVANTAGE - The method enables manufacture of polyurethane without using metal catalyst by environmentally-friendly process.    DETAILED DESCRIPTION - Manufacture of polyurethane involves forming an initial emulsion (e1) by mixing a mixture (A) comprising a monomer (a) and water immiscible organic solvent with a mixture (B) comprising water and surfactant, mixing initial emulsion (e1) and mixture (C) comprising water and monomer (b) to form emulsion (e2) including monomer (a) and monomer (b), and reacting monomer (a) and monomer (b) of the emulsion (e2) by interfacial polymerization. The obtained polyurethane has a number average molecular weight (Mn) of 30000-80000. The monomer (a) comprises two or more pentafluorophenyl carbonate (PFPC) groups having a structure of formula (I). The monomer (b) comprises two or more nucleophilic amine groups, and each of the two or more nucleophilic amine groups is capable of reacting with a respective pentafluorophenyl carbonate group of the monomer (a) to form a respective carbamate group.
NOVELTY - Producing biogas in wet fermentation using nitrogen-rich, impurity-loaded inlet substrate, comprises precipitating sedimenting solid particles with an ammonium nitrogen concentration of greater than 5 kg NH4-N/m3, removing contaminants in a fermentation container (5), and continuously forming acetic acid and methane from a fermentation substrate (7) at a stable temperature in psychrophilic range in fermentation container.    USE - The method and the biogas plant are useful for producing biogas in wet fermentation using nitrogen-rich, impurity-loaded inlet substrate (all claimed).    ADVANTAGE - The method produces high-quality biogas in safe, stable and cost-efficient manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a biogas plant (1) for wet fermentation using nitrogen-rich, impurity-loaded inlet substrate, comprising the fermentation container, and a discharging device for discharging sedimented contaminants; and    (2) fermentation container for the biogas plant, comprising at least one vertically arranged screw with a rotary drive.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the method for producing biogas.    Biogas plant (1)    Fermentation container (5)    Fermentation substrate (7)    Dry substance-rich fraction (14)    Dry substance poor fraction (15)
NOVELTY - A photocatalyst comprises optical semiconductor containing element(s) chosen from titanium, vanadium, niobium and tantalum, and oxide particles containing cobalt and manganese as co-catalyst supported on optical semiconductor.    USE - Photocatalyst is used for electrode for manufacturing hydrogen and/or oxygen by optical water-splitting reactions (all claimed).    ADVANTAGE - The photocatalyst has excellent photocatalytic activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogen and/or oxygen, which involves immersing photocatalyst in water or electrolyte aqueous solution, irradiating light to photocatalyst or electrode for optical water-splitting reaction and carrying out optical hydrolyzing.
NOVELTY - Gas produced through the design of the specification is purified methane up to 90-95%, is claimed.    USE - The gas is useful as a methane gas (claimed).    ADVANTAGE - The biomethane with hydrogen gives high calorific and high intensity flame which is colorless and burns in fraction of seconds, thus saving time of burning. The production of hydrogen using zinc obtained from used pencil cells as given specification is unique idea. The design and implementation of physical plant given in figures 1.1-1.5 of the specification are unique (claimed) and provide benefits including zero carbon dioxide, environmentally friendly, management of organic waste, best conversion of waste energy into useable form, compact in size to process more waste, thus saving space, negligible formation of hydrogen sulfide in process, no foul smell and no corrosion of metal parts, gas storage facility, efficient methane gas production, reduced LPG consumption, low maintenance thus being cost effective, provides manure that can be utilized for growing the plants.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) the digester design of the specification is generalized;    (2) the design and implementation of physical plant; and    (3) the production of hydrogen using zinc obtain from used pencil cells as given specification.
NOVELTY - Treatment of avermectin fermentation wastewater involves taking 1.8 kg glucose, 0.18 kg potassium dihydrogen phosphate, 60 kg water and 0.05 kg Geotrichum candidum spore suspension, culturing at 27-28 degrees C and 100 revolutions/minute (rpm) to obtain Geotrichum candidum seed culture liquid, taking avermectin fermentation wastewater, heating at 100 degrees C for 30 minutes, plate and frame filter pressing, mixing 600 kg pre-treated avermectin fermentation wastewater, 0.3 kg urea and 60 kg Geotrichum candidum seed culture liquid and culturing at 27-28 degrees C and 100 rpm for 24 hours.    USE - Method for treating avermectin fermentation wastewater (claimed).    ADVANTAGE - The method is simple, environment-friendly and has low production cost.    DETAILED DESCRIPTION - Treatment of avermectin fermentation wastewater comprises taking 1.8 kg glucose, 7.5 kg yeast extract, 0.6 kg urea, 0.18 kg potassium dihydrogen phosphate, 60 kg water and 0.05 kg Geotrichum candidum spore suspension, culturing at 27-28 degrees C and 100 revolutions/minute (rpm) to obtain Geotrichum candidum seed culture liquid, taking avermectin fermentation wastewater, heating at 100 degrees C for 30 minutes, plate and frame filter pressing, mixing 600 kg pre-treated avermectin fermentation wastewater, 0.3 kg urea, 0.18 kg potassium dihydrogen phosphate and 60 kg Geotrichum candidum seed culture liquid, culturing at 27-28 degrees C and 100 rpm for 24 hours, plate and frame filter pressing and drying filter cake to obtain Geotrichum candidum biological feed.
NOVELTY - Fuel cell comprises cloth water system (1), anaerobic reaction area, wetland ecological type anode area and symbiotic algae area. The fuel battery pool is set with sewage inlet. The top part of the water outlet is set with inlet pipe (1-2). The anaerobic reaction area (2) is provided with anode matrix oxide. The three-dimensional network-shaped titanium anode (3-2) is set in facultative area (3-1). The network-shaped titanium cathode is connected with network-shaped titanium anode.    USE - Fuel cell.    ADVANTAGE - The fuel cell is efficient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for using fuel cell, which involves:    (A) connecting fuel battery pool with water inlet pipe;    (B) entering the sewage in an anaerobic reaction area;    (C) dissolving organic molecules;    (D) absorbing inorganic matter; and    (E) purifying water.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a fuel cell.    Cloth water system (1)    Inlet pipe (1-2)    Anaerobic reaction area (2)    Facultative area (3-1)    Network-shaped titanium anode (3-2)
NOVELTY - Cultivation of Flammulina velutipes mushroom involves cultivating bacteria strain, configuring with conifer wood chips-containing culture medium, inoculating, performing fruiting management and harvesting.    USE - Method for preparing Flammulina velutipes mushroom.    ADVANTAGE - The method is inexpensive, and has convenient agricultural operation.
NOVELTY - Industrial cultivation of Flammulina velutipes mushroom involves cultivating bacterial, preparing culture medium, sowing, inoculating, performing fruiting management, harvesting and cleaning.    USE - Method for cultivating Flammulina velutipes.    ADVANTAGE - The method is inexpensive, time-saving, and has convenient agricultural operation.
NOVELTY - Pleurotus eryngii mushroom cultivation includes taking 72 wt.% agricultural and forestry waste, 20-26 wt.% bran, 2-3 wt.% mushroom pin, 1.5- wt.% lime and 1 wt.% precipitated calcium carbonate, taking mushroom pin, adding water, soaking for 18-24 hours at room temperature, adding slag cultivation feed, mixing, adding culture medium, adjusting periphery light, fermenting at 60 degrees C for 24 hours, adding lime and calcium carbonate, fermenting for 5-6 days, adjusting moisture content to 63-65%, cooling, performing fruiting management, adding water and soaking at room temperature.    USE - Method for cultivating Pleurotus eryngii mushroom (claimed).    ADVANTAGE - The method improves quality of Pleurotus eryngii mushroom, increases yield, and saves energy. It has high biological conversion rate.    DETAILED DESCRIPTION - Pleurotus eryngii mushroom cultivation involves taking 72 wt.% agricultural and forestry waste, 20-26 wt.% bran, 2-3 wt.% mushroom pin, 1.5- wt.% lime and 1 wt.% precipitated calcium carbonate, taking mushroom pin, adding water, soaking for 18-24 hours at room temperature, adding slag cultivation feed, mixing, adding culture medium, adjusting periphery light, fermenting at 60 degrees C for 24 hours, adding lime and calcium carbonate, fermenting for 5-6 days, adjusting moisture content to 63-65%, cooling, performing fruiting management, adding water, soaking at room temperature for 18-24 hours, filtering residue, collecting mushroom extract and adding water dilution. The agricultural and forestry waste are dried and crushed granules of cotton seed hulls, corn cobs, bagasse, wood chips, bamboo chips, cotton stalks, rapeseed stem, cassava stem or peanut shell.
NOVELTY - Cultivation of Pleurotus mushroom includes weighing 80 wt.%, agricultural and forestry waste product, 12-18 wt.% bran, 2-3 wt.% mushroom, 1.5 pts. wt. lime and 1 pt. wt. lime, mixing mushroom and water at room temperature, soaking for 18-24 hours, adding slag cultivation feed, mixing, adding culture medium, piling agricultural and forestry waste products, stacking, adjusting periphery light, covering with grass, fermenting at 60 degrees C for 24 hours, adding lime and calcium carbonate, fermenting for 5-6 days, adjusting moisture content to 63-65%, cooling and performing fruiting management.    USE - Method for cultivating Pleurotus mushroom (claimed).    ADVANTAGE - The method is time-saving, energy-saving and has high biological conversion rate. It increases yield and biological efficiency.    DETAILED DESCRIPTION - Cultivation of Pleurotus mushroom involves weighing 80 wt.%, agricultural and forestry waste product, 12-18 wt.% bran, 2-3 wt.% mushroom, 1.5 pts. wt. lime and 1 pt. wt. lime, mixing mushroom and water at room temperature, soaking for 18-24 hours, adding slag cultivation feed, mixing, adding culture medium, piling agricultural and forestry waste products, stacking, adjusting periphery light, covering with grass, fermenting at 60 degrees C for 24 hours, adding lime and calcium carbonate, fermenting for 5-6 days, adjusting moisture content to 63-65%, cooling, performing fruiting management and spawning. The agricultural and forestry waste are dried and crushed granules of cotton seed hulls, corn cobs, bagasse, wood chips, bamboo chips, cotton stalks, rapeseed stem, cassava stem or peanut shell.
NOVELTY - A visible light-responsive photocatalyst comprises lithium-bismuth borate, and is prepared by mixing lithium cobalt, bismuth oxide and boric acid powders with purity of 99.9% in a ball-milling tank, adding zirconia balls and anhydrous alcohol, ball-milling for 8 hours, mixing, drying, sieving by 200 mesh sieve, presintering at 650-700 degrees C for 6 hours, naturally cooling to room temperature, and crushing to particles having particle size of less than 2 mu m by a ball mill.    USE - Visible light-responsive photocatalyst is used in decomposition of harmful substances, organic biomass and bacteria.    ADVANTAGE - The visible light-responsive photocatalyst has excellent stability and light conversion efficiency, and is prepared by simple, efficient and economical process at low synthesis temperature.    DETAILED DESCRIPTION - A visible light-responsive photocatalyst comprises lithium-bismuth borate (LiBi3B4O11), and is prepared by mixing lithium cobalt, bismuth oxide and boric acid powders with purity of 99.9% in a ball-milling tank, adding zirconia balls and anhydrous alcohol, ball-milling for 8 hours, mixing, drying, sieving by 200 mesh sieve, presintering at 650-700 degrees C for 6 hours, naturally cooling to room temperature, and crushing to particles having particle size of less than 2 mu m by a ball mill.
NOVELTY - An integrated urban waste sludge treatment method involves constructing waste sludge processing plant, classifying waste materials, processing waste materials and using processed waste products.    USE - Integrated urban waste sludge treatment method (claimed).    ADVANTAGE - The method produces biogas using waste sludge incineration material as accelerant, improves combustion stability, enhances power generation efficiency of incinerator and increases the overall revenue. The method produces processed slag that is used as construction material and produces biomass diesel oil for waste transport vehicles in economical manner.
NOVELTY - A household organic fertilizer maker comprises rotten vegetable peel anaerobic fermentation bin (1), peculiar smell absorbing open water tank (2), cover (3), exhaust pipe (4), and pressure regulating valve (5).    USE - Household organic fertilizer maker.    ADVANTAGE - The household organic fertilizer maker is convenient to use, energy-saving and environment-friendly, and it has simple structure and low manufacturing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of household organic fertilizer maker.    Rotten vegetable peel anaerobic fermentation bin (1)    Peculiar smell absorbing open water tank (2)    Cover (3)    Exhaust pipe (4)    Pressure regulating valve (5)
NOVELTY - Photoelectric catalytic water decomposing hydrogen production assay detection system comprises photoelectric catalytic water decomposing hydrogen production device and gas quantitative analysis detection system. Photoelectric catalytic water decomposing hydrogen production device comprises a reactor (2), and a rotary cover. The reactor is cylindrical structure, which is closed in bottom and open at top. The reactor side wall is convex, and is provided with illumination window (5). The reactor lower part is provide with jacket (1).    USE - Photoelectric catalytic water decomposing hydrogen production assay detection system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of photoelectric catalytic water decomposing hydrogen production assay detection system.    Jacket (1)    Reactor (2)    Water outlet (3)    Water inlet (4)    Illumination window (5)
NOVELTY - Infectious hazardous waste aerobic sealed treatment comprises using a device comprising a first closed chamber and second closed chamber having first and second inlets, respectively, feeding carrion into the first closed chamber, sterilizing, feeding the sterilized carrion into the second closed chamber and conducting aerobic fermentation using composite microbial inoculum.    USE - Infectious hazardous waste aerobic sealed treatment (claimed).    ADVANTAGE - The method does not cause secondary environmental pollution, since all the steps are carried out in closed chambers.
NOVELTY - An organic fertilizer comprises 30-40 pts. wt. municipal domestic sludge, 20-25 pts. wt. plant ash, 5-10 pts. wt. crushed straw, 5-10 pts. wt. cassava slag, 15-20 pts. wt. poultry excrement, and 5-10 pts. wt. auxiliary agent.    USE - Organic fertilizer.    ADVANTAGE - The fertilizer has low cost, short composting time, and no peculiar smell. It does not pollute the environment.
NOVELTY - Comprehensive utilization of coal-based synthesis gas comprises contacting and reacting gas and methanol synthesis catalyst and/or reacting synthesis gas with low carbon alcohol catalyst; contacting and reacting gas and synthetic oil catalyst and/or reacting gas and synthetic natural gas catalyst; and combining.    USE - Method for comprehensive utilization of coal-based synthesis gas (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for comprehensive utilization of coal-based synthesis gas system comprising methanol synthesis reactor and/or low carbon alcohol synthesis reaction; and 1-3 synthetic oil reactors and/or synthesis gas reactors; where the reactors are connected in series and each reactor is provided with heat exchange device.
NOVELTY - Separating a feed gas in carbon dioxide involves applying wellhead pressure to a gas well for guiding the feed gas, and using gas separation membrane for separating feed gas from gas well. The wellhead pressure is 1-9 megapascal.    USE - Method for separating feed gas (claimed).    ADVANTAGE - The feed gas separation method is cost-effective and ensures recovery rate high.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for separating feed gas, which has feed gas inlet.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the feed gas separation method. (Drawing includes non-English language text).
NOVELTY - Method for preparing organic fertilizer involves (a) mixing sawdust, beet pulp and cottonseed meal in a weight ratio of 4-6:2-4:1-3, and harvesting mushroom using mixture, and pulverizing waste after 40-60 days of harvesting process, (b) mixing the product obtained in the step (a) with culture filtrate of wild ginseng root, Lactobacillus, Saccharomyces cerevisiae and Bacillus subtilis in a weight ratio of 450-550:8-12:0.5-1.5, and performing fermentation process at 25-30 degrees C for 5-10 days.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare product in an environmentally-friendly manner.
NOVELTY - Constructing biogas digesters system in Karst topography comprises looking pothole or ditch hole in Karst for constructing biogas digesters system, choosing one pothole or ditch hole as biogas digesters tank base (1), laying a layer of clay (2) in the inner wall of the tank base, where the thickness between the tank base bottom and the clay side wall is 30-100 mm, and the top thickness of the tank base is greater than or equal to 10 mm of the inner wall of clay.    USE - The method is useful for constructing biogas digesters system in Karst topography (claimed).    DETAILED DESCRIPTION - Constructing biogas digesters system in Karst topography comprises looking pothole or ditch hole in Karst for constructing biogas digesters system, choosing one pothole or ditch hole as biogas digesters tank base (1), laying a layer of clay (2) in the inner wall of the tank base, where the thickness between the tank base bottom and the clay side wall is 30-100 mm, and the top thickness of the tank base is greater than or equal to 10 mm of the inner wall of clay; the top of the tank base is provided with a cell cover (11); the tank base is partitioned into lower fermentation chamber (3) and upper water pressure room; the fermentation chamber and the pressure room are connected together by a hydraulically inter-channel (31); the inner side of the fermentation chamber is connected to the outer side of the tank base via hydraulically inter-channel; the top of the tank base is provided with sheds, where the toilet or waste disposal area of the shed is connected to fermentation chamber hydraulically inter-channel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas digesters system.    Tank base (1)    Clay (2)    Fermentation chamber (3)    Cell cover (11)    Hydraulically inter-channel (31)
NOVELTY - Production of potassium dihydrogen phosphate involves mixing calcium hydrogen phosphate and water in ratio of 1:2-1:3, transferring to gravity machine, high-speed mixing, heating at 85-95 degrees C, adding phosphoric acid, reacting, controlling pH value at 3-3.2, rapidly mixing obtained calcium dihydrogen phosphate in gravity machine, controlling temperature of reaction product at 80 degrees C, adding potassium sulfate solution, reacting for 2 hours, filtering, adjusting pH of filtrate to 4-4.5 using phosphoric acid, concentrating, cooling, crystallizing, dehydrating, and drying.    USE - Production of potassium dihydrogen phosphate (claimed).    ADVANTAGE - The potassium dihydrogen phosphate is produced with high quality and without producing waste, by simple and economical method.    DETAILED DESCRIPTION - Production of potassium dihydrogen phosphate involves mixing calcium hydrogen phosphate and water in ratio of 1:2-1:3, transferring to gravity machine, high-speed mixing, heating at 85-95 degrees C, adding phosphoric acid, reacting for 1 hour, controlling pH value at 3-3.2, rapidly mixing obtained calcium dihydrogen phosphate in gravity machine, controlling temperature of reaction product at 80 degrees C, adding potassium sulfate solution, reacting for 2 hours, filtering, adjusting pH of filtrate to 4-4.5 using phosphoric acid, concentrating until the density of filtrate reaches 1.32-1.33 kg/m3, cooling, crystallizing, dehydrating, and drying. The molar ratio of calcium hydrogen phosphate and phosphoric acid is 1:0.8-1:1.1. The molar ratio of calcium dihydrogen phosphate and potassium sulfate is 1:0.8-1:1.2.
NOVELTY - Method for multifunctional high yield cultivation technology involves (a) fermenting fresh pig, chicken, duck manure with decomposing agent to reduce fecal odor in barrel, maintaining the fermented product into fly maggot cultivation room for 2-3 days growth time, (b) collecting 40-60% maggot manure and adding grass or waste, fermenting using decomposing agent, maintaining the fermented product in earthworm cultivation farm, under strong light source and base.    USE - The method is useful as multifunctional high yield cultivation technology (claimed).    ADVANTAGE - The manure is multifunctional, has no odor, provides high yield, enhances animal disease resistance and growing speed, and is cost-effective.
NOVELTY - The device has a fertilizer molding apparatus (A) that molds the mixture in which foreign substance is separated. A dispersion cooling unit (80) disperses the dried food waste. A water control unit (30) controls the moisture by second dehydration in spraying device (40) and spreading of odor reduction agent. The spraying device is arranged with the supplementary raw material. A fermenter (60) deodorizes the generated second bad smell, while second separation and food is heated and dried.    USE - Fertilizer manufacturing device using food waste.    ADVANTAGE - The food waste is dehydrated while transferred and supplied in the hopper. The process efficiency of fertilizer is increased. The bad smell deodorizaton and impurity removal are achieved efficiently. The quality of manufacturing fertilizer is increased effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fertilizer manufacturing device using food waste.    Water control unit (30)    Spraying device (40)    Fermenter (60)    Dispersion cooling unit (80)    Fertilizer molding apparatus (A)
NOVELTY - Process for bio-flora culturing involves removing bacterial strain from storage tank, adding bacterial strain to culture tank, adding glucose, nitrogen and phosphorus nutrients continuously to culture tank, passing oxygen through air compressor to culture tank to control dissolved oxygen at 2-3 and culturing for 1 week to obtain mature bacterial species.    USE - The bio-flora culturing process is useful for obtaining mature bacterial species, which is useful for sewage treatment.    ADVANTAGE - The process enables simple and easy culturing of baterial species with enhanced activity.
NOVELTY - Fertilizer comprises 42.2-46.5 % fir slag, 35-37.5 % mud material, 14.2-17.5 % fir powder, 3.1-3.5 % biological degradation agent. Mud material comprises fresh weeds, perlite and loam which are fermented for 5-10 days to obtain mud material, where water content of mud material is 60-70 %. Water content of fir powder is 35-40 %.    USE - Fertilizer used for yew.    ADVANTAGE - The fertilizer solves yew low yields and poor growth problems.
NOVELTY - Preparing nutritive solution containing humic acid involves (a) dissolving amino acid in suitable amount of water, (b) adding ferrous sulfate in the form of chelated iron to the dissolved amino acid, (c) dissolving the remaining raw materials gradually, (d) adjusting pH value of humic acid containing supernatant to 6-7, (e) adding 20 wt.% supernatant to the mixture obtained in step (c), and (f) adding suitable amount of distilled water to the mixture, and adjusting pH value of the mixture to 2-3 using citric acid.    USE - The method is useful for preparing nutritive solution containing humic acid (claimed).    ADVANTAGE - The prepared nutritive solution promotes growth of fruits.    DETAILED DESCRIPTION - Preparing nutritive solution containing humic acid involves (a) dissolving amino acid in suitable amount of water, (b) adding ferrous sulfate in the form of chelated iron to the dissolved amino acid, (c) dissolving the remaining raw materials gradually, (d) adjusting pH value of humic acid containing supernatant to 6-7, (e) adding 20 wt.% supernatant to the mixture obtained in step (c), and (f) adding suitable amount of distilled water to the mixture, and adjusting pH value of the mixture to 2-3 using citric acid, where the raw materials comprise 8-10 wt.% urea, 5-10 wt.% potassium dihydrogen phosphate, 3-7 wt.% ferrous sulfate, 0.5-1.5 wt.% amino acid, 5-7 wt.% sucrose, 1-3 wt.% boric acid, 1-3 wt.% zinc sulfate, 0.5-1 wt.% copper sulfate, 0.2-0.8 wt.% manganese sulfate, 1-2 wt.% calcium chloride, 20 wt.% humic acid containing supernatant, and water (remainder).
NOVELTY - Preparation of farnesal involves reacting farnesol with organic solvent in presence of oxidant and catalyst. The catalyst is copper or copper compound.    USE - Preparation of farnesal used for manufacturing polyprenoic acid (claimed).    ADVANTAGE - The farnesal is prepared with yield of more than 85% and purity of more than 95% by environmentally-friendly method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of polyprenoic acid which comprises oxidizing farnesol with catalyst and oxidizing agent in organic solvent, subjecting the obtained farnesal to the Honel-Emmons reaction and hydrolyzing the obtained farnesal.
NOVELTY - Modifying a flavonoid compound terminated with glucuronic acid with hyaluronan oligosaccharide chain comprises adding uridine diphosphate-N-acetylglucosamine glucose into tris (hydroxymethyl)aminomethane hydrochloride buffer and then stirring to obtain uridine diphosphate-N-acetylglucosamine glucose solution. Hyaluronan synthase is added into uridine diphosphate-N-acetylglucosamine glucose solution and then heated at 28 degrees C for 10 minutes to obtain mixture. The mixture is stirred at 2-8 degrees C for 20-60 minutes to obtain supernatant. The supernatant is concentrated at 30-37 degrees C for 30-60 minutes to obtain concentrated liquid.    USE - Used for preparing anticancer drug.    ADVANTAGE - The method enables to prepare the flavonoid compound that is prepared in a cost-effective and eco-friendly manner and has potential clinical application.    DETAILED DESCRIPTION - Modifying a flavonoid compound terminated with glucuronic acid with hyaluronan oligosaccharide chain comprises adding uridine diphosphate-N-acetylglucosamine glucose into tris(hydroxymethyl)aminomethane hydrochloride buffer and then stirring to obtain uridine diphosphate-N-acetylglucosamine glucose solution. Hyaluronan synthase is added into uridine diphosphate-N-acetylglucosamine glucose solution and then heated at 28 degrees C for 10 minutes to obtain mixture. The mixture is stirred at 2-8 degrees C for 20-60 minutes to obtain supernatant. The supernatant is concentrated at 30-37 degrees C for 30-60 minutes to obtain concentrated liquid. The concentrated liquid is eluted using silica gel chromatography to obtain elute. the obtained elute is frozen and then dried to obtain the product.
NOVELTY - Cocoa special fertilizer comprises 24-26 pts. wt. soybean straw, 21-23 pts. wt. broad bean straw, 16-18 pts. wt. rape straw, 12-14 pts. wt. rice straw, 13-15 pts. wt. dried sainfoin, 8-10 pts. wt. dry locust leaves, 10-12 pts. wt. composted cattle manure, 5-7 pts. wt. peanut cake fertilizer, 7-9 pts. wt. diammonium phosphate, 4-6 pts. wt. boron and magnesium-phosphate fertilizer, 3-5 pts. wt. straw decomposition agent, 6-8 pts. wt. zinc sulfate heptahydrate, 1-3 pts. wt. alginic acid, 2-4 pts. wt. manganese chloride and 70-80 pts. wt. water.    USE - Cocoa special fertilizer (claimed).    ADVANTAGE - The fertilizer is rich in nutrients, increases soil organic matter, enhances stress resistance of cocoa, and enables to produce smooth and aromatic cocoa beans and soft and thin pod shell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing cocoa special fertilizer, which involves (a) crushing soybean, broad bean straw, rape straw, rice straw, dried sainfoin, dry locust leaves, composted cattle manure and peanut cake fertilizer to obtain 40 mesh size powder, (b) adding crushed mixture to diammonium phosphate, boron-magnesium-phosphate fertilizer, straw decomposition agent, zinc sulfate heptahydrate, alginic acid, manganese chloride and water, and (c) stirring mixture and sealing stirred mixture, fermenting for 5 hours and drying fermented mixture and granulating to obtain fertilizer.
NOVELTY - Fertilizer, comprises 60-80 parts mass chicken manure, 40-60 parts mass sheep manure, 20-40 parts mass protein sludge, 10-12 parts mass rock phosphate, 12-16 parts mass potassium mineral powder, 20-30 parts mass wheat middling, 20-30 parts mass lees, 5-7 parts mass ammonium sulfate, 8-10 parts mass potassium sulfate, 0.3-0.5 part mass borax, 20-30 parts mass furfural residue, and 80-100 parts mass water.    USE - As fertilizer for Gingko (claimed).    ADVANTAGE - The fertilizer increases Gingko yield, improves quality of Gingko fruit, improves soil, and does not leave residue, and cause pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer which involves crushing the above-mentioned raw materials using a crusher, adding water to the crushed materials, sealing the mixture 5-7 days, allowing the mixture to stand for 10 hours, and granulating the mixture.
NOVELTY - Breeding silver carp using biogas fermentation residue involves selecting a flat bottomed pond having good water draining facilities, stocking silver carp, common carp, crucian carp and other omnivorous animals in pond, stocking fishes during spring or autumn, applying biogas fermentation residue, adding water to pond, and harvesting fish after it grows to a size of 25-35 cm.    USE - The method is useful for breeding silver carp using biogas fermentation residue (claimed).    ADVANTAGE - The method is environmentally-friendly, and makes use of biogas fermentation residue.    DETAILED DESCRIPTION - Breeding silver carp using biogas fermentation residue involves (a) selecting a flat bottomed pond having good water draining facilities, good soil quality having a surface area of 2800-6400 m2, and depth of 2-3 m, (b) stocking silver carp at a density of 70%, and remaining 30% with common carp, crucian carp and other omnivorous animals in the pond, (c) selecting fry that has reached a size of 14-16 cm, (d) stocking 700-900 fishes per acre of pond during spring or autumn, where mid-March to end of April during spring, and between August to October during autumn, (e) applying 200-300 kg biogas fermentation residue per acre of pond, and adding water to a height of 50-80 cm, and (f) applying the residue once in every 10-12 days, where 28-32 kg residue is applied per 100 m2 of pond, and harvesting fish after it grows to a size of 25-35 cm.
NOVELTY - Marsh gas raw material composition comprises 30-35 pts. wt. pig manure, 40-45 pts. wt. dairy manure, 15-20 pts. wt. Arundo donax, 15-20 pts. wt. elephant grass, 15-25 pts. wt. mushroom residue and 10-20 pts. wt. marsh gas residue having 30-40% moisture content, where the marsh gas residue is precipitate of marsh gas digesters.    USE - As marsh gas raw material composition.    ADVANTAGE - The marsh gas raw material composition enables longer and higher marsh gas production.
NOVELTY - Marsh gas raw material composition comprises 30-35 pts. wt. switchgrass, 40-45 pts. wt. Sorghum straw, 45-50 pts. wt. livestock manure, 15-25 marsh gas residue and 10-20 pts. wt. biological bacteria.    USE - As marsh gas raw material composition.    ADVANTAGE - The marsh gas raw material composition enables longer and higher marsh gas production.
NOVELTY - Strain of microalgae Desmodesmus sp. 3Dp86E-1 has high rate of CO2 fixation and tolerance to high concentrations of CO2 in the cultivation medium, and the high ability to accumulate lipids enriched with polyunsaturated fatty acids. The strain is deposited in the Collection of microalgae cultures of the Institute of Plant Physiology n.a. K.A. Timiryazev RAS (IPPAS) under the registration number Desmodesmus sp. IPPAS S-2014 and can be used for conversion of carbon dioxide from industrial waste gases in the raw material for production of biofuel and feed additives.    USE - Biotechnology.    ADVANTAGE - Invention enables to improve the rate of fixation of CO2 in air-gas mixture.4 dwg, 1 tbl
NOVELTY - Manufacture of wood pellets involves collecting waste wood, transferring to a grinding chamber, injecting high pressure jet of sand into waste wood in grinding chamber, separating contaminants adhered to waste wood including oil, adhesive tapes, paint, enamel, varnish and concrete, removing contaminants, transferring the chamber to water tank by a conveyor, separating contaminant from sand based on specific gravity difference, and performing high-pressure molding.    USE - Manufacture of wood pellets (claimed).    ADVANTAGE - The wood pellets are manufactured efficiently and economically without affecting the environment by recycling waste wood effectively.
NOVELTY - A solubilization apparatus (100) of organic waste comprises storage tank (10) which stores organic waste before being sent to methane fermentation tank, greater than or equal to 3 solubilization tanks (11A-11C, 12A-12C) consisting of lowermost stage, uppermost stage, and middle stage which are connected in series, solubilization tank lines (11, 12) for performing solubilization of organic waste, and path where organic waste is sent.    USE - A solubilization apparatus of organic waste.    ADVANTAGE - Solubilization rate of organic waste can be increased, therefore improving methane fermentation efficiency of organic waste.    DETAILED DESCRIPTION - A solubilization apparatus (100) of organic waste comprises storage tank (10) which stores organic waste before being sent to methane fermentation tank, greater than or equal to 3 solubilization tanks (11A-11C, 12A-12C) consisting of lowermost stage, uppermost stage, and middle stage which are connected in series, solubilization tank lines (11, 12) for performing solubilization process of organic waste, and path where organic waste is sent. Height of path positioned between uppermost solubilization tank and middle stage solubilization tank is lower than height of path positioned between lowermost solubilization tank and middle stage solubilization tank. The apparatus solubilizes organic waste sent to methane fermentation tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional diagram of the solubilization apparatus. (Drawing includes non-English language text).    Storage tank (10)    Solubilization tank line (11)    Solubilization tanks (11A, 11B, 11C)    Solubilization tank line (12)    Solubilization tank (12A, 12B, 12C)    Solubilization apparatus (100)
NOVELTY - The method involves dosing organic waste materials in liquid or vapor form into an ascending gas flow against the counter-current to an energy buffer i.e. heated bulk moving bed (2). The organic waste is thermally cracked during the flow of the energy buffer under reductive conditions to synthesis gas. A natural temperature of the energy buffer is provided with a gradient, which is decreased in a direction of flow of the synthesis gas. The organic waste materials are treated with a temperature of 400 degree Celsius.    USE - Method for thermal cracking organic waste materials e.g. carbonaceous residues or simmering fractions, from distillation or refining processes from a chemical or petrochemical industry, carbonaceous secondary or co-products from chemical processes of transformation or organic residues from chemical or thermal utilization of biomasses, and carbonaceous residues or useless separation phases from extraction or eluate ion processes (all claimed).    ADVANTAGE - The natural temperature of the energy buffer is provided with the gradient, which is decreased in the direction of flow of the synthesis gas, so that thermal cracking of the organic waste materials can be performed in an efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a shaft reactor.    Shaft reactor (1)    Heated bulk moving bed (2)    Feed tube (3)    Emptying system (4)    Oxidation zone (7)
NOVELTY - A cathode comprises conductive support substrate consisting of catalyst coating which contains nickel phosphide (Ni5P4) nanocrystals.    USE - A cathode used for generating hydrogen gas from water by electrolysis and reduction of hydrogen cations (all claimed).    ADVANTAGE - The Ni5P4 compound as HER catalyst has excellent chemical stability in strong acid and strong base and shows unexpected and stable HER activity at both acidic and alkaline pH and provides cost-effective renewable hydrogen production from water when paired with water oxidation catalysts.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) generation of hydrogen gas from water by electrolysis which involves placing anode and cathode in electrolyte, placing anode and cathode in conductive contact with external source of electricity, providing source of water to cathode, and using external source of electricity to drive electrolysis reaction at the cathode in which hydrogen gas is generated from water;    (2) reduction of hydrogen cations to form hydrogen gas which involves placing anode and cathode in electrolyte, placing anode and cathode in conductive contact with external source of electricity, providing source of hydrogen cations to cathode, and using external source of electricity to reduce cations at the cathode in which hydrogen gas is generated at the cathode; and    (3) electrochemical cell for hydrogen evolution reaction (HER) comprising chamber capable of containing aqueous electrolyte, anode in contact with aqueous electrolyte when chamber contains aqueous electrolyte, and cathode which is in conductive contact with anode when chamber contains the aqueous electrolyte.    DESCRIPTION OF DRAWING(S) - The drawing shows a powder X-ray diffraction (PXRD) pattern of nickel phosphide microparticles and a reference pattern.
NOVELTY - Reaction vessel (200) comprises a first tubular shell (210), and a second tubular shell (220) positioned within the first tubular shell and is coaxially aligned with the first tubular shell. The second tubular shell comprises: a hydrogen permeable anode electrode (221) interior surface; a hydrogen permeable cathode electrode (222) exterior surface; and a proton transfer membrane positioned between the interior and exterior surfaces. The areas inside second tubular shell defines a first reaction zone and area between second tubular shell and first tubular shell define a second reaction zone.    USE - The reaction vessel is useful for producing an alcohol such as methanol from methane (claimed) which is useful as liquid energy storage fuels for producing hydrogen useful as a fuel in various applications.    ADVANTAGE - The reaction vessel provides improved yield efficiency of liquid fuel such methanol.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of a reaction vessel.    Reaction vessel (200)    First tubular shell (210)    Second tubular shell (220)    Hydrogen permeable anode electrode (221)    Hydrogen permeable cathode electrode (222)
NOVELTY - A catalyst comprises 10-30 pts. wt. nickel as active metal component and remainder of SBA-15-type mesoporous molecular sieve as catalyst carrier.    USE - Catalyst used for conversion of syngas to methane (claimed).    ADVANTAGE - The catalyst has excellent selectivity, stability, durability and activity, and has methane selectivity of 96%, and carbon monoxide conversion rate of 100%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of catalyst, which involves using nickel salt and solvent; and    (2) usage of catalyst for conversion of syngas to methane.
NOVELTY - The new type utility claims a plant for preparing liquefied natural gas device, relating to the field of a natural gas liquefying system increase energy efficiency, saves investment and increase benefit then project. The preparing liquefied natural gas comprising a cold box, wherein in the cold tank liquid oxygen and coal gasification process product and a full heat exchange. The utility model is new type may use for natural gas liquefaction.
NOVELTY - The apparatus has a set of feed inlets (124, 134) mounted tangentially onto sidewalls (102a, 102b) of an outer cyclone structure (101b) and a combustion chamber for infeed of biomass feedstock by blown gas. An outlet (108) is extended from a tapered top portion (104) into an upper portion of a cyclonic structure, where non- condensable gases or bio-oil vapours swirl upwards from a tapered bottom section (106a) of an inner cyclone structure (105) to exit though the outlet when solid products/remnants are discharged through an exit opening (109).    USE - Apparatus e.g. torrefaction reactor, bio-oil production reactor and gasifier (all claimed) such as fixed bed gasifier, fluidized bed gasifier and cyclonic gasifier, for producing biofuels from biomass.    ADVANTAGE - The apparatus enables effective control of temperature, pressure and air/fuel ratio to maintain a stable and consistent operating condition during thermal conversion process by using a programmable logic controller system, thus enhancing heat transfer rate to a feedstock by vigorous abrasion against heated walls of the apparatus under action of a centrifugal force generated by cyclonic motion of vortex generated inside the apparatus, and hence providing an improved apparatus with a simple structure without moving parts to minimize subsequent maintenance cost and providing longer residence time to allow relatively coarser particle sizes of biomass feedstock for torrefaction, pyrolysis and gasification processes.    DESCRIPTION OF DRAWING(S) - The drawing shows a front elevational view of an apparatus for producing biofuels from biomass.    Outer cyclone structure (101b)    Sidewalls (102a, 102b)    Tapered top portion (104)    Inner cyclone structure (105)    Tapered bottom section (106a)    Outlet (108)    Exit opening (109)    Feed inlets (124, 134)
NOVELTY - The new type utility claims one using a carbonizing rice hull combustion-supporting gas of burner, comprising air cavity, a mixing cavity is set with air in one end, and set with ignition in a mixed in after a set of combustion in a cavity after ignition. The air cavity by carbonizing rice hull fuel gas conveying pipe, a combustible gas supplying pipe and air conveying pipe one, the carbonizing rice hull fuel gas conveying pipe connected with the vent cavity when at least a a 2 a h, the air conveying pipeline connected with the air in time and at least a is 2 a entrance. The mixing cavity is cone section shape. A wall of the ignition cavity equipped with electronic ignition device. The utility model is new type can be effective when a rice hull smoldering of a flammable gas and full use, supplying using the burner for heating a foam heat preservation material, a waste use, and saves the production cost.
NOVELTY - The new type utility claims the domestic garbage into a coal and system, comprising orderly connected and set with filter device, drying device, a carbonization device and mixing device, a drying device and a carbonizing device also at the same time connected with smoke sum processing device, screen device comprises orderly equipped with a plate feeding machine, a magnetic separator, a sieve, a winnowing machine, a belt machine and crushing machine, drying device composed of a dry spiral feeder by a drying device, drying by a swing cylinder, a burner and air blower composed of a carbonizing device for carbonizing machine, carbonizing machine by a carbonization combustion room composed of a mixing device composed of a mixing spiral feeder by a stirrer, fume processing device composed of a cyclone dust collector by a spray dust remover. The utility model is new type household garbage processing into coal supply system and solves the existing second time pollute is serious, harmful gas and excess land occupying the more the problem better and protect the environment, reduce the occupying of a land.
NOVELTY - The utility model is new type relates to a kind integrated biomass carbonizing device, comprising a bracket equipped with a bracket a and a carbonization, carbonization with a feedstock in a upper part and a lower part of the out coal wherein, carbonizing a outside wall face is provided with a heating ring, wherein also a spiral discharging machine, a cooling and filtering a, spiral discharging machine on out a coal carbonization of a lower part of a cooling exhaust pipe and a carbonizing a connected, a sum and a a connected pipe, internal cooling is a multiple of a cooling pipe, a cooling set with a water inlet and a water outlet of the cooling pipe connected, under the cooling part provided with a tar outlet, a filter and discharge tube connected, a filter is provided with a filter object. Biomass coal from the discharge spiral conveying mechanism, a taking carbon, production efficiency high, the safety is good, cooling a tar from a fume and separation, realize the recovery of tar using; after filtering a gas to carry out a purification again outward discharge, discharge accord with a heat preservation requirement, protect the environment.
NOVELTY - The utility model is new type relates to a kind a pushing horizontal biomass carbonizing device, comprising foundation bed and a carbonization, carbonizing at a is equipped with a feed port, wherein also comprising power source and heat source, carbonizing a horizontal mounting on a substrate, a carbonizing terminal is provided with a pressing block, a power drive pressing block used for heating carbonizing a along axial direction moving back and forth, a source of a carbonizing in a carbonizing a, another a carbonization of a connected memory material tank, material tank into a cooling tank, material with a discharging box and a cooling box outside, material box and smoke connected. A carbonizing a horizontal installation, length may not be limit, is also very suitable, by pushing a pushing to carbonizing a raw material, a raw material pressure a compare, timing can be automatically quantitative feedstock, automatic degree high, large yield and high efficiency.
NOVELTY - The new type utility claims carbonizing rice hull combustion and combustion gas gas using device, a rice shell carbide combustion device, a cyclone de-dusting tower and a burner, the carbonizing rice hull combustion device by the following material open hopper, combustion chamber and ash hopper composed of the following. Between the cyclone de-dusting tower and burner in turn equipped with dripping water washing tower and condenser, the front end of the burner set with blower blowing the combustion chamber and the middle periphery a set 4 of observation hole, when a can observe the carbonizing rice hull condition within the combustion chamber, a what can be when carrying out the ash. Rear cover plate of said observation hole is the inverted door. The utility model is new type gas can be effective when a hull of a of a reflectance of no utility of some components, a large amount of carbon monoxide and methane gas, again for use, using a burner. And the device can be advantageously of a combustion exhaust gas to prevent these gas pollute air, has a very strong;
NOVELTY - The new type utility claims one kind dry coal dust gasification furnace, a combustion room, chilling room and, in a chilling room provided with a chilling ring and at least one of the second chilling ring, for a product from a combustion room and a spray, chilling, the utility new type equipped with a chilling ring and the position is higher than the tube lower end, thus can protect the first ring pipe by the throat pipe is led out from the raw gas and molten directly impact the ash, keeping a longer life, and also can be as a ring pipe and lower part has cooling protection effect, effective preventing the second ring pipe happen deformation or breakage under a high warm gas and impact of molten slag.
NOVELTY - The utility model claims a new one of gasification furnace feedstock system and coal gasification system, relating to coal gasification technology area, can solve the gasification furnace feedstock and gasification furnace system stability of coal gasification system compare the difference problem. The gasification furnace feedstock system comprises raw material gas supply system, the raw material gas supply system input end is provided with multiple raw material gas input pipeline for one of multiple combustion in gasification furnace and is corresponding connected with the nozzel, and each of the raw material gas output pipeline of are provided with limiting flow component. This new utility model providing the gasification furnace system for gasification furnace feedstock of feedstock, this utility new type of coal gasification system for providing coal gasification process and hydrogenation solid coal powder.
NOVELTY - The new type utility claims carbonizing rice hull fuel gas removing tar condensing device, a gas entrance pipeline, a condenser tube, turn chamber and fuel gas outlet pipe, a condenser tube is a thin middle thick and two spindle. Inner cavity and a condenser tube set with multiple air thin pipe, the air pipe and the gas entrance pipe connected, and removing air thin pipe outside the condenser tube and the fill. Upper end of the condenser tube opening connected with the cooling liquid in the pipeline, relative side opening connected with the cooling liquid out pipe. The coke oil gas and gas the utility new type can be effective when a hull of a reflectance of a liquefying, sum and liquid separation, to obtain relative pure of carbon monoxide and methane mixed gas. The utility model is new type avoids the combustion waste gas direct discharge to prevent these gas pollute air, has a very strong;
NOVELTY - The apparatus (100) is configured to produce current to fuel cell stack (110) by using signal current in which ripple current is generated when changed to on-state. An inductor (130) reduces specific resistance value of signal current to specific resistance value during off-state. A control unit (170) produces impedance of fuel cell stack by using current and voltage of fuel cell stack.    USE - Apparatus for production of injection current for fuel cell stack.    ADVANTAGE - The apparatus is enabled to reduce the heat loss by current flowing using the inductor, and the square wave of signal current is filtered effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for production of injection current for fuel cell stack.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit block diagram of the apparatus for production of injection current for fuel cell stack. (Drawing includes non-English language text)    Apparatus for production of injection current for fuel cell stack (100)    Fuel cell stack (110)    Inductor (130)    Current sensor (160)    Control unit (170)
NOVELTY - The apparatus has a control unit for producing impedance of a fuel cell stack by using current of voltage of the fuel cell stack. A current calculating unit produces current of the fuel cell stack by using stack current that is applied from the fuel cell stack. A voltage calculation unit produces voltage of the fuel cell stack by using stack voltage that is applied from the fuel cell stack. The voltage calculation unit produces voltage level of the fuel cell stack. Multiple harmonic distortion modules are provided in a control unit.    USE - Fuel cell stack trouble diagnosis apparatus.    ADVANTAGE - The apparatus produces the current value of the fuel cell stack by using the current calculating unit based on current value of the fuel cell stack, so that exact impedance can be implemented by using the current value of the fuel cell stack.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel cell stack failure diagnostic method.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit block diagram of a fuel cell stack trouble diagnosis apparatus.'(Drawing includes non-English language text)'
NOVELTY - Manufacture of softwood cone complexing agent involves crushing mastic, dissolving in organic solvent, filtering, concentrating, obtaining concentrated solution, diluting the resultant product using ethanol, adding softwood, and drying the resultant product.    USE - Manufacture of softwood cone complexing agent (claimed).
NOVELTY - The system has sealed pyrolysis chamber which contains conveying surface (32). Processing stations are provided with piston positioned in opening of chamber above conveying surface. The pistons are connected to driver located external to chamber. The driver is capable of moving the pistons in and out of contact with the conveying surface. A heater is provided for heating portion of conveying surface. A drive motor is located external to chamber to drive conveying surface. A vapor exhaust port directs vapors from chamber.    USE - System for performing biomass fractioning.    ADVANTAGE - The conveying surface system with interlocked tracks and overlapping side walls effectively contains the biomass during processing and is easier to clean than standard systems allowing for longer processing times without clogging. The current system provides efficient biomass delivery system within the pyrolysis chamber that allows for complete processing of the biomass and reduces the chance that the biomass residue clogs the system, thus preventing system shutdown. Thus, the unnecessary wear is prevented on the motors due to the harsh environment of the pyrolysis chamber and the overall efficiency of the system is increased by eliminating down time from failed motors or excessive maintenance in efficient manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) an apparatus for fractioning biomass; and    (2) a method for converting biomass to bio-oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the combining process of biomass fractionators onto to trailer or skid.    Bio-fractionator unit (30)    Conveying surface (32)    Crank shaft (33)    Catalyst system (34)    Separator (35)
NOVELTY - The fire starting device (21) has a housing which is provided with an open top end and an open bottom end. The housing is comprised with an interior volume for holding combustible materials (24). Several openings are formed on the housing. Several ridges are formed on the cylindrical housing. The housing is provided with several side walls, and folded so as to form a pentagon when viewed from the top. Each opening is formed to be rectangular or circular in shape.    USE - Fire starting device for use in outdoor environment e.g. campfire and indoor environment.    ADVANTAGE - The fire starting device increases the air flow and the air circulation so as to facilitate lighting and burning of the fire. The ease of lighting the fire is increased. The fire starting device is utilized for lighting indoor and outdoor fires. The fire starting device is fabricated from materials that permit relative economy and are commensurate with durability.    DETAILED DESCRIPTION - The fire starting device comprises an elongated panel (22) having several sections connected to one another in a side-by-side orientation. The panel is arranged in a wrapped configuration to form a geometric shape. The geometric shape comprises a defined interior volume for holding combustible materials. The panel is provided with several openings (23). An INDEPENDENT CLAIM is included for a method of starting fire involves placing a fire starting device in the center of several fire logs. The combustible materials held within the fire starting device are ignited. An oxidizer is supplied to fuel a fire.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the fire starting device.    Fire starting device (21)    Elongated panel (22)    Opening (23)    Combustible material (24)    First end of elongated panel (25)
NOVELTY - Invention relates to a water electrolytic generator for producing a mixture of hydrogen and oxygen via water electrolysis with flame treatment of materials, bipolar or monopolar-bipolar, having a housing with an electrolyte, a block of spaced-apart electrodes immersed in the electrolyte, said electrodes having openings for passage of the hydrogen-oxygen mixture and the electrolyte, and conductors for transmitting current to the electrodes. Said electrode block is placed in a tube made of dielectric material which encloses the electrodes without spacing around the periphery, one current-conducting wire connected to the electrode at the centre of the block and the other to both end electrodes.    USE - Chemistry.    ADVANTAGE - Use of the present invention enables to stabilise the composition of the electrolyte in the block, eliminate counterflow of gas or liquid in the electrode block, solves the problem of cracking due to triaxial expansion.3 cl, 1 dwg
NOVELTY - Processing pineapple leaf and stem involves harvesting and cutting the leaf and stem of the pineapple by mowing process. Mowed parts of pineapple are crushed to obtain fine particle. Obtained particles of pine-apple are reduced to obtain reduced product. Fermentation is carried out to form organic fertilizer.    USE - Method of processing pineapple leaf and stem used for producing organic fertilizer (claimed).    ADVANTAGE - The method enables to process pineapple leaf and stem in a cost-effective manner and prevents the acidification of field.
NOVELTY - The biogas installation has bioreactor that is concentrically with cylindrical container for arrying out psychrophilic step of the anaerobic digestion of biomass. The mesophilic step is performed at middle and thermophilic step at last. A pump is set to supply the feedstock. A substrate is set under the container. A system is set to clean, collect, store and process the biogas. The external and central sections have blade agitator devices. A central section has dosed SHF-heating unit which are arranged evenly.    USE - Biogas installation for uniform distribution of SHF energy.
NOVELTY - Bioreactor comprises cylindrical stainless steel body divided by internal walls into four chambers, boot and drain risers, stirrer drive, gas collector pipeline, and heat exchanger with heat-insulating layer.    USE - The bioreactor is useful for production of biogas (claimed).    DETAILED DESCRIPTION - Bioreactor comprises cylindrical stainless steel body divided by internal walls into four chambers, boot and drain risers, stirrer drive, gas collector pipeline, and heat exchanger with heat-insulating layer. The bioreactor is additionally supplied with device for stabilizing the temperature of biomass, which contains centrifugal and circulation pumps, reagent dispenser, buffer tank, and switchgear device for connecting conduit for reagent with valves and nozzles. The suction portion of the centrifugal pump is placed at the top of the fourth chamber of bioreactor. The centrifugal pump discharge nozzle is connected to the first inlet buffer tank, and second inlet is connected to reagent dispenser. The output buffer tank is connected through the connecting pipe and the circulating pump with distribution device, which through pipes and valves are connected to nozzles arranged in the bottom of the first, second and third chambers.
NOVELTY - A water-treatment chemical agent comprises greater than or equal to 1 type of chemical species which produces in water greater than or equal to 1 ion chosen from iron ion, manganese ion, copper ion, zinc ion and molybdenum ion, ion and greater than or equal to 1 type of chelating agent which can form chelate compound.    USE - A chemical agent used for water treatment process (claimed) of organic waste water.    ADVANTAGE - Aerobic treatment is performed efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a water-treatment process which adds water-treatment chemical agent to organic waste water and carries out aerobic treatment of organic waste water.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the confirmed trace element and effect of chelating agent. (Drawing includes non-English language text).
NOVELTY - Carbon dioxide is dissolved in a dispersion liquid containing micro algae and shearing force is applied to the mixture to crush micro algae, using high pressure dispersion apparatus. Lipid is extracted from the mixture at 0-45 degrees C under absolute pressure of 0.08-0.5 MPa.    USE - Extraction of lipid from algae (claimed). Uses include but are not limited to biofuel, biodiesel fuel, raw material for cosmetics chemical products and pharmaceuticals, and functional food.    ADVANTAGE - The method enables efficient extraction of lipids from algae.
NOVELTY - A droplet or emulsion PCR mixture comprises an aqueous droplet comprising a PCR mixture; an oil phase; and a surfactant.    USE - The droplet or emulsion PCR mixture is used for the amplification and detection of nucleic acid sequences in integrated microsystems.    ADVANTAGE - Provided are low cost and environment-friendly methods, devices and systems for emulsion/droplet PCR.    DETAILED DESCRIPTION - A droplet or emulsion PCR mixture comprises an aqueous droplet comprising a PCR mixture; an oil phase; and a surfactant having Formula I: R-(OCH2CH2)n-OH.    R=alkyl group consisting of 12-18 carbons; and    n=2-25.    INDEPENDENT CLAIMS are:    (1) a method for preparing a mixture for droplet or emulsion PCR by forming an aqueous droplet comprising a PCR mixture; surrounding the aqueous droplet with an oil phase; and adding a surfactant having Formula I described above; and    (2) a method for determining the capability of a surfactant for droplet or emulsion PCR by preparing an aqueous solution comprising polymerase; preparing an oil phase comprising a surfactant; forming a hanging drop of the aqueous droplet in the oil phase; and measuring a property of the hanging drop.
NOVELTY - A graphene supported platinum-cobalt alloy nanoparticles composite catalyst comprises platinum-cobalt alloy nanoparticles with particle size of 2-10 nm, and graphene dispersed in carrier surface, is new.    USE - Graphene supported platinum-cobalt alloy nanoparticles composite catalyst for use in alkaline or acidic medium of the oxygen reduction reaction (claimed)    ADVANTAGE - The catalyst has very high electric catalytic activity and stability and better performance than commercial platinum/carbon catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the preparation of the catalyst..
NOVELTY - Preparation of vegetable fungicide involves mixing microorganism, perlite powder and calcium carbonate powder, adding binder, obtaining microorganism sustained release agent, adding diniconazole, methylene diphenyl diisocyanate, methyl-benzimidazole-2-amino carboxylate and acetone to a reactor, heating, adding polyvinyl alcohol, maintaining at room temperature for 3 hours, filtering, obtaining polymer sustained release agent, mixing polymer sustained release agent and microorganism sustained release agent, adding surfactant, water retention agent and anti-freezing agent, and mixing.    USE - Preparation of vegetable fungicide (claimed).    ADVANTAGE - The method enables preparation of environmentally-friendly and nontoxic vegetable fungicide having excellent sterilization effect, and suppressed residue content.
NOVELTY - Manufacturing organic fertilizer involves utilizing plant fiber, poultry excrement, microorganism strain and earthworm. Plant fiber is cooked at pressure of 70-120 kilopascals for 10-30 minutes, and then crushed through 30-80 meshes, preferably 50 meshes into powder. Base material is mixed with microorganism strain in ratio of 1:100 to carry out expanding culture. Powder, pig manure and peptone are mixed in ratio of 1-3:1-2:4-8, and then cultured by mixing microorganism strain at 22-30 degrees C for 5-10 days.    USE - Method for manufacturing organic fertilizer used for plant (claimed).    ADVANTAGE - The method enables to manufacture organic fertilizer in a simple and cost-effective manner. Organic fertilizer improves soil fertility and looses soil.    DETAILED DESCRIPTION - Manufacturing organic fertilizer involves utilizing plant fiber, poultry excrement, microorganism strain and earthworm. Plant fiber is cooked at pressure of 70-120 kilopascals for 10-30 minutes, and then crushed through 30-80 meshes, preferably 50 meshes into powder. Base material is mixed with microorganism strain in ratio of 1:100 to carry out expanding culture. Powder, pig manure and peptone are mixed in ratio of 1-3:1-2:4-8, and then cultured by mixing microorganism strain at 22-30 degrees C for 5-10 days. Earthworm is mixed with cultured product, and then fermented at 15-25 degrees C for 20-50 days, preferably 36 days at room temperature. The fermented product is filtered, granulated, dried and packaged.
NOVELTY - Preparing bio-organic fertilizer involves utilizing 20-90 parts industrial fermentation waste residue, 1-2 parts Bacillus subtilis, 3-4 parts silicate bacteria, 2-4 parts green Trichoderma viride, 2-5 parts actinomycetes, 2-4 parts Azotobacter chroococcum, 10-13 parts active material, 1-2 parts Bacillus megaterium, 8-12 parts Lactococcus lactis, 1-2 parts glial Bacillus, 10-20 parts straw, 3-6 parts Escherichia coli, 8-12 parts cellulose, 5-6 parts phosphorylase and 8-12 parts protease.    USE - Method for preparing bio-organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare bio-organic fertilizer that provides nutrition to plant.    DETAILED DESCRIPTION - Preparing bio-organic fertilizer involves utilizing 20-90 parts industrial fermentation waste residue, 1-2 parts Bacillus subtilis, 3-4 parts silicate bacteria, 2-4 parts green Trichoderma viride, 2-5 parts actinomycetes, 2-4 parts Azotobacter chroococcum, 10-13 parts active material, 1-2 parts Bacillus megaterium, 8-12 parts Lactococcus lactis, 1-2 parts glial Bacillus, 10-20 parts straw, 3-6 parts Escherichia coli, 8-12 parts cellulose, 5-6 parts phosphorylase, 8-12 parts protease, 2-5 parts Lactobacillus plantarum, 3-9 parts Bacillus licheniformis and 20-30 parts phosphatase. Industrial fermentation waste residue is mixed with straw, and then supplying illumination intensity of 3500-3700 lumen for 7 hours. The product is sealed in a plastic film, and then sterilized to obtain product with moisture content of 40-60%. Microorganisms are mixed and stirred uniformly, and then mixed with the product to carry out fermentation process for 3 days.
NOVELTY - Liquid fertilizer comprises 1-10 pts. wt. edible white granulated sugar, 1-50 pts. wt. edible brown sugar, 1-10 pts. wt. soybean powder, 1-3 pts. wt. xanthan gum, 1-5 pts. wt. modified starch, 1-2 pts. wt. sucrose ester, 0.01-0.03 pts. wt. high temperature starch liquefaction enzyme, 0.001-0.003 pts. wt. sodium pyrophosphate, 0.01-0.05 pts. wt. dipotassium hydrogenphosphate, 73-95 pts. wt. purified water, 0.01-0.02 pts. wt. Lactobacillus bulgaricus and 0.01-0.02 pts. wt. Streptococcus thermophilus.    USE - Liquid fertilizer used for improving saline soil (claimed).    ADVANTAGE - The liquid fertilizer is suitable for wide application.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing liquid fertilizer, which involves;    (A) mixing edible white granulated sugar, edible brown sugar, soybean powder, xanthan gum, modified starch, sucrose ester, high temperature starch liquefaction enzyme, sodium pyrophosphate, dipotassium hydrogenphosphate and purified water in a homogenizer to obtain suspension;    (B) heating obtained mixture to obtain culture medium that is cooled to 35-40 degrees C; and    (C) fermenting culture medium with Lactobacillus bulgaricus and Streptococcus thermophilus for 48 hours to obtain liquid fertilizer that is split-charged and stored.
NOVELTY - Organic fertilizer is prepared by aerobic fermentation of 25-45 pts. wt. animal bone powder, 25-30 pts. wt. livestock and poultry excrement, 20-25 pts. wt. furfural residue, 3-5 pts. wt. urea, 1-2 pts. wt. microbial inoculum, 4-8 pts. wt. potassium sulfate and 2-5 pts. wt. caking agent.    USE - Organic fertilizer used for salty or saline soils.    ADVANTAGE - The organic fertilizer is prepared in a simple and cost-effective manner and enriched with calcium, and increases disease resistance of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) mixing animal bone powder, livestock and poultry excrement, furfural residue and microbial inoculum and drying to adjust water content to 50-60%;    (B) adding urea and potassium sulfate with the mixture, crushing and sieving with sieve of 0.5 mm to adjust water content to 20-30%; and    (C) mixing caking agent with the mixture, and then granulating.
NOVELTY - Preparation of n-butanol involves forming reaction mixture comprising ethanol, hydrogen, water and acetaldehyde, and contacting the reaction mixture with Guerbet catalyst in reactor (40) at 50-450 degrees C and 10-200 bar. The n-butanol yield based on ethanol is 10-35%. The selectivity to n-butanol is 65-95%. The mole ratio of hydrogen to ethanol is 0.1:1-5:1. The mole ratio of acetaldehyde to ethanol is 0.001:1-0.1:1. The mole ratio of water to ethanol is 0.05:1.    USE - Preparation of n-butanol used in gasoline engine of car.    ADVANTAGE - The method enables preparation of n-butanol having excellent green replacement for gasoline, with high yield of 90-95% and selectivity of 75% or more.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of preparation of n-butanol.    Ethanol feed (1)    Feed stream (15)    Reactor (40)    Molecular sieve (80)    Water rich feed stream (88)
NOVELTY - Method of planting Sorghum, involves performing seed treatment, then planting seed in a field, performing field management and finally applying fertilizer, where the fertilizer comprises 2-2.2 pts. wt. Bacillus subtilis, 0.2 pts. wt. Actinomycete, 0.2 pts. wt. nitrogen source, 0.2 pts. wt. Bacillus mucilaginosus, 2 pts. wt. diatomite, 1 pt. wt. spice powder, and further includes indole acetic acid, potassium sulfate, magnesium vitriol, zinc vitriol, alpha -naphthalene acetic acid sodium, sodium EDTA chelating agent and humic acid.    USE - The method is useful for planting Sorghum (claimed).    ADVANTAGE - The method improves the yield of Sorghum plant.
NOVELTY - A chub fish cultivation method involves constructing rectangular ponds, sterilizing ponds with quicklime, and injecting sterile lake or river water into the pond. The pond is added with stocked young fishes and added with green fodder. Water management is performed by providing oxygen for every two hours a day, replacing the water every single week of 1/3, adding coarse salt to the water, adding pond plants, followed by catching 2000 g fish every month.    USE - Method for cultivation of chub fish.    ADVANTAGE - The method enables cultivating chub fish with increased survival rate and quality in safe, environmentally-friendly and cost-effective manner.    DETAILED DESCRIPTION - A chub fish cultivation method involves constructing rectangular ponds with effective farming area of ??13-17 acres, depth of 2 m and thickness of 0.2 m of silt, controlling surrounding pollution, and supporting the pond with power aerator and 1 unit 3 kW automatic feeding machine. The pond is sterilized with 150 g quicklime, kept in sun for two weeks, injected with sterile lake or river water into the pond through inlet filter of 70-80 meshes silk yarn, stocked young fishes are soaked in 3% salt water for 10 minutes, and added into the pond. The chubs are added with green fodder once a day, where the ratio of feed and forage is 7:3 and the feed is provided once every two weeks in winter with a feeding quantity of 2-3%. Water management is performed by providing oxygen for every two hours a day, replacing the water every single week of 1/3, adding coarse salt to the water, ensuring the temperature of water at 18-25 degrees C, sprinkling lime per month, adding pond plants at a content of 10-15 kg/acre for every two months followed by catching 2000 g fish every month.
NOVELTY - The device has a sealed medicine box provided with a floating plate. A bottom part of the medicine box is provided with multiple drug release ports. A bottom end of an automatic release mechanism is connected with a fish luring device. A side of the medicine box is provided with a motor that drives a rotating turbine. The automatic releasing mechanism is provided with a sealing plate. An upper part of a fixing plate is formed with multiple holes. An upper end of the medicine box is connected with an elastic element i.e. spring.    USE - Fish cultivation pond dosing device.    ADVANTAGE - The device performs automatic fish disease recognition process so as to dose traditional Chinese medicine liquid. The device is simple in structure. The device reduces pollution of pond water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fish cultivation pond dosing device.
NOVELTY - A pig cultivating method involves manufacturing piggery by providing adequate sunlight and ventilation to piggery, and separating a fermentation bed house and a cement house. Fermentation bed manufacturing process is performed by paving mixture on a bottom layer, a tree leaf layer, a first layer and a second layer. The pig is placed in the cement house during pregnancy, breeding and fattening period, and is placed in fermentation bed during production period, nursing period and breeding period, and spraying disinfectant.    USE - Method for cultivating pig.    ADVANTAGE - The method enables cultivating pig with improved production and zero sewage discharge, enhanced disease resistance, increased feeding efficiency and meat quality, rapid healthy grow in cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - A pig cultivating method involves manufacturing piggery by providing adequate sunlight and ventilation to piggery, and separating fermentation bed house and cement house, where the fermentation bed is utilized as a low floor type structure, and has groove height of 90-100 cm. Fermentation bed manufacturing process is performed by mixing straw, rice hull, sawdust, tree leaves, rice bran, peanut shell, fungus and beneficial microorganism, paving the mixture on a bottom layer, a tree leaf layer, a first layer and a second layer, where the thickness of bottom layer is 30-50 cm, leaf layer is 10-12 cm, the first layer is 10-30 cm and the second layer is 10-30 cm. The pig is placed in the cement house during pregnancy, breeding and fattening period, and placed in fermentation bed during production period, nursing period and breeding period, and spraying disinfectant into the fermentation bed house and slightly turning second fermentation layer 1-2 times every day.
NOVELTY - Biogas fermenter comprises feed tube (11), discharge tube (12), U-type pipe (20), discharge tube drainage holes (30), discharge hole (32), vent (40) and manifold (50). Biogas fermentation and accumulation is carried out in U-type pipe. Inflow pressure in the feed pipe drainage hole maintains uni-direction in the fermenter. Water pressure is provided in the storage tank to maintain the reflux and biogas slurry circulation.    USE - Biogas fermenter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biogas fermenter.    Feed tube (11)    Discharge tube (12)    U-type pipe (20)    Discharge tube drainage hole (30)    Discharge hole (32)    Vent (40)    Manifold (50)
NOVELTY - Ultra-efficient biogas generating device comprises feeding pipe (11) for feeding raw material in U-type pipeline (20) to generate marsh gas, where space is present between feeding pipe blocking plate (26) and material-blocking plate to accommodate marsh gas. A collecting pipeline is provided to allow flow of fermentation material of the feeding tube and discharge pipe (12) into drainage holes (28). Drainage holes are provided to allow unidirectional flow of slurry to discharging pipe, where methane fermentation pressure in pipeline drops manifold upon storage.    USE - Ultra-efficient biogas generating device used for promotion of biogas slurry circulation and biogas generation (claimed).    DESCRIPTION OF DRAWING(S) - The drawing illustrates a schematic view of ultra-efficient biogas generating device.    Feeding pipe (11)    Discharge pipe (12)    U-type pipeline (20)    Feeding pipe blocking plate (26)    Drainage holes (28)
NOVELTY - Production of compound fertilizer granules comprising plasticizing raw material mixture, extruding and rubbing, cutting into strips or tablet, granulating, and squeezing.    USE - Method for production of compound fertilizer granules (claimed).    ADVANTAGE - The method obtains uniform particle size, rounded appearance, more accurate nutrient and improved storage properties compared to prior art, and it has simple process which eliminates the need for drying, screening and breaking large particles, reduced emissions and overall energy consumption, and improved workshop environment compared to conventional agglomeration process.
NOVELTY - A composite organic fertilizer comprises 20-60 pts. wt. potassium sulfate complex fertilizer, 40-55 pts. wt. crop straw, 20-30 pts. wt. livestock and poultry excrement, 0.01-0.03 pt. wt. VT-1000 type fermenting bacteria, and 0.1-0.3 pt. wt. caking agent.    USE - Composite organic fertilizer used for fruit trees (claimed).    ADVANTAGE - The fertilizer contains large amount of organic substances and microorganisms, has high usage rate, and increases quality and yield of fruit tree and soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite organic fertilizer comprising adding livestock manure, crop straw and VT-1000 type fermenting bacteria to mixing tank, heating at 80 degrees C plus minus 5 degrees C for 2 hours, stir-fermenting for 3-6 days, stacking for 3-7 days, and turning; adding complex fertilizer, mixing, stirring, crushing, steaming, granulating, drying, cooling, and sieving; and adding caking agent and coating.
NOVELTY - A composite organic fertilizer comprises 10-15 pts. wt. nitrogenous fertilizer, 40-55 pts. wt. crop straw, 20-30 pts. wt. livestock and poultry excrement, 0.01-0.03 pt. wt. VT- 1000 type fermenting bacteria, and 0.1-0.3 pt. wt. caking agent.    USE - Composite organic fertilizer used for vegetables (claimed).    ADVANTAGE - The fertilizer contains large amount of organic substances and microorganisms, has high usage rate, and increases quality and yield of vegetables and soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite organic fertilizer comprising adding livestock manure, crop straw and VT-1000 type fermenting bacteria to mixing tank, heating at 80 degrees C plus minus 5 degrees C for 2 hours, intermittent stir-fermenting for 3-6 days, stacking for 3-7 days, and turning; adding nitrogenous fertilizer, mixing, stirring, crushing, steaming, granulating, drying, cooling, and sieving; and adding caking agent and coating.
NOVELTY - A special fertilizer comprises 1000-1200 g dairy manure, 100-120 g licorice, 70-80 g corn straw, 50-60 g cottonseed, 50-60 g beer, 10-15 g organic fertilizer leavening agent, 10-15 g organic fertilizer synergistic agent, 20-30 g ammonium sulfate, 25-35 g urea, 30-40 g calcium superphosphate, 30-35 g potassium sulfate, 4-6 g copper sulfate, 40-50 g ferrous sulfate, 5-10 g pesticide, 3-5 g nano carbon, 10-15 g sepiolite, 3-6 g chitosan, 3-4 g Eucalyptus oil, 2-3 g propylene glycol alginate, and 4-5 g sodium metasilicate.    USE - Special fertilizer used for Photinia serrulata (claimed).    ADVANTAGE - The fertilizer is rich in organic matter, nitrogen, phosphorus, potassium and trace elements, prevents iron deficiency and pest, ensures bright appearance of Photinia serrulata making it more suitable for viewing.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer comprising taking cow dung, hay, straw, cottonseed, beer, and organic fertilizer leavening agent, crushing, adding remaining raw materials, stirring, fermenting, and mixing.
NOVELTY - The kiln has a vertical rotating rubbish gasification furnace connected with an air outlet of a kiln body. A feed port of a rubbish gasification furnace is connected with an outlet of a rubbish conveying device. The rubbish conveying device is provided with a rubbish material inlet. A rubbish material shed is fixed with a rubbish grab bucket device. A furnace cover is fixed on a cylindrical furnace body. Bottom of the furnace body is provided with a slag funnel. A side wall of the furnace body is equipped with a supporting part.    USE - Domestic rubbish gasification cement kiln.    ADVANTAGE - The kiln simplifies gasification process, reduces processing cost, avoids assistant fuel and ensures rubbish feeding homogeneity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a rubbish gasification cement kiln operating method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a domestic rubbish gasification cement kiln.
NOVELTY - The method involves preparing a fluidization bed. Oxidation-reduction reaction is generated by a gasification medium. Biomass fuel gas conveying function is determined. A biomass raw material is pre-heated by a pre-heater through the gasification medium. Dust and tar of biomass fuel gas are removed by a drying part. The biomass raw material is conveyed to the fluidization bed through a spiral feeder after pre-heating the biomass raw material. The biomass fuel gas is filtered from conveying gas by a combustion device.    USE - High-efficient fluidization bed biomass gasification and purification method.    ADVANTAGE - The method enables carrying out cooling of the biomass fuel gas of the fluidization bed, increasing energy utilization rate and gasification efficiency, reducing investment and operation cost of a gasification device and labor intensity and removing tar and dust of the biomass fuel gas so as to reach effective purification of goal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a high-efficient fluidization bed biomass gasification and purification device.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a high-efficient fluidization bed biomass gasification and purification device.'(Drawing includes non-English language text)'
NOVELTY - The method involves generating biomass pyrolysis and gasification biomass fuel gas. Biomass fuel gas burning process is performed to generate kiln furnace supply heat. High-warm smoke sum is generated by the kiln furnace supply heat according to the biomass pyrolysis. Water steam is generated. A high-warm gas medium is obtained according to the biomass fuel gas.    USE - Industrial kiln furnace biomass gasification combustion supply heating method.    ADVANTAGE - The method enables increasing system stability and heating efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating an industrial kiln furnace biomass gasification combustion supply heating method.
NOVELTY - The device has a reaction furnace part (1) provided with a reaction cell, a purification channel (2) and a gas outlet (3). The purification channel is connected with a bottom part of the reaction cell. The gas outlet is located in a top part of the purification channel. An inner side part of the purification channel is fixed with an atomizing spray device to control fuel gas flow direction. A mounting sleeve (4) is provided with an air inlet unit that is fixed on a wind box (5). A bottom part of the reaction furnace part is fixed with an ash room (9).    USE - Biomass fuel gas furnace purification device.    ADVANTAGE - The device improves quality of a biomass fuel gas furnace and increases biomass fuel gas furnace purification efficiency, and has convenient operation and wide application range.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass fuel gas furnace purification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a biomass fuel gas furnace purification device.    Reaction furnace part (1)    Purification channel (2)    Gas outlet (3)    Mounting sleeve (4)    Wind box (5)    Ash room (9)
NOVELTY - Purifying biodiesel involves mixing cellulosic material clay, adding crude biodiesel to obtained mixture, and then conveying the mixture into a mixer through a conveyor. The mixture is processed in a reaction tank at 50-70 degrees C for 10-20 minutes, and then high fibrous material, clay and crude biodiesel are added to processed material. The mixture is kept in a settling tank for certain time period to obtain precipitate. The precipitate is processed with sunflower oil, cypress seed oil, hempseed oil or Camellia oil to obtain the desired product.    USE - Method for purifying biodiesel (claimed).    ADVANTAGE - The method enables to purify biodiesel in a simple, eco-friendly and cost-effective manner.
NOVELTY - Producing biodiesel involves utilizing hydrogen to perform hydrogenation reaction with cultured oil-producing microalgae cells. The obtained product is subjected to purity analysis to obtain high-quality biodiesel as the finished product.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method enables to produce biodiesel in simple and environment-friendly manner.
NOVELTY - A fluorescent carbon point nano probe producing method involves weighing 5 g litchi nucleus in a crucible, heating in a muffle furnace at 300 degrees C for 2 hours and removing. The obtained product is put into a grinding pot for grinding. 20 ml pure water is added, ultrasonic treatment is performed for 30 minutes, filtered and centrifuged at 10000 rpm for 10 minutes. The upper layer clear liquid is taken and stored at 4 degrees C.    USE - Method for producing fluorescent carbon point nano probe that is utilized for detecting methylene blue and live cell fluorescence imaging (claimed).    ADVANTAGE - The probe can be prepared with high selectivity, in a simple, cost-effective, eco-friendly and rapid manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) use of a fluorescent carbon point nano probe for detecting methylene blue by utilizing phosphate buffer solution with a pH of 8, where the methylene blue response speed is 5 minutes, fluorescence quenching value reaches 80%, the detection limit of methylene blue is low as 0.05 mu mole/l and the linear response range is 0.8-10 mu mole/l    (2) use of a fluorescent carbon point nano probe in the detection of live cell imaging applications by adding 80 mu g/ml probe to the fluorescence cell culture dishes, incubating the cells for 6 hours, 12 hours, 24 hours, washing the cells with phosphate-buffered saline to remove non-entry into the cell of cluster of differentiation and observing the cells continued to emit blue fluorescence by utilizing laser confocal microscope system.
NOVELTY - Fractionating (40) oilseed dry cake comprises: crushing (410) oilseed cakes into a powder of ultrafine particles, triboelectrostatic charging (420) of the ultrafine particles of the powder, and deviating (425) path through the electric field of the charged particles to sort the particles and provide at least a fraction enriched in lignocellulose.    USE - The method is useful for fractionating oilseed dry cake which is useful for: obtaining fractions enriched in lignocellulose, fractions enriched in protein, and fractions rich enriched in polysaccharides; generating biofuel and biogas from fractions enriched in lignocellulose; and extracting phenolic derivatives from lignin-enriched fractions (all claimed), where the biofuel is biohydrogen and/or bioethanol.    ADVANTAGE - The method: provides separation of fibers and proteins in oilcakes without altering their structures and functional properties; and allows a user to adjust the fineness of grind based on crushed oilcake and quality of the desired sorting.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart for fractionating oilseed dry cake.    Fractionating oilseed dry cake (40)    Crushing oilseed cakes (410)    Triboelectrostatic charging of the ultrafine particles (420)    Deviating path through the electric field (425)    Purifying enzymes of the sorted particles (430)
NOVELTY - Modular system comprises a biomass receiving container with at least one annular side wall (5) and a roof structure arranged on the wall, a waterproof layer (9') arranged inside the container and a gas storage film (9) arranged above the roof structure. At least one waterproof layer is connected in an air tight manner. At least one part of the container is formed with a recess (2) embedded in the ground (6). The edge of the recess is embedded into the ground via an annular bottom anchoring e.g. a foundation, which is arranged with the annular side wall.    USE - The modular system is useful for preparation of a biogas fermenter (claimed).    ADVANTAGE - The modular system: has easy and simple construction; has reliable operation and maintenance; and is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparation of a biogas fermenter with at least one container system comprising at least one container having at least one space for receiving biomass, a roof structure and at least one gas storage film, installing a recess having trapezoidal cross section, at the edge region of the annular side wall, designing earth recess together with the annular side wall internally set with a film layer, installing at least one support element on the roof structure for supporting, and arranging gas storage film above the roof structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the modular system for preparation of a biogas fermenter.    Recess (2)    Annular side wall (5)    Ground (6)    Gas storage film (9)    Waterproof layer (9')
NOVELTY - The new type utility claims a marsh gas a concentrated vitriol..... Anaerobic reactor, raw biogas sum from entrance of Anaerobic reactor entrance to c, from Anaerobic reactor in a process wherein after the exit and entrance to flow out in a biological desulfurization reactor, after processing is finished and in the biological desulfurization reactor to enter into a film..., also comprising one energy using device, a receiving the biological desulfurization reactor is a product. The novel utility of effective solves the problem that the methane (natural gas) by-product treatment, total vulcanization hydrogen removing rate of desulphurization is more than 99%. Vulcanization hydrogen content in a gas is more than 5000 ppm under condition, out of vulcanization hydrogen content in sum less than 200mg/l; thio acid through thin film filter, a c a certain concentration.
NOVELTY - The utility model is new type provide a easy to carry out operation and a low cost of using sludge to prepare combustion coal... A. using sludge to prepare combustion coal of a sludge storage chamber, auxiliary agent adding device, adding device, a stirrer and forming finished product transfer device, sludge storage chamber, auxiliary agent adding device and agent adding device are a feeding end of a stirrer, a discharging end of a finished product mixer forming transport device, sludge storage cabin sludge conveying device connected the feeding terminal, a sludge conveying device of stirring machine has a sludge metering l of auxiliary agent adding device comprises storage tank, storage tank by conveying a connection auxiliary agent measuring l; between combustion improver added device comprises combustion chamber, combustion chamber a combustion-supporting agent delivery device connected the feeding terminal, conveying device and combustion chamber of a combustion improver metering l mixer.
NOVELTY - The utility model is new type relates to a kind mobile biology diesel oil preparation device, a biological energy source technology field. The utility model is new type comprises main body system, a system, a pump, stirring system and storage tank system. The utility model is new type by push rod, a roller and a design assist reaction raw material tank, a the device at any time and any place all a process in the biological diesel oil, and project each of a pump and control system in a process complete, precise, design of waste water tank a production of waste water can obtain collective treatment to avoid discharging place then cause second time pollute; the device using flexible, suitable operation, biological diesel oil high quality, is a glycerol, clean and environment-friendly.
NOVELTY - The new type utility claims a plant containing a biological diesel oil of a raw material, a biological energy source technology field, the utility model is new type device comprising a reactor, heater, heating oil circulation pump, product separator, flash evaporator, auxiliary raw material inlet, material inlet, a slag discharging port, material plate, a clapboard, a material plate rotate, an overflow port, insulating layer, heating plate pipe, the internal reactor provided with one or more of a material plate, a material fixing plate is provided with a more than one of a material fixing plate is provided with an overflow port, the overflow wherein a lower layer containing material fixed bed, outside the reactor provided with insulating layer, internal insulating layer in a spiral around the around the reactor in the heating coil, heating two end plate of a connecting tube and a bottom heating oil circulation pump and heater, reactor through crude product separator and a flash evaporator. A biological diesel oil raw material oil by extraction of a biological diesel oil preparation process of organic combined, increase the efficiency, reducing the production cost, a process is simple, the equipment investment cost low, a clean, with environment friendly character.
NOVELTY - The utility model is new type relates to a seaweed cultivation and planting biology diesel oil extracting integrated device, belongs to biological diesel oil extraction equipment technology field. The utility model is new type comprises alginate culture, collection tank,, separating machine, reaction tank and water tank of sodium alginate culture a culture box I, box II culture, culture tank I of the alginate culture, culture tank II respectively connecting the collection tank through pipe I and pipe II, a collection tank outlet through pipeline III., press outlet through pipeline IV. separating machine, separating machine outlet through a pipeline V connected the alginate culture, and the other outlet through pipeline VI... tank, reaction tank surface has a separate water pipe, water pipe and water pipe head... connecting pipe II, the other head connecting a water inlet pipe II, water tank with insulating layer periphery, out water tube I and water tube II.; the water inlet pipe I, a water inlet pipe II are connect water tank. The utility model is new type of alga high yield, clean, heat utilize rate high, using suitable.
NOVELTY - Production of biological organic fertilizer comprises taking fresh wet feces, Enterococcus faecium AnP01 with greater than or equal to 2x 108 colony forming unit/g viable cells and yeast liquid with greater than or equal to 5x 108 colony forming unit/g viable cells at weight ratio of 8000-12000:1:1, mixing fresh wet feces and Enterococcus faecium AnP01, dissolving in water to obtain component A, mixing fresh wet feces and yeast liquid, dissolving in water to obtain component B, mixing two components, primary fermenting at 35-40 degrees C for 12-24 hours, stirring, secondary fermenting at 25-40 degrees C and crushing.    USE - Method for producing biological organic fertilizer (claimed).    ADVANTAGE - The method has improved decomposition of lignin and cellulose, and inhibits proliferation of pathogenic bacteria.
NOVELTY - Synthesis of 2-amino nicotinic acid (III) comprises adding 2-chloro-3-trichloromethyl pyridine (I) and ammonia into autoclave, heating, incubating, removing excess ammonia, washing solid with water, filtering, and low-temperature drying to obtain 2-amino-3-trichloromethyl pyridine (II); and adding alkali solution, heating, dehydrating, adjusting pH with hydrochloric acid, filtering white solid, and drying.    USE - Method for synthesis of 2-amino nicotinic acid (claimed).    ADVANTAGE - The method is environment-friendly, achieves product purity of up to 97% and total yield of up to 89.2%, and it has inexpensive raw materials.    DETAILED DESCRIPTION - Synthesis of 2-amino nicotinic acid of formula (III) comprises adding 2-chloro-3-trichloromethyl pyridine of formula (I) and ammonia at molar ratio of 1:3 into autoclave, heating to 35-80 degrees C, incubating for 5-15 hours, removing excess ammonia, washing solid with water, filtering, and low-temperature drying to obtain 2-amino-3-trichloromethyl pyridine of formula (II); and adding alkali solution at molar ratio of 1:1-5, heating to 30-90 degrees C to carry out hydrolysis for 2-6 hours, dehydrating, adjusting pH to 3-5 with hydrochloric acid, filtering white solid, and drying.
NOVELTY - Gel type alcohol fuel composition comprises 90-98 pts. wt. 1-6C lower alcohol, 0.5-2.5 pts. wt. thickener, and 0.3-3.5 pts. wt. polyoxyethylene alkyl amine neutralizing agent with 17-30 degree of polymerization on ethylene oxide.    USE - Used as gel-type alcohol fuel composition.    ADVANTAGE - The composition has excellent storage stability and gelation stability, and is easy to process in cost effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing gel type alcohol fuel composition, comprising (a) adding, mixing and stirring lower alcohol and thickener in general stirrer equipped with a condenser, (b) transferring into a container and mixing, (c) introducing neutralizing agent into the container and stirring at a high-speed stirrer, and (d) producing the del in the container, and sealing the container.
NOVELTY - Roasting of carbonaceous feedstock (1) involves drying carbonaceous feedstock, roasting the dried carbonaceous feedstock, producing roasting gases (8) and roasted biomass (3), and regenerating portion of the roasting gases combustion process for producing combustion gas (13) at 700 degrees C or more. Portion of recycled gas is mixed with gaseous effluent. The temperature of the gaseous mixture recycled in the drying process is 200-900 degrees C.    USE - Roasting of carbonaceous feedstock used for producing biofuel such as gasoline and diesel, and electricity.    ADVANTAGE - The method enables economical roasting of carbonaceous feedstock, using filler having increased moisture content, without changing the time of charge flow, minimizes drying gas flow without changing quality or hourly throughput of the treated filler, and reduces drying loop, in order to reduce space.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the explaining the roasting process.    Feedstock (1)    Roasted biomass (3)    Roasting gases (8)    Fuel (9)    Combustion gas (13)    Heat exchanger (C)
NOVELTY - A Planifilum fistulosum, is new. The P.fistulosum has (a) iso C15:0, iso C16:0, C16:0 and iso C17:0 as main fatty acid components, (b) alanine, glutamic acid, and meso diaminopimelic acid (meso-DAP) as amino acid composition of cell-wall peptidoglycan, and (c) MK7 as main menaquinones.    USE - The P.fistulosum is used for processing organic waste, preferably excrement, organic sludge, foodstuff residue, or animal excrement (all claimed).
NOVELTY - The utility model is new type A is a organic fertilizer manufacture device, has a rolling fermentation tank, auxiliary material adding device, drying device and extruding device, the rolling tank. rolling tank comprises a machine frame, a rolling tank is fixed above a machine frame, a rolling tank is...... rolling tank bottom through conduit and auxiliary material adding device connected, the auxiliary material adding device comprises auxiliary material adding pipe, stirring tank and a stirrer, the auxiliary material adding pipe is set above a stirring tank, a stirrer set at bottom of stirring tank, the auxiliary material adding device and macroscopic device between has a conduit, bottom of said drying device set has blanking and extruding device is connected, the extruding device comprises extruding machine and a chute, the extrusion and a extruder, the discharging groove at the tail part is equipped with a press, the novel organic fertilizer making machine comprises using is simple, production efficiency high, and the quality is high.
NOVELTY - The new type utility claims a organic fertilizer bi-direction side. Turning, comprising: box body and a main shaft, a turning bottom turning main shaft tank body located on the front, the middle part of main shaft turning to turn the main shaft provided with a shifting material leaves the paddle rotating shaft, two side turning shaft is provided with a spiral stirring blade, shifting material paddle leaf above the inner box body set with lifting belt, lifting two rows of blocking plate on conveyor belt provided with interval is set with lifting a turning upper layer is set with conveying belt with guide shaft, the lower turning lower part provided with a wheel lifting conveyor below the top part provided with lateral conveying belt; a box body lifting conveyor is located right ahead is provided with material input window. The utility model is new type of beneficial effect as follow: through set with blocking plate of lifting conveyor and capable of bi-direction transmission side of material transfer with mutually matched, which can realize a resistance of a fertilizer and improve working efficiency of side turning Turning.
NOVELTY - The utility model is new type of intelligent high warm environment-friendly manufacturing fertilizer, comprising a fermentation chamber and main shaft transmission device and the connection of turning, lifting device, high pressure wind device, deodorizing device, a fermentation cabin provided with feeding and discharging wherein wherein, air inlet pipe and discharge pipe of lower end of upper end, main shaft transmission device comprises installation provided with several turning on a centre stirring shaft, stirring shaft centre of the vertical direction in a fermentation chamber transverse stirring shaft, high pressure wind device comprises a air inlet pipe in the fermentation chamber is a wind of high pressure fan, deodorizing device in a deodorizing tank, deodorizing tank discharge pipe... a chamber has a plurality of a smell, and also set with tank. pneuma tube. The utility model is new type convenient use,. drying effect is good, uniform stirring, and effectively solves the problem that the traditional technique small square meter a large problem. Fermentation condition rapidly reaches a warm a low to ensure continuous production a warm environment below.
NOVELTY - The new type utility claims a. organic fertilizer production line, a press process in turn comprises pulverizer, fermentation pool, a granulator, dryer, a cooling machine, machine, a sieving and metering split charging machine,... a dumper provided with a push machine turn across a pool at the under frame and... one walking wheel frame, the front of walking wheel.. two row set, two walking wheel of interference fit connection method for installation in a double end rotating shaft, a first rotating shaft by mounting the frame on the electric machine drive, a first rotating shaft axial direction are cloth has a multi-turning machine, multi-stirring claw of the turning machine by set rotating shaft outside and b and the same rotating shaft is set a shaft direction are set is one cloth. Front two rows of walking wheel is driving wheel drives the frame forward, at the same time turning mechanism is also the rotating shaft turning for the first fermentation compost in a process of turning, without a need to operate, can finish the turning, turning uniformity, fermentation, organic fertilizer nutrient.
NOVELTY - Organic composite fertilizer comprises 30-50 pts. wt. rotten fruits and vegetables, 10-15 pts. wt. dry dairy manure, 12-15 pts. wt. biological bone material, 12-14 pts. wt. straw powder, 25-30 pts. wt. ammonium sulfate, 15-17 pts. wt. zinc sulfate, 15-18 pts. wt. grass carbon, 15-16 pts. wt. boric acid, 30-35 pts. wt. calcium superphosphate and 40-50 pts. wt. bentonite.    USE - Organic composite fertilizer used for cultivating grape seedling (claimed).    ADVANTAGE - The organic composite fertilizer ensures easy absorption, improved soil, provides nutrient to grape seedling, reduced cultivating cost, increased survival rate and reduced atmosphere and soil pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic composite fertilizer, which involves:    (A) fermenting rotten fruits and vegetables for 10-13 days;    (B) filtering fermented material;    (C) drying filtered residue for 30-45 minutes;    (D) grinding dried materials;    (E) mixing and grinding biological bone material and straw powder to obtain fine powder;    (F) mixing ground materials and obtained fine powder to obtain mixed powder material;    (G) mixing obtained materials with ammonium sulfate, zinc sulfate, grass carbon, boric acid, monoammonium phosphate, calcium superphosphate and bentonite; and    (H) pelletizing obtained mixture in a pill machine to obtain product.
NOVELTY - Powder additive comprises 60-63 wt.% organic selenium source, 7-9 wt.% nano-chitosan, 3-5 wt.% protein, 3-5 wt.% inorganic selenium source, 5-6 wt.% kudzu root, 2-3 wt.% vitamin C, 3-5 wt.% organic iron source and 10-12 wt.% chestnut powder.    USE - Powder additive used for planting selenium-enriched edible fungus (claimed) for production of food.    ADVANTAGE - The powder additive facilitates long-term preservation of selenium-enriched edible fungus, and has slow release effect.
NOVELTY - Fertilizer comprises 15-20 pts. wt. garden soil, 10-15 pts. wt. pulp and paper sludge, 5-8 pts. wt. sawdust, 6-10 pts. wt. pumice, 8-12 pts. wt. urea, 5-10 pts. wt. phosphoric acid, 0.5-1 pts. wt. molybdenum sulfate, 0.1-0.5 pts. wt. zinc sulfate, 5-10 pts. wt. water retention agent, 10-15 pts. wt. deionized water, 1-3 pts. wt. microorganism and 2-5 pts. wt. nitrogen-fixing bacteria.    USE - Fertilizer used for planting (claimed).    ADVANTAGE - The fertilizer ensures enriched nutrients, is non-toxic and eco-friendly, protects crop, looses soil, and has improved stress resistance, water retaining and ventilation properties.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) mixing garden soil, pulp and paper sludge, sawdust and pumice to obtain a product;    (B) mixing remaining components, and then mixing obtained product;    (C) performing fermentation of then mixture at 45 degrees C with maintaining air humidity 40-45% for 1-2 days in a fermentation tank;    (D) fermenting obtained product by covering through plastic film at 50 degrees C; and    (E) cooling the product, and then drying and crushing to obtain fertilizer.
NOVELTY - Fertilizer comprises 50-60 pts. wt. dry pond mud powder, 40-50 pts. wt. straw, 10-20 pts. wt. bamboo, 10-30 pts. wt. longan shell, 12-18 pts. wt. prepared Rehmannia rhizome, 4-9 pts. wt. Celastrus, 1-5 pts. wt. green Artemisia and 2-6 pts. wt. radix sophorae flavescentis.    USE - Fertilizer used for fruit (claimed) and growth of crop.    ADVANTAGE - The fertilizer is eco-friendly, and ensures insect repellent and insect disease-resistant properties.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) grinding crop straw powder, longan shell and Celastrus by a pulverizer, and then mixing crushed bamboo and pond mud powder;    (B) adding remaining components with the mixture, and then fermenting by addition of water (10 times) in a fermentation tank for 15 days; and    (C) stirring the product uniformly to obtain the fermentation product, drying it in shade, and then packaging to obtain final product.
NOVELTY - Compound fertilizer comprises 30 pts. wt. pig viscera, 15 pts. wt. tobacco stick, 20 pts. wt. mushroom residue, 20 pts. wt. sawdust, 20 pts. wt. peanut, 15 pts. wt. bagasse, 20 pts. wt. plant ash, 30 pts. wt. turves, 8 pts. wt. shrimp powder, 10 pts. wt. sweet potato powder, 10 pts. wt. urea, 10 pts. wt. brown sugar, 8 pts. wt. ferric oxide, 10 pts. wt. potassium dihydrogen phosphate, 5 pts. wt. ferrous sulfate, 30 pts. wt. chicken manure, 40 pts. wt. human excrement, 20 pts. wt. fly ash and 3 pts. wt. trace element.    USE - Compound fertilizer used for growing flowers and trees (claimed).    ADVANTAGE - The compound fertilizer ensures enriched organic nutrient and long-acting, increases survival rate of trees without damaging leaves and flowers, and improves quality of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing compound fertilizer, which involves:    (A) heating pig viscera at 85-95 degrees C, adding aqueous bone slurry and crushing to obtain mixture;    (B) crushing other components, and then mixing and stirring with 30 wt.% water;    (C) performing fermentation of the product at 40-45 degrees C for 7 days in a fermentation tank; and    (D) cooling the fermentation product, drying, and then packaging.
NOVELTY - Organic composite fertilizer comprises 3-5 pts. wt. chicken manure, 4-5 pts. wt. dairy manure, 12-15 pts. wt. bone material, 10-15 pts. wt. green vegetable leaf, 12-14 pts. wt. wood powder, 18-22 pts. wt. ammonium sulfate, 18-22 pts. wt. ferrous sulfate, 18-22 pts. wt. urea, 18-22 pts. wt. boric acid and 18-22 pts. wt. monoammonium phosphate.    USE - Organic composite fertilizer used for planting blueberry.    ADVANTAGE - The organic composite fertilizer ensures easy absorption, improved soil, reduced breeding cost and increased survival rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic composite fertilizer, which involves:    (A) fermenting mixture of chicken manure, cow dung and green vegetable leaves for 3-7 days;    (B) fermented materials;    (C) drying filtered residue for 30-45 minutes;    (D) grinding dried materials to obtain powder;    (E) grinding remaining materials; and    (F) mixing obtained powders and ground materials to obtain organic composite fertilizer.
NOVELTY - Compound fertilizer comprises 100-150 pts. wt. cattle and sheep manure, 5-20 pts. wt. urea, 1-10 pts. wt. calcium superphosphate, 1-10 pts. wt. bamboo carbon powder, 1-5 pts. wt. boric acid, 1-2 pts. wt. ferrous sulfate, 1-2 pts. wt. zinc sulfate, 1-2 pts. wt. sodium selenite, 0.5-2 pts. wt. potassium dihydrogen phosphate and 0.1-0.5 pts. wt. ammonium molybdate.    USE - Compound fertilizer used for increasing flavone content of tartary buckwheat (claimed).    ADVANTAGE - The compound fertilizer improves soil quality and economic benefit by increasing total yield of 160 kilograms/micron dosage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing compound fertilizer, which involves:    (A) mixing Bacillus subtilis, Bacillus megaterium and Rhizobium and sterilizing at 120 degrees C for 20 minutes to prepare culture medium;    (B) mixing and stirring Tween with bacterial mixture in ratio of 100:1 for 10 minutes, and then standing for 4-7 days;    (C) mixing remaining components with culture medium, and then fermenting and centrifuging with speed of 3000-4000 revolutions per minute at 35-40 degrees C for 10-30 minutes; and    (D) drying the product in air for 10-20 hours, and then crushing through 200 mu aperture sieve to obtain product.
NOVELTY - A municipal sewage sludge energy-saving environment-friendly treatment method comprises adjusting weight ratio of raw materials and moisture content of municipal sewage sludge to 70-85%, mixing, placing into fermentation equipment at vertical direction, performing dynamic aerobic fermentation, and dehydrating until moisture content is 50% or less.    USE - Method for municipal sewage sludge energy-saving environment-friendly treatment (claimed).
NOVELTY - A biodegradable sludge composting conditioner comprises organic conditioner and sludge compost at mass ratio of 1:4-10.    USE - Biodegradable sludge composting conditioner.    ADVANTAGE - The biodegradable sludge composting conditioner can effectively improve sludge pile structure, improves efficiency of oxygen diffusion, can be recycled, and it has high mechanical strength and water absorption, reduced dosage fresh conditioners and sludge disposal costs, and no residue and secondary pollution. The method promotes compost maturity, and it has short fermentation cycle, reduced odor, and smooth fermentation process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biodegradable sludge composting conditioner comprising mixing raw materials, and molding to room temperature at 2-150 MPa into sphere, cuboid or cylinder shape.
NOVELTY - A bioactive fertilizer comprises maggot, parasitic pathogen microorganism, and organic material. The parasitic pathogen microorganism is Metarhizium, Bassiana and/or Bacillus thuringiensis. The organic material is manure having humidity of 20-40% and/or high-temperature treated dead livestock having humidity of 20-40%. The high-temperature treated dead livestock is prepared by heating dead livestock to remove hair, cutting, and high-temperature sterilizing.    USE - Bioactive fertilizer, i.e. powder or granules (all claimed) used for high standard organic agriculture, environment-friendly agriculture and pollution-free agriculture.    ADVANTAGE - The bioactive fertilizer has high protein, improves soil fertility, promotes plant growth, and it has killing larvae and reducing pests effect, and simple method which can improve the efficiency of agricultural production and farmer's income.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of bioactive fertilizer comprising mixing organic material into wet and dry mixing tank, pumping maggot, dehydrating, adjusting humidity to 8-12%, controlling temperature to 20-30 degrees C until spore releases parasitic pathogenic microorganism for 5-7 days, and adjusting humidity to 3-6%.
NOVELTY - Harmless processing of sludge compost comprises mixing dewatered sludge and wood chips at weight ratio of 40-45:55-60, adding 20-25 wt.% Bacillus natto, rice bran, Trichoderma and Azotobacter at weight ratio of 2:2:1:1, stirring, and fermenting to 35-40 degrees C for 5-7 days.    USE - Method for harmless processing of sludge compost (claimed).    ADVANTAGE - The method can adjust the bacteria group.
NOVELTY - A tea tree organic fertilizer comprises 100-200 pts. wt. chicken manure, 100-120 pts. wt. rapeseed cake, 50-80 pts. wt. peanut meal, 5-8 pts. wt. bone powder, 0.3-0.5 pt. wt. decomposing inoculant, 0.3-0.6 pt. wt. Trichoderma harzianum, 0.5-0.8 pt. wt. Bacillus megaterium, 0.2-0.4 pt. wt. potassium bacteria, and 0.3-0.5 pt. wt. nitrogen-fixing bacteria.    USE - Tea tree organic fertilizer used for increasing growth speed.    ADVANTAGE - The fertilizer solves problem such as difficult absorption of large amount of nitrogen-phosphorus-potassium elements and increases absorption of nutrient elements.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer comprising taking chicken manure, bone powder and part decomposing inoculant and fermenting for 15-20 days; taking rapeseed cake, peanut meal, and remaining decomposing inoculant and fermenting for 10-15 days; and mixing fermented components and adding remaining raw materials.
NOVELTY - Mountain tea tree fertilizer additive comprises 10-15 pts. wt. organic matter, 4-6 pts. wt. humic acid, 6-10 pts. wt. minerals, 0.3-0.5 pts. wt. microorganism, 4-7 pts. wt. slow release agent, and 2-3 pts. wt. plant antivirus agent.    USE - Mountain tea tree fertilizer additive.    ADVANTAGE - The additive solves the problem of low soil organic matter content and soil compaction.
NOVELTY - Preparation of organic fertilizer comprises mixing animal excrement and corn powder, spraying microorganism on mixture, uniformly stirring, adding water to a moisture content of 50-65%, spreading mixture on fermentation pool to a thickness of 30 cm, putting animal carcass to a thickness of 30 cm, anaerobically fermenting for 20-35 days; sprinkling 30% formaldehyde aqueous solution, uniformly stirring, sealing for 5-10 hours, adding urea, stirring for 50-90 minutes; granulating, and drying.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The fertilizer has low energy consumption, low cost, and less environment pollution.
NOVELTY - Mesorhizobium huizhouense (RITF711), having a preservation number CCTCC NO: M2014354, is new.    USE - Mesorhizobium huizhouense (RITF711) is useful for preparing nitrogen-fixing microbial inoculum or bioorganic fertilizer (claimed).    ADVANTAGE - Mesorhizobium huizhouense has strong 1-aminocyclopropane-1-carboxylate (ACC) deaminase activity, and improves Acacia tree growth and stress resistance.
NOVELTY - Rhodopseudomonas palustris strain LY-1 having a preservation number of CCTCC M 2014524, is new.    USE - The biocontrol agent is useful for promoting growth in tobacco plants, and preventing and treating tobacco mosaic virus (claimed).    ADVANTAGE - The method is economical, produces non-toxic materials, and thus it is environmental friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (I) Rhodopseudomonas palustris strain LY-1-containing biocontrol agent; (II) Rhodopseudomonas palustris strain LY-1-containing biocontrol agent; and (III) preparing Rhodopseudomonas palustris strain LY-1-containing biocontrol agent, comprising (i) activating Rhodopseudomonas palustris strain LY-1 by culturing the strain by double plate culture process, and culturing until the single colonies appear red-color, (ii) adding red single colonies into a serum bottle-containing photosynthetic bacteria liquid culture medium, and culturing until the cells reach logarithmic growth phase, to obtain bacteria liquid, (iii) adding 5% photosynthetic bacterial liquid into total volume of a flask, and inoculating, and culturing photosynthetic bacteria, to obtain logarithmic growth phase microbial inoculums, and (iv) centrifuging cultured microbial inoculums, precipitating, and sterilizing by using sodium chloride solution, re-suspending, to obtain bacterial suspension, and finally obtaining the product.
NOVELTY - 5-acetamido-N,N'-bis(2,3-dihydroxypropyl)-2,4,6-triiodoisophthalamide (Compound (A)) is produced by (i) reacting 5-amino-N,N'-bis(2,3 -dihydroxypropyl)-2,4,6-triiodoisophthalamide with mixture acetic anhydride/acetic acid to form slurry, (ii) heating slurry to 60 degrees C, (iii) adding acid catalyst to slurry at a rate such that reaction temperature is maintained at 65-85 degrees C, (iv) adding deactylating agent to form reaction mixture comprising Compound (A), and (v) purifying reaction mixture by (vi) passing reaction mixture comprising Compound (A) through membrane filtration system.    USE - Production of 5-acetamido-N,N'-bis(2,3-dihydroxypropyl)-2,4,6-triiodoisophthalamide for iodixanol and iohexol production used as non-ionic X-ray contrast agents.    ADVANTAGE - The process has increased product yield and reduced energy consumption and process time, resulting in reduced overall costs.    DETAILED DESCRIPTION - 5-acetamido-N,N'-bis(2,3-dihydroxypropyl)-2,4,6-triiodoisophthalamide (Compound (A)) is produced by (i) reacting 5-amino-N,N'-bis(2,3 -dihydroxypropyl)-2,4,6-triiodoisophthalamide with mixture acetic anhydride/acetic acid to form slurry, (ii) heating slurry to 60 degrees C, (iii) adding acid catalyst to slurry at a rate such that reaction temperature is maintained at 65-85 degrees C, (iv) adding deacetylating agent to reaction mixture to form reaction mixture comprising Compound (A), (v) purifying reaction mixture by (vi) passing reaction mixture comprising Compound (A) through membrane filtration system, (vii) collecting retentate, and repeating step (v), and (viii) continuously repeating steps (v)-(vii).
NOVELTY - This utility new type relates to a gas treatment field, specifically in caprolactam production, referring to a condenser and a gas treatment device comprises the condenser is. This utility new type example provide the one a condenser, a single sealing head. The upper tube plate and lower tube plate tube and respectively and one side between upper pipe plate and lower pipe plate is welding, another side on tube plate and end enclosure is fixedly connected, another side and a nozzle lower plate is fixedly connected, the utility model is new type example provide a condenser of a gas treatment device, a top has emptying wherein is equipped with tertiary butyl alcohol tank, sealing head condenser is equipped with gas absorbing bucket and the first pipeline of water, another side lower plate and a vent is tertiary butyl alcohol tank fixedly connected, upper head of single sealing head equipped with condenser has gas phase outlet, gas phase outlet through a pipe and gas absorbing bucket connection. Can be a gas, which avoids pollute environment, reduce the energy waste of effect.
NOVELTY - A micro-ecological biological fertilizer comprises 13-26 pts. wt. plant Lactobacillus, 10-16 pts. wt. Aspergillus niger, 1-5 pts. wt. glue mass bud holding Bacillus, 1-3 pts. wt. large bud holding Bacillus, 8-15 pts. wt. Bacillus subtilis fungus powder, and 1-3 pts. wt. Aspergillus awamori culture.    USE - Micro-ecological biological fertilizer.
NOVELTY - Preparing fermented animal serum involves heating raw material containing sodium selenite, animal blood hydrolyzed liquid, composite trace element, potassium dihydrogen phosphate, urea, peptone, yeast powder, sodium chloride, sodium hydroxide, sodium nitrate, ammonium chloride, dipotassium phosphate, beef extract, glucose, starch, calcium carbonate, amino acid, potassium nitrate, ferrous sulfate, vitriol, citrate and enzyme at 75-80 degrees C for 8-15 hours to obtain mixture. Hydrolase is added into mixture and then heated at 120 degrees C for 1-2 hours to obtain hydrolyzed liquid.    USE - Method for preparing fermented animal serum used for preparing fertilizer for crop such as grape, apple, pumpkin, pepper, cucumber, cabbage rape, tomato and eggplant (claimed).    ADVANTAGE - The method enables to prepare fermented animal serum that is rich in selenium.    DETAILED DESCRIPTION - Preparing fermented animal serum involves heating raw material containing sodium selenite, animal blood hydrolyzed liquid, composite trace element, potassium dihydrogen phosphate, urea, peptone, yeast powder, sodium chloride, sodium hydroxide, sodium nitrate, ammonium chloride, dipotassium phosphate, beef extract, glucose, starch, calcium carbonate, amino acid, potassium nitrate, ferrous sulfate, vitriol, citrate and enzyme at 75-80 degrees C for 8-15 hours to obtain mixture. Hydrolase is added into mixture and then heated at 120 degrees C for 1-2 hours to obtain hydrolyzed liquid. Bacillus amyloliquefaciens, Bacillus licheniformis and Bacillus thuringiensis are added into hydrolyzed liquid to obtain the product.
NOVELTY - Bio-fertilizer comprises 400 pts. wt. inorganic fertilizer, 0.4 pts. wt. Bacillus amyloliquefaciens liquid, 0.4 pts. wt. Bacillus licheniformis liquid, 0.2 pts. wt. Bacillus subtilis liquid, 0.05-0.10 pts. wt. skimmed milk powder, 1.10-1.26 pts. wt. silicon dioxide particles obtained through 600 meshes, 0.2-0.4 pts. wt. iron oxide particles obtained through 200 meshes, 1.8-3.6 pts. wt. calcium carbonate, 2 pts. wt. glycerol. Inorganic fertilizer is present in granular form comprises 45% nitrogen-phosphorus-potassium.    USE - Bio-fertilizer.    ADVANTAGE - The bio-fertilizer ensures high inorganic content i.e. nitrogen, phosphorus and potassium content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-fertilizer, which involves:    (A) fermenting Bacillus amyloliquefaciens by using a culture medium containing sterile 4.0-4.5 pts. wt. bean flour, 2.6-3.0 pts. wt. corn powder and 0.42-0.50 corn powder glucose in a fermentation tank at 32-37 degrees C with rotating speed of 180 revolutions per minute;    (B) fermenting Bacillus subtilis by using a culture medium containing sterile 2.0-2.5 pts. wt. starch, 3.0-3.2 pts. wt. peptone, 2.1-2.5 pts. wt. beef extract, 3.5-3.8 pts. wt. glucose and 1.8-2.4 pts. wt. sodium chloride in a fermentation jar at 35-37 degrees C with rotating speed of 200 revolutions per minute;    (C) fermenting Bacillus licheniformis by using a culture medium containing sterile 3.2-3.6 pts. wt. cottonseed, 2.0-2.5 pts. wt. corn powder, 0.50-0.55 pts. wt. glucose, 0.80-1.20 pts. wt. sodium chloride and 1.0-1.2 pts. wt. potassium dihydrogen phosphate in a fermentation tank at 32-37 degrees C with rotating speed of 200 revolutions per minute; and    (D) mixing fermented liquids with remaining components and then stirring uniformly, and then packaging to obtain final product.
NOVELTY - Method for producing drug-eluting stent, involves (a) storing biodegradable polymer and drug in solution storing portion, (b) checking alignment of injector or collection portion in x, y and z directions, (c) injecting the solution stored in the solution storing portion using the injector, and (d) repeating steps (b) and (c), where the stent further comprises heating unit in the solution storing portion, and floating device.    USE - The method is used for producing drug-eluting stent (claimed).
NOVELTY - Bio-organic fertilizer comprises 25-35 pts. wt. traditional Chinese medicinal residue, 15-25 pts. wt. fat residue, 15-25 pts. wt. rabbit manure, 8-12 pts. wt. wheat bran, 8-12 pts. wt. humic acid, 8-12 pts. wt. mushroom residue, and 1% microbial cultures.    USE - The bio-organic fertilizer is useful for potted flowering bonsai plants in homes (claimed).    ADVANTAGE - The bio-organic fertilizer is environmentally-friendly as compared to existing fertilizers, provides good fertilization effect and required amount of essential nutrients to soil holding the bonsai plants, prevents lack of nutrients in bonsai pots, has no toxicity, high quality and low cost, and enables human to create green and better environment in their living rooms.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation method of the above-mentioned bio-organic fertilizer, which involves weighing the above-mentioned raw materials in the above-mentioned weight proportions, mixing weighed raw materials uniformly except microbial cultures, crushing obtained mixture into fine powder, adding the fine powder to a tank, spraying water and microbial cultures into the tank, maintaining water content of 30-50% in obtained mixed material, fermenting and decomposing the mixed material at 55-60 degrees C, and obtaining fully decomposed fermented product.
NOVELTY - Production method of golden needle mushroom involves using 60-70 pts. wt. old golden needle mushroom, 5-10 pts. wt. young corn cob, 1.5-2 pts. wt. soybean flour, 2-3 pts. wt. saw dust, 0.5-1 pt. wt. calcium superphosphate and 0.5-1 pt. wt. sugar.    USE - Production method of golden needle mushroom using old golden needle mushroom (claimed).    ADVANTAGE - The produced golden needle mushroom contains nutrients and variety of organic matter e.g. glucose and amino acid from old golden needle mushroom. Survival rate of mushroom is promoted, and environmental pollution and production cost are reduced, as old golden needle mushroom is fully utilized.
NOVELTY - Cordate Houttuynia special fertilizer comprises 24-26 pts. mass straw, 18-20 pts. mass white clover, 10-12 pts. mass sesame straw, 5-7 pts. mass pumpkin vine, 8-10 pts. mass mulberry leaf, 7-9 pts. mass lees, 11-13 pts. mass potassium sulfate, 6-8 pts. mass copper sulfate, 7-9 pts. mass zinc sulfide, 3-5 pts. mass polyaspartic acid, 2-4 pts. mass decomposed crop straw, 4-6 pts. mass phosphate-solubilizing bacteria type fertilizer, 2-4 pts. mass forchlorfenuron, 3-5 pts. mass ammonium citrate and 60-70 pts. mass water.    USE - Cordate Houttuynia special fertilizer used for promoting growth of Cordate Houttuynia.    ADVANTAGE - The cordate Houttuynia special fertilizer has simple preparation, low cost and increased utilization rate, improves Cordate Houttuynia blade thickness and promotes complete absorption of nitrogen, phosphorus and potassium elements.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cordate Houttuynia special fertilizer comprising taking straw, white clover, sesame straw, pumpkin vine, mulberry leaf and lees, adding into pulverizer, crushing to 40 mesh to obtain mixture A, adding mixture A with potassium sulfate, copper sulfate, zinc sulfate, polyaspartic acid, decomposed crop straw, phosphate-solubilizing bacteria type fertilizer, forchlorfenuron, ammonium citrate and water, uniformly stirring, standing, sealed fermenting for 7 days, drying, granulating and obtaining the product.
NOVELTY - Producing special fertilizer, by (a) drying Salix branches, pulverizing, and passing through 80 mesh sieve, (b) taking cow dung, pig manure, chicken manure and river mud, drying, mixing with product obtained in step (a), composting, drying, inoculating bacterial strain, fermenting, drying, crushing, and passing through 120 mesh sieve, and (c) crushing cowherb seed, radix stemonae, Sophora subprostrata and cortex mori radicis to 120 mesh powder, adding silicon fertilizer, mixing with product obtained in step (b), and granulating the mixture.    USE - The method is used for producing special fertilizer (claimed).    ADVANTAGE - The produced fertilizer improves fertility and structure of soil.    DETAILED DESCRIPTION - Method for producing special fertilizer, involves (a) drying Salix branches until moisture content reaches 22-30%, pulverizing, and passing through 80 mesh sieve, (b) taking cow dung, pig manure, chicken manure and river mud, drying until moisture content reaches 85-100%, mixing with product obtained in step (a), composting at 110-130 degrees C for 30-50 minutes, drying until moisture content reaches 65-80%, inoculating 0.8-2 pts. wt. bacterial strain, fermenting at 15-25 degrees C for 15-20 days, drying at 25-60 degrees C until moisture content reaches 28-35%, crushing using mill, and passing through 120 mesh sieve, and (c) crushing cowherb seed, radix stemonae, Sophora subprostrata and cortex mori radicis to 120 mesh powder, adding silicon fertilizer, mixing with product obtained in step (b), and granulating the mixture, where the fertilizer comprises 22-28 pts. wt. cow dung, 35-40 pts. wt. pig manure, 15-20 pts. wt. chicken manure, 18-25 pts. wt. river mud, 25-30 pts. wt. Salix branches, 15-18 pts. wt. silicon fertilizer, 1-2.5 pts. wt. cowherb seed, 2-5 pts. wt. radix stemonae, 0.8-2 pts. wt. S.subprostrata and 5-8 pts. wt. cortex mori radicis.
NOVELTY - A vegetable organic fertilizer comprises 800-1000 pts. wt. chicken manure, 200-300 pts. wt. plant ash, 200-300 pts. wt. rice straw, 80-100 pts. wt. soybean meal, 25-30 pts. wt. urea, 6-10 pts. wt. potassium dihydrogen phosphate, 4-6 pts. wt. formaldehyde, and 3-5 pts. wt. dazomet.    USE - Vegetable organic fertilizer (claimed).    ADVANTAGE - The vegetable organic fertilizer is clean, rich in nutrients, economical, and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of vegetable organic fertilizer.
NOVELTY - Washing composition for pesticide residue comprises 4.75-5.25 wt.% sodium hypochlorite, 24.035-26.565 wt.% sodium dichloroisocyanurate, 14.63-16.17 wt.% scavenger, 38.57-42.63 wt.% purifying agent, 3.04-3.36 wt.% potassium permanganate and 9.975-11.025 wt.% fatty alcohol polyoxyethylene ether. The raw material is stirred in a stirrer to obtain pesticide.    USE - Washing composition for removing pesticide residue .
NOVELTY - Cultivation of straw mushroom includes mixing cotton seed hulls, straw, bran and lime, adjusting pH, placing into bags, sterilizing, and cooling to obtain culture medium; high-temperature sterilizing linen cloth, placing bedding fabric into ground, placing sterile bags, covering with sterile linen cloth, cooling, and inoculating fungi; digging furrow, placing inoculated fungi into tubes, putting into furrow, covering with thick soil, adjusting pH, and covering tube; and cultivating.    USE - Method for cultivation of straw mushroom (claimed).    ADVANTAGE - The method is environment-friendly, and it has effective sterilization process, low cost, and high survival rate.    DETAILED DESCRIPTION - Cultivation of straw mushroom comprises:    (A) mixing 55-75 wt.% cotton seed hulls, 10-30 wt.% straw, 10-20 wt.% bran, and 1-5 wt.% lime, adjusting pH to 8-9, placing 1.5-1.7 kg wet material into 17 cm diameter and 30 cm long bags, sterilizing to 100 degrees C under atmospheric pressure condition for 15-16 hours, and cooling to obtain culture medium;    (B) high-temperature sterilizing linen cloth, placing bedding fabric into ground, placing sterile bags, covering with sterile linen cloth, cooling to 30 degrees C or less, and inoculating fungi to 20-25 degrees C under dark condition for 15 days;    (C) digging 1-1.2 m wide and 15-20 cm deep furrow, placing inoculated fungi into tubes, putting into furrow, covering with 1-2 cm thick soil, adjusting pH to 7.5-8, and covering tube; and    (D) cultivating under low light and temperature conditions at humidity of 60-70% for 7 days to grow hyphae, fruiting for 15 days, and harvesting.
NOVELTY - Method of increasing greenhouse tomato production, involves creating ridge having height of 300-600 mm, bottom width of 400-700 mm and distance of 800-1400 mm in greenhouses, interconnecting the ridges between furrows, closing top of the ridges covered with several films used for ground covering, and passing ozone for 1 hectare at a rate of 20 mg/m2/hour for 50-90 hours, or 30 mg/acre/hour for 45-65 hours.    USE - The method is useful for increasing tomato production in greenhouse (claimed).    ADVANTAGE - The method improves soil quality.
NOVELTY - Method for producing 2-keto-L-gulonic acid, involves inoculating strain capable of producing 2-keto-L-gulonic acid into liquid culture medium, and/or fermentation medium, and adding substance that cannot be directly synthesized by the strain.    USE - The method is useful for producing 2-keto-L-gulonic acid (claimed).    ADVANTAGE - The method enables to increase 2-keto-L-gulonic acid yield, and metabolic efficiency of cells, and avoid emission of harmful substance during production process, and pollution.
NOVELTY - The method involves mixing fertilizer grade dicalcium phosphate and concentrated phosphoric acid according to a certain mix ratio, to obtain a mixture. The mixture is then supplied to the self-control mixer. The reaction mixture in the mixer is then supplied to the curing unit through belt feeder. The oxygen gas is supplied to the mixture and the cured semi-finished product is then crushed and dried to prepare triple superphosphate having preset phosphorus content. The triple superphosphate product is then sieved and packed.    USE - Method for producing triple superphosphate used as fertilizer of crops such as rice, wheat, corn, sorghum, cotton, fruit, and vegetable.    ADVANTAGE - The ore resource can be saved and triple superphosphate production cost can be reduced. The triple superphosphate can be produced easily in an environment-friendly manner. Thus, effective water soluble phosphorus content product can be produced reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a block flow diagram explaining the process for producing triple superphosphate. (Drawing includes non-English language text)
NOVELTY - Use of high temperature resistant Streptomyces is claimed for composting agricultural waste. The composting is performed by inoculating Streptomyces strain JSD-1 to fermentation medium containing straw, fermenting mixture to obtain microbial inoculum, and mixing microbial inoculum with agricultural waste and manure.    USE - The high temperature resistant Streptomyces is useful for composting agricultural waste (claimed).    ADVANTAGE - The high temperature resistant Streptomyces enables to degrade lignocellulose rapidly.
NOVELTY - Preparing fertilizer for sugarcane using sisal hemp residue involves (a) adding cell culture strain and filter slurry to the filtered sisal hemp residue, and fermenting mixture at room temperature, (b) controlling fermentation temperature to obtain fermented feed, (c) adding inorganic fertilizer, water-soluble fertilizer element, and trace element to the fermented material, milling mixture, adding alcohol wastewater as a binder to mixture, and granulating to obtain granular particles, and (d) inspecting, weighing and packing fertilizer.    USE - The method is useful for preparing fertilizer for sugarcane (claimed).    ADVANTAGE - The prepared fertilizer increases sugarcane yield, does not pollute environment pollute, improves soil, and quality of sugarcane even when used in small dosage.    DETAILED DESCRIPTION - Preparing fertilizer for sugarcane using sisal hemp residue involves (a) filtering sisal hemp residue, adding cell culture strain and filter slurry to the filtered sisal hemp residue, placing in a fermentation room, and fermenting mixture at room temperature, (b) controlling fermentation temperature at 50-60 degrees C for 8-20 days to obtain fermented feed, (c) adding inorganic fertilizer, water-soluble fertilizer element, and trace element to the fermented material, milling the mixture, adding alcohol wastewater as a binder to the mixture, and granulating to obtain granular particles, and (d) inspecting, weighing and packing the fertilizer. The fertilizer comprises 50-100 pts. wt. sisal hemp residue, 1-6 pts. wt. cell culture strain, 8-10 pts. wt. filter slurry, 30-50 pts. wt. inorganic fertilizer, 1-3 pts. wt. water-soluble fertilizer element, 0.3-0.5 pt. wt. trace element, and 10-12 pts. wt. alcohol wastewater.
NOVELTY - Fertilizer comprises 100-140 parts mass pig manure, 14-16 parts mass calcium superphosphate, 30-50 parts mass kelp residue, 20-40 parts mass furfural residue, 18-20 parts mass lard, 20-40 parts mass donkey bone powder, 12-14 parts mass radix sophorae flavescentis, 50-60 parts mass oil residue, 30-50 parts mass Alopecurus aequalis, 20-40 parts mass crabgrass, 3-5 parts mass photosynthetic bacteria, and 152-172 parts mass water.    USE - As fertilizer for safflower.    ADVANTAGE - The fertilizer is rich in nutrients, causes no pollution, and can be prepared in simple and environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves mixing and crushing the above-mentioned materials, sealing and fermenting mixture for 6-8 days, and granulating fermented product.
NOVELTY - Organic fertilizer comprises 80-100 pts. wt. animal feces, 20-30 pts. wt. plant waste, 10-15 pts. wt. straw powder, 10-15 pts. wt. leaves powder, 2-5 pts. wt. corn, 0.1-1 pt. wt. fermented microbial inoculum, 5-10 pts. wt. gypsum powder, and 5-15 pts. wt. nitrogen-phosphorus-potassium fertilizer, and water (suitable quantity).    USE - The fertilizer is useful for improving crop yield and quality.    ADVANTAGE - The fertilizer improves soil fertility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned organic fertilizer, which involves preprocessing the above-mentioned raw materials, adding water, stacking the mixture to a height of 0.5 m, tightly covering the stacked mixture using plastic film, fermenting the covered mixture at 45 degrees C, and cooling the fermented mixture.
NOVELTY - Fertilizer comprises 26-28 parts mass ammonium chloride, 21-23 parts mass calcium magnesium phosphate fertilizer, 17-19 parts mass hydrated lime powder, 14-16 parts mass composting horse manure, 10-12 parts mass charcoal from grass, 11-13 parts mass potassium dihydrogen phosphate, 7-9 parts mass chelated zinc, 4-6 parts mass Bacillus preparations, 2-4 parts mass Calopogonium vine, 3-5 parts mass copper oxide, 5-7 parts mass water lettuce manure, 1-3 parts mass humic acid, and 60-70 parts mass water.    USE - As fertilizer for cabbage (claimed).    ADVANTAGE - The fertilizer improves organic substance in soil, and quality of cabbage, and increases yield of cabbage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer which involves mixing the above-mentioned raw materials, stirring the mixture for 10 minutes, allowing the mixture to stand for 2.5 hours, and drying the mixture.
NOVELTY - The device has a swirl type burner (15), a flame sensor (16), a thermocouple for temperature control and a microprocessor (17) for controlling automated operation. A processing unit is used for processing heating parameters based on input parameters related to specific data of biomass gasification.    USE - Biomass heating device.    ADVANTAGE - The device provides a display for a user-machine interface for which the operator can monitor the reading of data visually. The device is inexpensive, and provides a better control of the temperature of the gasifier.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for manufacturing a biomass heater device    (2) a biomass heating method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a biomass heating device.    Temperature sensor (11)    Reactor (12)    Swirl type burner (15)    Flame sensor (16)    Microprocessor (17)
NOVELTY - Plant comprises distillation columns (3,4) where both former and latter distillation columns have a set of perforated plates (5,9) arranged longitudinally and set close to the inner walls of distillation column. A coil (12) of the plant is utilized for circulation of the fermentation fluid, and the periphery of coil is provided with steam outlets (15) that promote the introduction of steam to the bottom of distillation columns. The upper end portion of former distillation column is connected to a duct (1) that leads to the latter distillation column for performing saccharification process.    USE - Plant used for producing hydrated ethyl alcohol fuel (AEHC).    ADVANTAGE - The plant produces hydrated ethyl alcohol fuel in an eco-friendly and cost-effective manner. The produced AEHC is a good substitute for fuels consumed in vehicles because it does not emit pollutant components such as carbon monoxide, sulfur dioxide, lead compounds and other toxic organic compounds such as benzene, and thus the produced AEHC effectively minimizes impacts of pollutants on public health.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a hydrated ethyl alcohol fuel producing plant.    Duct (1)    Distillation columns (3,4)    Perforated plates (5,9)    Coil (12)    Steam outlet (15)
NOVELTY - Method comprises application of a coating material - peat pretreated with a preparation containing calcium ion and formalin on the compost inoculated with mycelium with periodic irrigation it with water. At that probiotic Bacillus subtilis is applied in the irrigation water. Preferably irrigation is carried out at a rate of CFU/m2 from 1 x 106 to 1 x 107. The first irrigation is carried out immediately after the termination of pouring the coating material and the subsequent after removal of each wave.    USE - Agriculture.    ADVANTAGE - Method enables to increase the yield of mushrooms and their preservation, to reduce the duration of their cultivation to achieve the maximum yield.3 cl, 2 tbl, 3 ex
NOVELTY - The utility model is new type belongs to biomass can use technology field, specifically relates to a plant biomass carbonization device. The device comprises a feedstock, carbonization reactor, collected coal box, carbonization condensation purification system, liquid collecting tank, the gas storage cabinet and the combustion system. Biomass raw material in a dry distillation reactor, a method of fixed wall heat transfer, heating, a gaseous product and solid coke, gaseous product by condensing purification after a liquid product and a gas, sending into a combustible gas storage cabinet, a combustion biomass carbonization supply the needed heat. The device for biomass raw material with good adaptability and, in particular to a crushing pre-processing raw material, and by burning a fuel gas and supply heat, may implement a carbonization of a FORMULA.
NOVELTY - The utility model is new type relates to a plant biomass carbonizing device, comprising bracket, and equipped with a heating bracket and a carbonizing a, heating up in outside wall is set with a carbonization, wherein also comprises smoke cooling tank, and a bucket box, from the cooling tank and through, its one end connected with a carbonization, another end connected with tar bucket, cooling tank set with a water inlet and a water outlet, a tar bucket at lower part of cooling tank, a tank connected discharge pipe, a sum pipe and tar bucket connected, internal filter box provided with a object. Biomass raw material, in a carbonization product of a fume enter into smoke by cooling in a cooling tank, a tar after condensing a liquid stored in a bucket tar, tar from a fume separation, realize the tar recovery and use, then a fume and a condensing sum after namely enter into filter tank through a purification again outward discharge, discharge accord with a heat preservation requirement, protect the environment.
NOVELTY - The method involves introducing two polymer separation membrane areas for gas separation. Ratio of one of the polymer separation membrane area and the other polymer separation membrane area is 1:3-1:7. Transmission part of polymer separation membrane is re-circulated to a compression process. Bio-gas is compressed and pressurized at pressure of 3-11 bar and temperature of -20-10 degree Celsius. A decompression process of the bio-gas is performed at decompression condition of 0.2-0.9 bars. 10-60 wt.methane and carbon dioxide are separated from the bio-gas.    USE - Method for separating methane gas from a bio-gas of food waste and organic compound in a methane gas purifier (claimed).    ADVANTAGE - The method enables separating high-purity methane gas from the biogas generated in food waste and organic compound so as to improve yield of methane. The method enables maintaining low temperature of the biogas before injecting the biogas in the polymer separation membranes so as to optimize aspect ratio of a separation film and reduce methane refinement device installation cost and methane refinement equipment driving cost. The method enables separating the methane gas in a safe manner.    DETAILED DESCRIPTION - The bio-gas comprises moisture, hydrogen sulfide, ammonia, siloxane, nitrogen and oxygen. An INDEPENDENT CLAIM is also included for a methane gas purifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a methane gas purifier.
NOVELTY - The detector has a planar mirror (2) and a concave spherical mirror (4) for facing the planar mirror and having an optical axis (6) orthogonal to the planar mirror. A distance (D) between the mirrors is equal to 0.75 times a radius of curvature of the spherical mirror, to within 10%. A radiation emitter (E) is arranged at the point of intersection of the spherical mirror and of the axis. A radiation receiver (R) is arranged at the point of intersection of the planar mirror and of the axis. The planar mirror and the receiver/emitter form a single assembly comprising a support plate.    USE - Optical detector for detecting presence of gas e.g. carbon dioxide, carbon monoxide, methane or toxic gases such as xylene or toluene, in an atmosphere.    ADVANTAGE - The detector is manufactured in a simple manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of an optical gas detector.    Distance between planar and spherical mirrors (D)    Radiation emitter (E)    Radiation receiver (R)    Planar mirror (2)    Concave spherical mirror (4)    Optical axis (6)
NOVELTY - The sensor (20) has an objective (211) situated on a substrate (231) to collect light beams (212, 213) emitted by a light source (210). An eyepiece (250) collects an incident light beam to focus it on a detector (251). Return reflective surfaces (281, 282) are arranged facing the substrate. A relay lens (221) is arranged on an intermediate reflective surface (222). The objective, the eyepiece, the relay lens, and the surfaces together form an optical system that is arranged, such that the beam propagates by reflections from the objective to the eyepiece while passing through the relay lens.    USE - Gas sensor for measuring gas i.e. ethanol, in an ethylometer (claimed). Can also be used for measuring a gas e.g. carbon dioxide, carbon monoxide, domestic usage gas such as methane, ethane, propane, butane, ammonia.    ADVANTAGE - The gas sensor possesses a higher compactness than existing gas sensor for a same length of optical path travelled by a light beam inside the cavity receiving the gas to be studied. The gas sensor is manufactured at low cost and on a large scale.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gas sensor.    Gas sensor (20)    Light source (210)    Objective (211)    Light beams (212, 213)    Relay lens (221)    Intermediate reflective surface (222)    Substrate (231)    Eyepiece (250)    Detector (251)    Return reflective surfaces (281, 282)
NOVELTY - A hydrogen generating apparatus comprises porous body which supplies liquid raw material containing liquid fuel to capillary force of pore and carries catalyst, hollow and ribbon-shaped flexible material which has supply part of liquid raw material and discharge part of generated hydrogen. Liquid raw material is vaporized and overheated. Hydrogen is produced by decomposition reaction or steam reforming reaction of hydrocarbon in presence of catalyst.    USE - An apparatus for generating hydrogen (claimed).    ADVANTAGE - Hydrogen is efficiently generated from hydrocarbon type liquid raw materials e.g. liquid methanol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen generation process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the basal principle of hydrogen generation from liquid fuel by exhaust-heat recovery. (Drawing includes non-English language text).
NOVELTY - An emulsified fuel comprises 5-15 %mass biomass pyrolysis oil, 69-80 %mass diesel oil and 11-15 %mass emulsion stabilizer mixture containing 74.8-84.1 wt.% Span 80 (RTM: sorbitan monooleate) and 15.9-25.2 wt.% Tween 80 (RTM: polysorbate 80) and having hydrophilic-lipophilic balance (HLB) value of 6-7.    USE - Emulsified fuel (claimed).
NOVELTY - System comprises works for anaerobic treatment in upflow anaerobic filter (UAF) tank, and aerobic treatment of activated sludge in combination with membrane-filtration in submerged membrane bioreactor (MBR) tank and works for treating sludge by anaerobic fermentation method for recovering methane. The system is automatically controlled by programmable logic controller (PLC) with dissolved oxygen content, chemical oxygen demand (COD) and total suspended solids (TSS) as input parameters.    USE - The system is used for treating brewing and beverage industry wastewater having high organic content.    ADVANTAGE - The system can be separately or integrally designed.
NOVELTY - Ethanol is produced which involves contacting acetic acid and hydrogen in a reactor in the presence of a catalyst comprising a binder and a mixed oxide comprising cobalt and tin. The mixed oxide is present in an amount of 60-90 wt.%, based on the total weight of the catalyst.    USE - The process is useful for producing ethanol (claimed).    ADVANTAGE - To reduce the cost of the catalyst, the catalyst is preferably substantially free of precious metals, but still demonstrates a high stability with high conversion of acetic acid and selectivity to ethanol. Even without the presence of precious metals, the catalysts comprising a mixed oxide of cobalt and tin demonstrate an advantageous conversion of acetic acid to ethanol at high selectivities with low ethyl acetate formation and other by-product formation, in particular diethyl ether. Low byproduct formation reduces the separation requirements to obtain ethanol. This allows the catalysts to be used in some processes for producing ethanol.
NOVELTY - Device comprises a feed cone (1) and an upper airtight chamber (2), where the feed cone is connected with the upper airtight chamber above and below of a cutting valve and a top closure (3) of the trunk-conical section. A reactor is integrated with an inferiorly body (4) between an outer closure (5) and a thermal insulation layer. The base of the device is formed by a cylindrical cone (11). The cylindrical cone is provided with a cone of the ash discharge and a cone of the gas chamber. A lower airtight chamber is provided above and below a cutting valve.    USE - Device used for conversing constructive disposal solid residue into energy (claimed).    ADVANTAGE - The device is cost-effective and practical.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a device for conversing constructive disposal solid residue into energy.    Feed cone (1)    Upper airtight chamber (2)    Top closure (3)    Inferiorly body (4)    Outer closure (5)    Cylindrical cone (11)
NOVELTY - The sealing device includes environment-friendly biomass, and a wood vinegar liquid charcoal for continuous production of critical function. A special sealing is provided between carbide furnace and screw feeder at high and low temperature in order to effectively prevent gas leakage.    USE - Sealing device.    ADVANTAGE - The sealing device enhances industrial production value, makes a valid located biomass waste, and reduces environment pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sealing device.    High temperature sealing material (2)    Sealing material (3)    Fastener (4)    Steel fastening fastener (5)    Anaerobic carbonization converter (6)
NOVELTY - Preparation of linezolid involves dissolving N-(2R)-2-((3-fluoro-4-morpholin-4-yl)amino)-2-hydroxy ethyl acetamide and carbonyl alkylating agent in organic solvent, adding inorganic alkali catalyst, adjusting pH to 8-10, reacting at 20-60 degrees C, extracting, washing, drying and recrystallizing.    USE - Method for preparing linezolid (claimed).    ADVANTAGE - The method is simple, environmental-friendly and safe.
NOVELTY - The grid has a profile of parallel channels in trapezoidal or rectangular shape. Each channel includes a side wall (1) having a ribbed-wedge (2) with oppositely directed vertices in which another side wall is located.    USE - Grid for distribution of electricity produced from carbonate fuel cells powered by biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a channel of a grid.    Side wall (1)    Ribbed-wedge (2)
NOVELTY - The device (15) has housing having an inlet (20) provided for connection to an access port venting gas from an internal operating field. The housing outlets (30A-30E) are provided to vent gas from detection device. The non-electrical colorimetric enteric gas sensors (25A-25E) having silica granules is arranged within a passageway for determining presence of a selected enteric gas comprises hydrogen sulfide, dimethylsulfide, methanethiol, aka methyl mercaptan, methane and hydrogen and the concentration of gas and indicating that presence by a visually-apparent change in appearance.    USE - Device for detection of in-line enterotomy for use in surgical procedure.    ADVANTAGE - The gas composition present in the intraabdominal cavity of the patient is monitored by using a small, low-cost, non-electrical and disposable device during a minimally invasive procedure and/or robotic procedure and the occurrence of an unplanned enterotomy such as the presence of gas e.g. hydrogen sulfide, dimethylsulfide and methanethiol, aka methyl mercaptan, methane and hydrogen concentrations found only within the bowel is detected. The surgeon and operating room personnel are alerted to the occurrence of the enterotomy during the procedure so as to allow for appropriate correction of the enterotomy which in turn avoids postoperative complications.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of detecting perforation of a bowel.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of an in-line enterotomy detection device.    In-line enterotomy detection device (15)    Inlet (20)    Colorimetric enteric gas sensors (25A-25E)    Outlets (30A-30E)    Proximal chamber (40)
NOVELTY - A hydrogen-producing electrode has a catalyst layer containing platinum, nickel, and palladium or ruthenium as main component, supported on an electroconductive base material.    USE - Hydrogen-producing electrode used as cathode for electrolysis (claimed) of water and salt, in electrolysis industry such as brine-electrolysis industry.    ADVANTAGE - The hydrogen-producing electrode has stable low hydrogen-overvoltage characteristics and excellent durability. The electrode is manufactured by a simple process and contributes to reduction in energy consumption during electrolysis. The peeling of the catalyst during electrolysis process and startup or shutdown process is prevented.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of hydrogen-forming electrode, which involves forming a catalyst layer precursor on a conductive substrate, and performing reduction to form the catalyst layer; and    (2) electrolysis, which involves electrolyzing water or alkali metal chloride aqueous solution in an electrolytic cell which has the hydrogen-producing electrode as cathode, and anode arranged on both sides of a diaphragm, and producing hydrogen gas and alkali metal hydroxide aqueous solution from the cathode and oxygen gas or gaseous chlorine from the anode.
NOVELTY - Bacterial culture comprises a biomass composition and a population of lactic acid bacteria. The population of lactic acid bacteria comprise (i) a first population of lactic acid bacteria which have been genetically modified to express a secreted cellulase, and (ii) a second population of lactic acid bacteria which have been genetically modified to express a secreted xylanase, where the ratio of the first population and second population is selected such that the specific activity of cellulase:xylanase in the culture is greater than 4:1 or less than 1:4.    USE - The bacterial culture is useful for processing lignocellulose (claimed).    ADVANTAGE - The bacterial culture simply and cost-effectively processes lignocellulose.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) population of lactic acid bacteria which have been genetically modified to express a secreted cellulase and a secreted xylanase, where the population of lactic acid bacteria are Lactobacillus plantarum, (2) method of processing lignocellulose, involves propagating the culture, thus processing the lignocellulose; and (3) silage comprising the culture, and produced by processing lignocellulose by above-mentioned method.
NOVELTY - A micro-carbon fiber is produced by introducing selected chemical mixture into heating chamber (2), heating using series of burners (1), and injecting carbon feed stock into catalyst reaction chamber (6) to initiate micro-carbon generating chemical process to occur.    USE - Production of micro-carbon fiber for huge volume of non-polluting hydrogen fuel and absorption of cellphone radiation embedded in plastic or other material and electromagnetic radiation.    ADVANTAGE - Fiber has electromagnetic energy absorbing ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for production of micro-carbon fiber comprising heating chamber, series of burners, catalyst reaction chamber, and injector (4).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of apparatus for production of micro-carbon fiber.    Series of burners (1)    Heating chamber (2)    Injector (4)    Catalyst reaction chamber (6)    Graphite pump (7)
NOVELTY - The device has a hydrogen water generator portion that is positioned at a bottom portion of the housing. An electrolysis portion is set with a metal reticulate electrode mounted on up-and-down both sides of an insulating spacer horizontally provided in the bottom portion of the housing. A chlorinated lime smell deodorizing reactor is filled with the ceramic coarse grain containing sulfurous-acid calcium which decomposes chlorinated lime component and set with principal portion formed with a reticulated or porous material provided in inside of the housing.    USE - Simple electrolytic-type hydrogen water generator device.    ADVANTAGE - Since the chlorinated lime component is decomposed by the predetermined chemical reaction, the chlorinated lime smell is no longer sensed for the hydrogenous water to drink at all. The damage of the secondary battery, connected power supply and electrode current apparatus substrate is prevented, even if natural water is moved from the reactor to the hydrogen water generator device.
NOVELTY - Biological-fuel element for transfer of electrical energy during fermentative oxidation of organic compounds, comprising one cuvette which comprises oxidizable substrate, where the cuvette is electrically connected with working electrode and reference electrode. The working electrode is platinum electrode. The biological-fuel element is made onto basis of thermo-extended graphite and diaphragm fractions of Gluconobacter oxydans strain VKM (V-1280). The strain is immobilized in chitosan gel.    USE - The biological-fuel element is used for transferring electrical energy during fermentative oxidation of organic compounds (claimed).
NOVELTY - Cultivation of corn comprises selecting high quality and high yield corn, subsoiling, raking, adding fertilizer containing nitrogen, phosphorus and potassium fertilizer, farmyard manure and boron, zinc, manganese, iron, copper and rare earth fertilizer, sowing, planting where plant spacing is between 15-18 cm, carrying out seed germination, applying atrazine suspension concentrate with chlormequat, adding urea, diammonium phosphate and potassium chloride per acre, spraying with potassium dihydrogen phosphate and rare earth fertilizer and harvesting.    USE - Method for cultivating corn (claimed).    ADVANTAGE - The method is environment-friendly and has high yield.    DETAILED DESCRIPTION - Cultivation of corn comprises selecting high quality and high yield corn, subsoiling to 30-45 cm by 25 cm deep, raking, adding 80 kg of fertilizer containing nitrogen, phosphorus and potassium fertilizer (15 wt.% of fertilizer), farmyard manure and boron, zinc, manganese, iron, copper and rare earth fertilizer, sowing, planting where plant spacing is between 15-18 cm, carrying out seed germination, applying 40% atrazine suspension concentrate with 72% chlormequat, adding 25 kg urea, 50 kg diammonium phosphate and 50 kg potassium chloride per acre, spraying with 50 g potassium dihydrogen phosphate and 1.3 kg rare earth fertilizer and harvesting.
NOVELTY - An environmentally-friendly pesticide comprises 1-3 pts. wt. biosynergist and 2-5 pts. wt. Chinese medicine composition.    USE - Environmentally-friendly pesticide is used for preventing peanut underground insect pest.    ADVANTAGE - The environmentally-friendly pesticide has excellent soil pest control effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of environmentally-friendly pesticide, which involves using sesame meal and soybean meal.
NOVELTY - The furnace has a furnace body, a hearth and a hearth chamber body, where bottom of the hearth is provided with a hearth inlet. A feeding channel is divided into a feeding pipe (10) and a feed bucket (33). The upper part of the feeding pipe is crumpet-shaped. The feed bucket is connected with the upper part of the feeding pipe. The feed bucket is provided with a feeding air inlet valve (34) and feeding push rod (32).    USE - Biomass gasification furnace.    ADVANTAGE - The furnace is small in size, and reduces feeding resistance.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification furnace.    Feeding pipe (10)    Air hole (28)    Feeding push rod (32)    Feed bucket (33)    Feeding air inlet valve (34)
NOVELTY - The reactor has a coal inlet, a de-semi coke outlet, a sum and mixed coal air outlet, an air inlet baffle plate, a bed, a de-semi coke inlet, a gasification semi-coke outlet, a gasification coal outlet, a pre-heating air inlet and a steam inlet. A bottom of the bed is provided with a baffle plate. The baffle plate is fixed between the de-semi coke inlet and the gasification semi-coke outlet. A sum solid separator is connected with the gasification coal outlet. A mixed coal output is connected with a waste heat boiler.    USE - Spouted bed reactor.    ADVANTAGE - The reactor is low in cost, consumes less energy and prevents carrier separation purifying problem.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic circuit diagram of a spouted bed reactor.
NOVELTY - The device has a U type hollow bottomed housing, a machine cover and a sealing cover, where the machine cover and a sealing cover are utilized to close a reaction area. The reaction area is along an axial direction of the housing. The machine cover is provided with a biomass inlet at a baking area. A center of the housing is fixed with a double-shaft spiral packing auger.    USE - Biomass double-shaft spiral pyrolysis device.    ADVANTAGE - The device has high material mixing efficiency and heat transfer mass transfer effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a biomass double-shaft spiral pyrolysis device.
NOVELTY - Production of biomass pellet fuel involves drying wood biomass raw material until the moisture content is 6-18 wt.%, crushing the raw material using pulverizer, sieving using a sieve having mesh size of 4-8 mm, mixing obtained powder with water and pine sawdust using a mixer, controlling moisture content to 15-25 wt.%, softening mixed material by steam, then granulating using granulator, pressing into material having diameter of 5-15 mm, length of 3-6 cm and moisture content of 15-20 wt.%, cooling, screening and controlling moisture content to 10-15 wt.%.    USE - Production of biomass pellet fuel (claimed).    ADVANTAGE - The method enables simple production of biomass pellet fuel with high quality, excellent combustibility and reduced bottom ash slagging rate by environmentally-friendly process.
NOVELTY - A micro-emulsion biodiesel comprises 61-85 pts. wt. biodiesel, 3-8 pts. wt. emulsifier and 30-50 pts. wt. water. The emulsifier comprises 23 pts. wt. fatty alcohol ethoxylates, 16 pts. wt. 3,5,4'-trihydroxy-trans-stilbene, 11 pts. wt. maleic acid dimethyl ester, 20 pts. wt. maleic anhydride and 30 pts. wt. mannitol.    USE - Micro-emulsion biodiesel (claimed).    ADVANTAGE - The micro-emulsion biodiesel has excellent stability, high volatility, and low viscosity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of micro-emulsion biodiesel.
NOVELTY - A biomass pellet fuel comprises 40-50 pts. wt. larch timber, 10-15 pts. wt. elm wood, 10-15 pts. wt. willow tree wood, 10-15 pts. wt. poplar tree wood, 10-15 pts. wt. peach tree wood, and 6-9 pts. wt. additive.    USE - Biomass pellet fuel (claimed).    ADVANTAGE - The biomass pellet fuel is environmentally-friendly, and generates reduced ash during combustion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass pellet fuel.
NOVELTY - A catalyst is prepared by air-drying flowers of Bombax ceiba, burning the dried flowers to obtain ash, and cooling the ash to bring to an ambient temperature.    USE - Catalyst is used for trans-esterification of oil (claimed) for preparing biodiesel.    ADVANTAGE - The biodegradable catalyst is easily separable, has excellent thermal stability, durability, reusability, and catalytic property when activated by heating at 4000-7000 degrees C, and can be economically produced by environmentally-friendly process. The trans-esterification of oil can be carried out in a short period of time. The produced biodiesel has high quality.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (i) transesterification of vegetable oil, which involves contacting the catalyst comprising ash of flowers of Bombax ceiba with a vegetable oil in the presence of a solvent; and (ii) preparation of transesterification catalyst, which involves collecting mature flowers of Bombax ceiba, air-drying the collected flowers, burning the dried flowers to obtain ash, cooling the ash to bring to an ambient temperature, and optionally drying the ash in an oven at a temperature of 100-120 degrees C.
NOVELTY - A process for pyrolyzing biomass (15) involves pyrolyzing biomass in fast pyrolysis chamber by heating the biomass to preset temperature to generate pyrolysis vapor flow, directing pyrolysis vapor flow from fast pyrolysis chamber along a vapor flow conduit (37) to a condensation trap at a temperature to condense vapor to liquid and generating thermal gradient along vapor flow conduit between pyrolysis chamber and condensation trap. A majority of pyrolysis vapor flow along vapor flow conduit to condensation trap is achieved by natural convection.    USE - Pyrolysis of biomass for producing power.    ADVANTAGE - The pyrolysis is carried out with high efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of batch pyrolysis system.    Pyrolysis system (10)    Biomass (15)    Removal of carbon (16)    Pyrolysis liquid (17)    Vapor flow conduit (37)
NOVELTY - A dry cleaning hair spray comprises 20-30 wt.% butane, 30-40 wt.% propane, 3-10 wt.% aluminum starch octenyl succinate, 0.02-0.2 wt.% denatured alcohol, 5-10 wt.% aqueous distearyl dimethylammonium chloride, 0.02-0.2 wt.% Aloe extract liquid, 0.02-0.2 wt.% flavor and 0.03-2 wt.% menthol, and remainder of deionized water.    USE - Dry cleaning hair spray is used as hair care product.    ADVANTAGE - The safe and mild dry cleaning hair spray has excellent cleaning ability and compatibility, and is easy to use, and can be used by people with sensitive skin.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of dry cleaning hair spray, which involves mixing aluminum starch octenyl succinate, denatured alcohol, aqueous distearyl dimethylammonium chloride, flavor, Aloe extract solution and menthol, adding butane, propane and deionized water at high pressure and low temperature, and filling in cylinder at high pressure.
NOVELTY - A polymer-carboxylic acid functionalized nano hydrogel composite film comprises 70-95% polyoxyethylene -polycaprolactam block copolymer and 5-30% carboxylic acid functionalized nano hydrogel composition, where the polyoxyethylene - polycaprolactam block copolymer, polyoxyethylene segments represents the mass fraction of the block copolymer of 55- 60%, polycaprolactam segment of 40-45%, and the film has thickness of 70-105 mu m.    USE - Polymer-carboxylic acid functionalized nano hydrogel composite film for separating carbon dioxide/methane mixed gas, and carbon dioxide/nitrogen gas mixture (all claimed).    ADVANTAGE - The film has improved performance of composite membranes for gas separation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for preparing polymer-carboxylic acid functionalized nano hydrogel composite film    (2) use of polymer-carboxylic acid functionalized nano hydrogel composite film for separating carbon dioxide/methane mixed gas.
NOVELTY - Preparation of catalyst comprises crushing rice husk, drying, placing in muffle furnace under nitrogen condition, heating, and calcining to obtain rice husk powder; adding egg shell to distilled water, removing impurities, drying, crushing, sieving, placing in muffle furnace under nitrogen condition, calcining, and vacuum drying to obtain white powdery solid; and dissolving rice husk powder in deionized water, adding in white powdery solid, stirring, drying, placing in muffle furnace under nitrogen conditions, and calcining.    USE - Method for preparing catalyst used for preparing biodiesel (claimed).    ADVANTAGE - The method is simple and environment-friendly and has wide source raw materials, low cost, high production rate and high yield of more than 80%. The catalyst has strong catalytic activity.    DETAILED DESCRIPTION - Preparation of catalyst comprises crushing rice husk, drying at 90-110 degrees C for 12-20 hours, placing in muffle furnace under nitrogen condition, heating to 400-800 degrees C, and calcining at 400-800 degrees C for 2-4 hours to obtain rice husk powder; adding egg shell to distilled water, removing impurities, drying at 90-110 degrees C for 10-18 hours, crushing, sieving through 160-180 meshes sieve, placing in muffle furnace under nitrogen condition, calcining at 800 degrees C for 2 hours, and vacuum drying to obtain white powdery solid; and dissolving 1-3 g rice husk powder in 50 ml deionized water, adding in 7-9 g white powdery solid, stirring at 400-600 revolutions/minute for 3-5 hours, drying, placing in muffle furnace under nitrogen conditions, and calcining at 600-1000 degrees C for 2-5 hours.
NOVELTY - A plasma reforming generator comprises center electrode (1), PTFE layer (2), external electrode (3), outer cylinder (4), feeding port (5), and air outlet (6). The center electrode has copper rod tip. The external electrode has copper scaling. The outer cylinder wall is made of stainless steel tube.    USE - Plasma reforming generator used for producing hydrogen and ethanol (claimed).    ADVANTAGE - The generator is controllable and has raw material adaptability characteristic, high raw material usage rate, and low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of plasma reforming generator.    Center electrode (1)    PTFE layer (2)    External electrode (3)    Outer cylinder (4)    Feeding port (5)    Air outlet (6)
NOVELTY - Anaerobic sewage treatment method involves concentrating sludge by sedimentation. Copper sulfate is dissolved into the concentrated sewage for anaerobic digestion. Digested product is washed with water. Gas is collected, which is produced from the anaerobic digestion of sewage.    USE - Anaerobic sewage treatment method for producing methane gas (claimed).    ADVANTAGE - The method ensures increased methane production by utilizing low amount of copper sulfate.
NOVELTY - High pressure biogas generating device comprises feed tube (11), discharge pipe (20), discharging pipe blocking plate (28), discharging pipe drainage hole (30), water discharge hole (32), gas collecting pipe (40), drain pipe (50), cloth pipe (52), and fabric hole cloth (54). U-type fermentation pipeline connected to feeding tube and pressure fermentation tank, and gas feed pipe stopper plate. Pressure feed pipe is provided with drainage holes. U-shaped fabric is provided with extended pipeline. Check valve controls the unidirectional flow.    USE - High pressure biogas generating device (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of high pressure biogas generating device.    Feed tube (11)    Discharge pipe (20)    Discharging pipe blocking plate (28)    Discharging pipe drainage hole (30)    Water discharge hole (32)    Gas collecting pipe (40)    Drain pipe (50)    Cloth pipe (52)    Fabric hole cloth (54)
NOVELTY - Device having bacterial strain cloth comprises feeding pipe (11) through which raw material is fed into U-type pipeline for generating marsh gas by biogas fermentation. A gas collecting pipe (40) is present in the space between feeding pipe blocking plate (22) and discharge pipe blocking plate (26), where a discharge pipe (12) is provided for extrusion of liquid. The feed tube has holes that provide unidirectional flow of slurry into the fermentation chamber. The reflux device provides complete biogas slurry circulation. Marsh gas occupies space inside the pipeline.    USE - Device having bacterial strain cloth used for promoting generation of marsh gas (claimed).    DESCRIPTION OF DRAWING(S) - The drawing illustrates a schematic view of device having bacterial strain cloth.    Feeding pipe (11)    Discharge pipe (12)    Feeding pipe blocking plate (22)    Discharge pipe blocking plate (26)    Gas collecting pipe (40)
NOVELTY - The method involves taking 1850.2 g sample from a food waste recycling bin at 110 degrees C, drying in an oven to gain constant weight, and then crushing and grinding the dried food waste via a mini-mill plants to a particle size less than 1mm. The pulverized food waste (20 g) is purged into 1.2 liters per minute flow rate of nitrogen purge 20 minutes at 400-500 degrees C. The pyrolysis volatile products are cooled by a condenser and an ice water bath, where the resulting product is washed with chloroform at 50 degrees C to obtain quality tar. The pyrolysis products are detected and analyzed.    USE - Method for treating medium volatile organic food waste (claimed).    ADVANTAGE - The method treats medium volatile organic food waste in a simple and cost-effective manner.
NOVELTY - The pyrolysis furnace apparatus comprises a furnace body (1) for separating gasification channel (2) and pyrolysis channel (3), where the gasification channel is communicated with the pyrolysis channel. The gasification channel and pyrolysis channel are introduced into raw material, where the pyrolysis channel is provided with an external communication of furnace gas outlet (4). The pyrolysis channel is provided with a temperature controller, where the temperature controller comprises a channel located in entrance and exit of thermocouple (5).    USE - Pyrolysis furnace apparatus.    ADVANTAGE - The pyrolysis furnace apparatus produces high-temperature biomass gasification gas in channel, and removes dust and tar in a simple manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the pyrolysis furnace apparatus.    Furnace body (1)    Gasification channel (2)    Pyrolysis channel (3)    Furnace gas outlet (4)    Thermocouple (5)
NOVELTY - The alcohol fuel additive comprises 15-25 pts. wt. octanol, 15-25 pts. wt. silicone bis-imidazoline, 25-35 pts. wt. cinnamon oil, and 25-35 pts. wt. acetone or petroleum ether. The silicon oil is low viscosity silicon oil.    USE - Alcohol fuel additive.    ADVANTAGE - The alcohol fuel additive can be stably dissolved in methanol, and improves calorific value of methanol, and reduces fuel costs.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an alcohol fuel additive synthesis device, which comprises mixing chamber, methyl alcohol and alcohol ether; and    (2) a method for synthesizing alcohol fuel additive, which involves preparing methanol and alcohol fuel additive to form a liquid-gas mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the alcohol fuel additive synthesis device.    Methyl alcohol tank (1)    Additive tank (2)    Mixing chamber (3)    Pump (4)    Low frequency ultrasonic wave mixing chamber (6)
NOVELTY - Adhesive comprises wood vinegar raw liquid, and is obtained by distilling the wood vinegar raw liquid under normal pressure at 90-102 degrees C.    USE - Adhesive used for preparing biomass coke (claimed).    ADVANTAGE - The adhesive is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for applying adhesive, which involves:    (A) mixing adhesive, biomass semi-coke and water;    (B) stirring the mixed material;    (C) subjecting the mixed material for direct compression molding to obtain biomass coke precursor; and    (D) drying the obtained precursor to obtain the desired product.
NOVELTY - Biomass fuel comprises 40-60 pts. wt. wood chips, 20-30 pts. wt. wheat straw and 20-30 pts. wt. rice straw.    USE - Biomass fuel.    ADVANTAGE - The biomass fuel has good viscosity, low ash content and high heat value.
NOVELTY - The biomass fuel comprises 40-50 pts. wt. straw powder, 35-45 pts. wt. wood shoulder, 25-35 pts. wt. rice straw, 10-20 pts. wt. Saccharum officinarum, 5-15 pts. wt. cottonseed hull, 3-10 pts. wt. camellia shell, 3-8 pts. wt. corncob, 3-10 pts. wt. furfural residue, 2-6 pts. wt. dechlorinating agent, and 2-6 pts. wt. dehydration agent.    USE - Biomass fuel.    ADVANTAGE - The biomass fuel is eco-friendly.
NOVELTY - Deacidifying natural ester oil involves subjecting the natural ester oil for preliminary deacidification treatment and then subjecting the obtained material for vacuum gassing treatment at 95-100 degrees C and vacuum degree of -0.96-1 megapascal. The treated material is deacidified at 253-260 degrees C in an oil insulating device and then the obtained material is discharged. The discharged material is collected with acid value greater than or equal to 0.03 milligrams of potassium hydroxide per gram and then is further discharged to obtain the oil with acid value less than -0.03 milligrams of potassium hydroxide per gram.    USE - Method for deacidifying natural ester oil (claimed).    ADVANTAGE - The method enables to deacidify natural ester oil in simple and cost-effective manner, and with high yield.
NOVELTY - Biodiesel production involves entering liquid in a separator for separating diluted solution into two portions by centrifugation, and then conducting the liquor into evaporator to leave syrup after evaporation of water. An ethanol vapor is placed into extractor at 75-90 degrees C for 6-7 hours after extraction to obtain a crude extract and fodder. The obtained extract is placed into extractor for evaporating ethanol to give a concentrate to obtain oil and syrup waste.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method produces biodiesel in a simple, cost-effective and eco-friendly manner with easy storage, long shelf life, high efficiency, low energy consumption and good product market.    DETAILED DESCRIPTION - Biodiesel production involves entering liquid in a separator for separating diluted solution into two portions by centrifugation, and then conducting the liquor into evaporator to leave a syrup after evaporation of water. An ethanol vapor is placed into extractor at 75-90 degrees C for 6-7 hours after extraction to obtain a crude extract and fodder. The obtained extract is placed into extractor for evaporating ethanol to give a concentrate to obtain oil and syrup waste. The obtained oil, ethanol vapor and an acid catalyst or a base catalyst are placed into the reactor for transesterification at 150-170 degrees C for 7-8 hours to get lower glycerol solution, and crude biodiesel. The crude biodiesel is placed into rectifier for recovering refined biodiesel.
NOVELTY - Coke oven gas is desulfurized, and supplied to three adiabatic methanation reactors (r1-r3), and carbon in inlet of methanation reactor (r2) is compensated. The hydrogen, carbon monoxide and carbon dioxide produced by reaction of methanation of coke oven gas are condensed and separated, to obtain more than 95% methane-containing gas.    USE - Methanation of coke oven gas and natural gas (claimed).    ADVANTAGE - The method provides synthesis gas with high methane content, with low energy consumption and low equipment investment, and without using circulation compressor.
NOVELTY - Dry fractionation of lignocellulosic biomass involves crushing biomass comprising lignin, cellulose and hemicellulose to ultrafine powder, and separating fraction rich in lignin, fraction rich in cellulose and fraction in hemicellulose by electrostatic separation of ultrafine powder.    USE - Dry fractionation of lignocellulosic biomass used for preparing fuel (claimed).    ADVANTAGE - The method enables environmentally-friendly dry fractionation of lignocellulosic biomass by economical process, with reduced energy consumption.
NOVELTY - A composition comprises lignocellulose-containing organic matter and spawn of lignin-digesting fungal species.    USE - Composition in the form of powder, granules, suspension, dispersion and/or fibrous matter used as fertilizer for treating soil (all claimed).    ADVANTAGE - The composition uses low cost recycled material, accelerates composting properties, increases plant production, decreased chemical and biological pollution and pest burden, and restoration of active biological soil diversity. The composition is capable of degrading a lignin-rich material in situ to provide enhanced nutrition availability for plant uptake. In addition, the composition serves as a soil mediator by reducing harmful chemicals and nematodes and adjusting properties of the soil physically, chemically, and functionally. Because lignocellulose-containing organic matter can be obtained from recycled material such as spent coffee grounds (SPG), the production of the composition is inexpensive and environmentally friendly. The resulting enhanced organic matter aerates the soil and inoculates the immediate area with beneficial microorganisms that consume the lignocellulose-containing organic matter and nutrients for growth and reproduction, thus providing immediate nutrient requirements to the soil, while improving friability, drainage, and moisture management to clay, compacted, or sandy soil conditions.
NOVELTY - A genetically enhanced Chlorogloeopsis sp. host cell comprising a first recombinant gene encoding a first protein for the production of ethanol under the transcriptional control of a first inducible promoter, having greater than or equal to 85-95% sequence identity to an endogenous inducible promoter of the Chlorogloeopsis sp. host cell, is new.    USE - The genetically enhanced Chlorogloeopsis sp. host cell is useful for producing ethanol. The construct is useful for transforming Chlorogloeopsis sp. host cells (all claimed).    ADVANTAGE - Provided is a new cyanobacterial strain for the production of ethanol, which can withstand hard culturing conditions and the metabolic stress associated with the production of chemical compounds of interest.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a method for producing ethanol by (a) culturing the genetically enhanced Chlorogloeopsis sp. host cells above in a culture medium, the host cells thus producing ethanol, and (b) retrieving ethanol from either one of: the host cells, the medium or the headspace above the medium; (2) a method for producing genetically enhanced Chlorogloeopsis sp. host cells; and (3) a construct for transformation of Chlorogloeopsis sp. host cells, comprising a first recombinant gene encoding a first protein for the production of ethanol under the transcriptional control of a first inducible promoter, having greater than or equal to 85-95% sequence identity to an endogenous inducible promoter of the Chlorogloeopsis sp. host cell.
NOVELTY - The new type utility claims one kind A/O technology and phase combined is a a MFC waste water processing system. Between anode room and cathode room by proton exchange film, anode room in a main anode, auxiliary anode, and connected by lead, in cathode room bottom provided with aeration device, a cathode provided with cathode, cathode by variable resistance box and a anode connected, anode water room through a peristaltic pump, a sediment pool, the third peristaltic pump and a cathode water inlet connected, a precipitate pool by a peristaltic pump and a water inlet connected anode, a cathode water outlet through the fourth peristaltic pump,. a third, fifth peristaltic pump and a water inlet connected anode, a cathode water outlet and the fourth sediment pool connected. The utility model is novel. using the two of a a a a microorganism fuel battery is, realize the synchronous denitrification removing nitrogen and carbon P, a lasting and stable the current to achieve the unified of sewage treatment and energy recovery, further improved the microorganism fuel cell waste water processing technology.
NOVELTY - Production of a chemical compound, involves: (a) forming a mash or slurry comprising a non-cellulosic sugars and a lignocellulose fiber; (b) fermenting the mash to produce a chemical compound from the non-cellulosic sugar; (c) adding an enzyme to the fermenting mash to hydrolyze the lignocellulose fiber to cellulosic sugars and cellulosic sugar oligomers; (d) continuing fermenting the non-cellulosic and the cellulosic sugars to produce additional chemical compound; and (e) terminating the fermentation and recovering the chemical compound.    USE - The method is useful for producing a chemical compound, preferably ethanol (claimed), and for the conversion of biomass to biofuels and other products and co-products.    ADVANTAGE - The method can efficiently manage the viscosity of the downstream process streams or stillage streams in an ethanol production plant that result from processing the starch based fermentation mash or whole corn mash slurries with cellulases and or other treatments to convert all or part of the component fiber into fermentable sugars.
NOVELTY - Processing of biomass involves reacting biomass with solvent system comprising water, acid(s) and organic compound(s) chosen from lactone, furan and cyclic ether for time (T1) and at temperature (M1) to yield liquid fraction enriched in solubilized 5C-sugar-containing oligomers and 5C sugar monomers and a solid fraction enriched in substantially insoluble cellulose and C6-sugar-containing oligomers.    USE - Processing of biomass (claimed).    ADVANTAGE - The biomass is processed by economical method. The processed biomass can be used as renewable substitute for petroleum-based resources.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the processing of biomass.    Step for grinding raw biomass (10)    Reaction process (12)    Solid-liquid separation (14)    Step for production of furfural (18)    Step for production hydroxymethylfurfural, levulinic acid or gamma-valerolactone (22)
NOVELTY - A hair-care aerosol comprises 30-60 wt.% environmentally-friendly solvent, 5-13 wt.% ultrafine oil absorbing powder, 0.5-5 wt.% hair conditioning agent, 0.1-2 wt.% flavor, and 20-50 wt.% propellant.    USE - The hair-care aerosol is useful for cleaning hair.    ADVANTAGE - The hair-care aerosol provides freshness to hair, and is suitable for routine use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing hair-care aerosol.
NOVELTY - An organic granule fertilizer comprises 20-30 wt.% molasses fermentation liquid, 10-20 wt.% biochemical fulvic acid, 5-10 wt.% 80-90-mesh brucite, 5-10 wt.% natural magnesium sulfate, 1-3 wt.% citric acid, 20-30 wt.% urea, 10-20 wt.% diammonium phosphate, 10-20 wt.% potassium fertilizer, 3-5 wt.% caking agent, and 3-5 wt.% trace element.    USE - Organic granule fertilizer.    ADVANTAGE - The fertilizer has smooth and uniform appearance, high hardness, and good disintegration.
NOVELTY - Separation of petunidin in Lycium ruthenicum includes taking Lycium ruthenicum, extracting with methanol containing formic acid, filtering, concentrating filter liquor, removing methanol, dissolving extract with formic acid aqueous solution, respectively eluting with water and methanol in macroporous resin column, collecting methanol eluent, drying to obtain crude extract; taking methyl tertiary butyl ether, n-butanol, acetonitrile, and water, putting in separating funnel to form two-phase solvent system and filling stationary phase into countercurrent chromatography column.    USE - Method for separating petunidin in Lycium ruthenicum (claimed).    ADVANTAGE - The method is simple, efficient, fast and suitable for industrial production, yields high-purity petunidin of up to 97%, has low cost, and no loss and pollution, and does not need solid-phase carrier and reversible adsorption.    DETAILED DESCRIPTION - Separation of petunidin in Lycium ruthenicum comprises taking Lycium ruthenicum, extracting with methanol containing 1-3 vol.% formic acid, filtering, concentrating filter liquor, removing methanol, dissolving extract with 1-3 vol.% formic acid aqueous solution, respectively eluting with water and methanol in macroporous resin column, collecting methanol eluent, drying to obtain crude extract; taking methyl tertiary butyl ether, n-butanol, acetonitrile, and water at a ratio of 1:2.5:1.5:5, putting in separating funnel to form two-phase solvent system, filling stationary phase into countercurrent chromatography column at 25-28 degrees C and rotating speed of 800-1000 revolutions/minute (rpm), pumping mobile phase at a flow rate of 1-2.5 ml/minute, where crude extract is dissolved into mobile phase to prepare sample solution, and monitoring sample solution under UV detector.
NOVELTY - Preparation of kitchen garbage fertilizer comprises cutting leaves into 3-5 cm, adding kitchen waste to leaves, piling at 1-3 m wide, 1-1.5 m high and 5-10 m long, sprinkling leavening agent every 25 cm high, covering with insulation film and fermenting.    USE - Method for preparing kitchen garbage fertilizer (claimed).    ADVANTAGE - The fertilizer is environment-friendly and non-toxic.
NOVELTY - Large-scale anaerobic biogas digester comprises components such as discharge channel, a feed inlet, processed sludge outlet, reservoirs and biogas collection tank, where all the components are placed located at the top of the large-scale anaerobic biogas digester along a rail. The sludge is fed into the large-scale anaerobic biogas digester through feed inlet. The biogas collection tank with a diameter of 8 centimeter is provided with a safety pipeline.    USE - Large-scale anaerobic biogas digester.    ADVANTAGE - The large-scale anaerobic biogas digester greatly enhances the production efficiency of biogas in an economical manner.
NOVELTY - The tester has a micro pump whose air outlet end is connected with a carbon monoxide probe and a vulcanization hydrogen probe. An oxygen probe is connected with a pin of a single chip that is connected with a voltage stabilizer that is connected with a white element. The voltage stabilizer is connected with a voltage regulator. The single chip is provided with a display. A buzzer is connected with a cathode. An LED display is connected with a positive electrode. A positive pole is fixed with a voltage terminal.    USE - Suction pump type multiparameter tester for a mine.    ADVANTAGE - The tester has high precision, and detects methane, oxygen and carbon monoxide content in an effective manner and protects environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a suction pump type multiparameter tester. '(Drawing includes non-English language text)'
NOVELTY - The method involves compressing remain part stream of a first polymer separation membrane. Bio-gas is compressed and cooled in a second polymer separation membrane. The second polymer separation membrane is connected to a third polymer separation membrane. The third polymer separation membrane is connected to a fourth polymer separation membrane. Carbon dioxide is separated from transmission part stream through the second polymer separation membrane. Selectivity range of the carbon dioxide about methane is 20-100. Pressure of the bio-gas 5-100 bar.    USE - Method for separating methane gas from bio-gas generated in food waste and organic compound.    ADVANTAGE - The method enables compressing and cooling the bio-gas in the first polymer separation membrane, and connecting the second polymer separation membrane to the third polymer separation membrane so as to effectively separate high-purity methane gas from the carbon dioxide with high concentration, so that productivity and recovery rate about the high-purity methane gas can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a methane gas purifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a methane gas purifier.
NOVELTY - Cogenerating methanol and 2-4C alcohol, comprises passing feed gas containing carbon ester and synthesis gas through a reactor containing the catalyst, reacting at 150-350 degrees C, at reaction pressure of 0.1-20 MPa, where the reaction volume airspeed is 100-40000 ml/g/hour, weight hourly space velocity of low carbon ester is 0.01-3/hour, and cogenerating methanol and 2-4C alcohols; the catalyst active component is copper, and optionally zinc and/or aluminum.    USE - The method is useful for cogenerating methanol and 2-4C alcohol (claimed). Low carbon alcohol is used as liquid fuel material, and as additive to increase gasoline octane value.    ADVANTAGE - The method coproduces certain volume of 2-4C alcohols under the condition of using low-carbon ester and the synthesized gas as cofeed, can increase product diversity and economical efficiency, increases production flexibility and device operation flexibility, has important practical significance in coal chemical engineering industry, uses low carbon ester to promote catalytic reaction activity without affecting catalyst life, can greatly increase product flexibility to have market adaptability, realizes flexible operation and is suitable for large scale.
NOVELTY - Preparing 4-(2-(4-methylphenylthio)phenyl)piperidine (I), comprises carrying out reduction of 4-(2-(p-tolylsulfanyl)phenyl)piperidine-2,6-dione (II) in an organic solvent to obtain final product.    USE - The method is useful for preparing 4-(2-(4-methylphenylthio)phenyl)piperidine (claimed).    ADVANTAGE - The method: has high product yield; is safe, environment-friendly, and suitable for industrial production.    DETAILED DESCRIPTION - Preparing 4-(2-(4-methylphenylthio)phenyl)piperidine of formula (I) or its salts, comprises carrying out reduction of 4-(2-(p-tolylsulfanyl)phenyl)piperidine-2,6-dione of formula (II) in an organic solvent to obtain final product. INDEPENDENT CLAIMS are also included for:    (1) 3-(2-(p-tolylsulfanyl)phenyl)-pentanedioic acid (III) and 4-(2-(p-tolylsulfanyl)phenyl)piperidine-2,6-dione (II); and    (2) preparing 4-(2-(4-methylphenylthio)phenyl)piperidine hydrochloride salt (IX), comprising adding (I) to hydrochloric acid in presence of an organic solvent to obtain (IX).
NOVELTY - A composition comprises an organic solvent and lignin or its derivatives in which hydroxyl group(s) is substituted by ester group to form esterified lignin or its derivatives.    USE - Composition is used for producing lubricant and fuel (all claimed) e.g. diesel, petrol, analogs of diesel and petrol, biogasoline and biodiesel. Can also be used for preparing foams, plastics, rubbers, paint and aromatic compounds.    ADVANTAGE - The composition efficiently and economically provides fuel with reduced usage amount of oxygen, by simple method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of the composition, which involves mixing lignin or its derivatives with an esterification agent, or a fatty acid and an esterification agent, and optionally a catalyst, heating the mixture at 80 degrees C, reacting to obtain esterified biomass material, isolating the obtained esterified biomass material and mixing the esterified biomass material with a solvent; and    (2) manufacture of fuel, which involves treating the composition in hydrotreater or catalytic cracker.
NOVELTY - The apparatus has a filled layer (1a) that is set with filler to which microorganisms are adhered in multiple stages in a biological desulfurization column (1). An inflow gas line (5) is respectively connected to an upstream edge portion of the filled layer. The inflow gas line is set with a hydrogen-sulfide containing gas supply volume adjustment portion (7). A process-gas outflow line (10) is provided to discharge the process gas provided in a downstream edge portion of the filled layer formed at the side of downstream portion.    USE - Biological desulfurization apparatus for processing hydrogen-sulfide containing gas emitted during methane fermentation treatment of organic substance such as sewage, livestock excrement, excrement, industrial waste water, sludge, garbage and foodstuff residue.    ADVANTAGE - Highly efficient biological desulfurization process is maintained by distributing hydrogen-sulfide containing gas to the filled layer in multiple stages. The hydrogen sulfide in high load is processed efficiently. The obstruction in the apparatus is eliminated by converting the hydrogen sulfide into sulfuric acid. The need for performing the washing process is eliminated. The hydrogen-sulfide containing gas is processed at low-cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biological desulfurization method.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the outline of the biological desulfurization apparatus.    Biological desulfurization column (1)    Filled layer (1a)    Inflow gas line (5)    Hydrogen-sulfide containing gas supply volume adjustment portion (7)    Process-gas outflow line (10)
NOVELTY - Gaseous mixture is passed through an adsorption pipe (B) filled with a microporous adsorbent having high retention capacity for carbon dioxide than remaining components in exhaust gas containing nitrogen, such that adsorption pipe is increasingly loaded with carbon dioxide. The adsorption pipe is purged with nitrogen in opposite direction until the stored carbon dioxide is completely removed, and the resultant mixture of carbon dioxide and hydrogen is supplied to catalytic reactor for methanation.    USE - Separation of carbon dioxide from gaseous mixture e.g. exhaust gas obtained from combustion of fossil fuel.    ADVANTAGE - The method enables separation of carbon dioxide from gaseous mixture with excellent selectivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for separating carbon dioxide from gaseous mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of device for separating carbon dioxide from gaseous mixture.    Electrolyzer (A)    Adsorption pipe (B)    Catalytic reactor (C)    Fuel cell (D)    Electric lines (E1,E2)    Shutoff valves (V1,V2)    Three-directional valves (V3,V4)
NOVELTY - Method for isolation of milbemycins A3 or A4 from fermentation broth of microorganisms belonging to species of Streptomyces, involves (a) performing lyophilization of mycelium cake to obtain dry powder, (b) extracting dried cells with supercritical carbon dioxide, and (c) extracting carbon dioxide extract with methanol.    USE - The method is useful for isolation of milbemycins A3 or A4 from fermentation broth of microorganisms belonging to species of Streptomyces (claimed), where the milbemycins A3 or A4 is useful for providing anthelmintic, antiparasitic, acaricidal and insecticidal effects.    ADVANTAGE - The method is relatively nontoxic, noncorrosive, chemically stable and environmentally-friendly, and provides isolation of milbemycins A3/A4 with high purity and high recovery rate.
NOVELTY - Method for preparing microalgae with increased microalgae lipid content, involves culturing microalgae in stress conditions.    USE - The method is used for preparing microalgae with increased microalgae lipid content which is used in biomass (all claimed) for producing biodiesel.
NOVELTY - Synthesizing cerium oxide nanoparticles, comprises subjecting the cerium oxide solution to aqueous leaf extract of Cicer arietinum or proteome of Cicer arietinum leaf extract under conditions that reduces cerium ions to cerium oxide nanoparticles.    USE - The method is useful for synthesizing cerium oxide nanoparticles which are useful in various domains of biomedical applications and for treating and managing ocular disease comprising glaucoma (all claimed).    ADVANTAGE - The method: provides cerium oxide nanoparticles having an enhanced antioxidant property and an enhanced carbonic anhydrase inhibitory property (claimed); and is very simple and has eco-friendly approach.
NOVELTY - The utility model is new type relates to a portable a one carbon monoxide, comprising shell, liquid crystal display screen, an alarm indicator lamp, a power supply indication lamp, a charging wherein, loudspeaker, switch, circuit plate, a bandage, a infrared probe, infrared carbon monoxide sensor, information transmission wherein, and power supply, power supply for future use, a power supply and charging wherein a, circuit plate provided with the CPU and charging control circuit, storage device, input and a switching value output circuit, an acousto-optic alarm circuit, state indicating circuit, a power supply circuit, clock circuit, carbon monoxide detecting circuit, a detecting circuit and liquid crystal display screen connect, acousto-optic alarm circuit and a loudspeaker alarm indication lamp connected; a input and switching value input circuit and switch and information transmission wherein a, state indicating circuit and power supply indicating lamp connected, a charging control circuit and charging wherein, power supply and power supply conversion circuit connected the power source conversion circuit and also a transfer probe and a carbon monoxide sensor.
NOVELTY - The system has a gas refining system (2) equipped at a catalytic reactor (21) that is connected to a bypass pipeline (22). The bypass pipeline is coupled to a cyclone part (23). A first heat-exchanger opens a synthetic gas passage. A gasifier is fixed to an oxidizing agent recirculation system. A second heat-exchanger (44) collects heat of effluent. A wastewater treatment facility (45) delivers cooling water to a cooling apparatus (43). A third heat-exchanger (46) is provided with a scrubber (41). The third heat-exchanger collects heat of the cooling water to cool a power generator (15).    USE - System for generating combined heat and power by utilizing gasification biomass.    ADVANTAGE - The gas refining system is equipped at the catalytic reactor that is connected to the bypass pipeline so as to effectively remove contaminant or impurity present in synthetic gas through dry and wet gas purifiers, reduce exhaustion of the contaminant and recycle sludge and tar by utilizing the exhaust gas heat generated in the power generator, so that power generation efficiency, energy efficiency and fuel regeneration efficiency of the system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a system for generating combined heat and power by utilizing gasification biomass.'(Drawing includes non-English language text)'    Gas refining system (2)    Power generator (15)    Catalytic reactor (21)    Bypass pipeline (22)    Cyclone part (23)    Scrubber (41)    Cooling apparatus (43)    Heat-exchangers (44, 46)    Wastewater treatment facility (45)
NOVELTY - The utility model is new type relates to a cultivation field house outside a zero discharging device, wherein, comprising a farm sewage draining channel connected the sewage collecting pool, the sewage collecting pool upper part a and a is a part is connected, and a connecting pipe connected to the a t plant of a biological matrix. The utility model is new type outside cultivation field house zero discharging device by taking all dirt cultivation field by discharging channel discharging the sewage collecting pool to carry out unified collection, then into a hardening and tempering in a tempering process is conveyed after paved the plant biological matrix, thus to make the matrix in plant biology.. equal in one section of time effect, can be organic fertilizer using, thus it not only avoids the farm excrement sewage directly discharging equal to pollute environment, and can change waste as treasure and use.
NOVELTY - Chemical and UV-treated polymer of intrinsic microporous membrane involves preparing intrinsic microporous polymer, chemically crosslinking the intrinsic microporous polymer with crosslinking compound to produce chemically-crosslinked intrinsic microporous polymer and treating the resultant product with UV radiation for preset period of time to provide chemical and UV-treated polymer of intrinsic microporous membrane.    USE - Chemical and UV-treated polymer of intrinsic microporous membrane is used for separating fluid stream (claimed) e.g. separation of 3C or more hydrocarbons and carbon dioxide from natural gas and other gas streams.    ADVANTAGE - The chemical and UV-treated polymer of intrinsic microporous membrane has excellent permeability, chemical resistance and carbon dioxide/methane selectivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for separation of fluid stream, which involves contacting fluid stream with chemical and UV-treated polymer of intrinsic microporous membrane to separate fluid stream into permeate stream which passes through the chemical and UV treated polymer of intrinsic microporous membrane, and retentate stream which does not pass through the chemical and UV-treated polymer of intrinsic microporous membrane.
NOVELTY - The fertilizer facility has an electric bubble rising separator that separates drain water from a money livestock waste and ejects drain water in which foreign substance is included through an exhaust pump (280) to outside. The drain water is separated from a compressor (300) which stores foreign substance that is compacted after compressing foreign substance and removing moisture in a reservoir (244). The foreign substance included in drain water is filtered. A fibrous filter (400) discharges water in which foreign substance is filtered as outside through a blowing pump (410).    USE - Money livestock waste liquid state fertilizer facility used in stockbreeding farmhouse.    ADVANTAGE - The chemical coagulant for the coherence of the foreign substance included in the money livestock waste is unnecessary. The money livestock waste is continuously processed regardless of the environmental change. The regeneration of the bad smell due to additional decay of the reducing odor and residual foreign substance are suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the structure of the money livestock waste liquid state fertilizer facility.    Reservoir (244)    Exhaust pump (280)    Compressor (300)    Fibrous filter (400)    Blowing pump (410)
NOVELTY - An aquatic plant planting matrix filler comprises 38-52 wt.% white clay, 25-35 wt.% diatomite, 10-18 wt.% rice chaff, 5.5-11.5 wt.% calcium oxide, and 1.5-3.5 wt.% ferment bacteria in which ferment bacteria consists of 2000000000/g Bacillus subtilis, 3500000/g yeast, and 3000000 Actinomycete.    USE - An aquatic plant planting matrix filler for municipal sewage treatment (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of aquatic plant planting matrix filler which involves calcining white clay in kiln at 490-510 degrees C for 110-130 minutes, uniformly mixing rice chaff and ferment bacteria, naturally fermenting at 65-70 degrees C for 2 weeks, and uniformly mixing with diatomite and calcium oxide; and    (2) municipal sewage treatment using aquatic plant planting matrix filler which involves mixing aquatic plant planting matrix filler, natural water, and brown sugar at weight ratio of 1:0.3:0.006, using after 3 hours, planting reed and aquatic plant in matrix filler, placing in municipal sewage A/O system O segment, starting use, adding 12 kg of ferment bacteria, 6 kg of sugar, and 60 kg of water per 1000 kg matrix for interval of 9-11 days, spraying into filler, planting for 2 hours, and putting in O section aeration pool.
NOVELTY - Method for preparing compound fertilizer involves mixing sheep manure, straw, pumpkin vine, tea leaf and chitosan. Nitrogen-phosphorus-potassium (4-10%) of glutamic acid (2-4%), serine (0.2-0.5%), leucine (0.1-0.2%), tyrosine (0.3-0.8%) and amino acid (4-8%) are added in the obtained mixture. The mixture is pulverized and dried to reduce water content by 60%. Hydrated lime, potassium fulvate, nano non-metal mineral material and sodium selenite are mixed and stirred uniformly with the product. Mixture is dried and ground and then mixed uniformly.    USE - Method for preparing compound fertilizer used for preventing and treating southern blight disease of Clivia miniata (claimed).    ADVANTAGE - The method enables to prepare compound fertilizer that reduces use of fungicide, and restrains generation of plant diseases.    DETAILED DESCRIPTION - Method for preparing compound fertilizer involves mixing sheep manure, straw, pumpkin vine, tea leaf and chitosan. Nitrogen-phosphorus-potassium (4-10%) of glutamic acid (2-4%), serine (0.2-0.5%), leucine (0.1-0.2%), tyrosine (0.3-0.8%) and amino acid (4-8%) are added in the obtained mixture. The mixture is pulverized and dried to reduce water content by 60%. Hydrated lime, potassium fulvate, nano non-metal mineral material and sodium selenite are mixed and stirred uniformly with the product. Mixture is dried and ground and then mixed uniformly with Trichoderma harzianum, Saccharomyces cerevisiae and effective microorganisms to carry out fermentation, and then granulated.
NOVELTY - Organic fertilizer comprises 2 pts. wt. ammonium molybdate, 3 pts. wt. naphthalene acetic acid, 4 pts. wt. magnesium sulfate, 8 pts. wt. ferrous sulfate, 12 pts. wt. urea, 15 pts. wt. potassium mineral powder, 15 pts. wt. phosphate rock powder, 3.5 pts. wt. microelement, 15 pts. wt. tobacco stick, 40 pts. wt. human excrement, 10 pts. wt. sugar, 20 pts. wt. mushroom residue, 20 pts. wt. sawdust, 20 pts. wt. peanut shell powder, 20 pts. wt. fly ash and 10 pts. wt. sweet potato powder.    USE - Organic fertilizer used for planting cabbage (claimed).    ADVANTAGE - The organic fertilizer improves yield and physical and chemical properties of soil, and enhances cabbage lodging capacity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) mixing human manure, sawdust and fly ash in a container in and carrying out fermentation for 7 days to obtain fermentation product;    (B) mixing remaining components with the fermentation product at speed of 10-25 revolutions per minute; and    (C) drying the mixture in a drier for 25-35 minutes to obtain organic fertilizer to obtain final product.
NOVELTY - Organic fertilizer comprises 30 pts. wt. rotten fruits and vegetables, 15 pts. wt. biological bone material, 80 pts. wt. attapulgite, 9 pts. wt. Celastrus angulatus, 5 pts. wt. green southernwood residue, 12 pts. wt. urea, 3.5 pts. wt. trace element, 5 pts. wt. amino acid, 15 pts. wt. duck feather, 40 pts. wt. chicken manure, 20 pts. wt. longan shell, 20 pts. wt. fly ash and 10 pts. wt. sweet potato powder.    USE - Organic fertilizer used for planting cabbage (claimed).    ADVANTAGE - The organic fertilizer prevents insecticidal disease, and ensures high yield and insect repellent effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) fermenting rotten fruits and vegetables, chicken manure and fly ash in container for 7 days;    (B) mixing fermented materials with remaining ground materials using mixer for l0-25 minutes; and    (C) drying obtained mixture for 25-35 minutes to obtain organic fertilizer.
NOVELTY - Biodegradable slow release fertilizer comprises 62-75 pts. wt. straw, 45-53 pts. wt. vegetable, 15-20 pts. wt. chitin, 33-37 pts. wt. coal ash, 15-18 pts. wt. urea, 10-13 pts. wt. ammonium dihydrogen phosphate, 26-33 pts. wt. leaves, 8-10 pts. wt. leavening agent and 3.5-4.5 pts. wt. trace element.    USE - Biodegradable slow release fertilizer used for crops.    ADVANTAGE - The biodegradable slow release fertilizer is eco-friendly, and increases yield of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biodegradable slow release fertilizer, which involves:    (A) crushing straw and leaves in a crushing machine;    (B) adding remaining components with the mixture, and then performing fermentation for 25-30 days;    (C) mixing ammonium dihydrogen phosphate and trace element with the fermented product; and    (D) drying the product, and then granulating.
NOVELTY - Organic ecological fertilizer comprises 20-32% urea, 15-25% monoammonium phosphate, 15-22% coal fertilizer, 20-30% potassium chloride or potassium sulfate, 3-5% vegetable organic matter, 3-8% humic acid, 2-5% biological amino acid, 1-3% trace element and 1-2% beneficial bacteria.    USE - Organic ecological fertilizer used for restoring soil (claimed).    ADVANTAGE - The organic ecological fertilizer ensures good effect, increased soil surface area, improved soil plate structure and increased soil water capacity and crop drought resistance.
NOVELTY - Organic fertilizer comprises 20 pts. wt. animal viscera, 40 pts. wt. pig manure, 8 pts. wt. bagasse, 15 pts. wt. ponds sludge, 20 pts. wt. bamboo root, 10 pts. wt. oil cake fermentation liquid, 18 pts. wt. pea and 20 pts. wt. potassium dihydrogen phosphate.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer is eco-friendly, and increases plant yield, increases environmental protection and reduce waste discharge and chemical fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) heating animal viscera at 85-95 degrees C with water to obtain bone slurry that is milled to obtain mixture;    (B) crushing bagasse, bamboo root and pea in a stirrer to obtain powder;    (C) mixing obtained powder and mixture with remaining materials;    (D) fermenting obtained mixture for 3-10 days at 25-30 degrees C; and    (E) drying fermented product to obtain desired product.
NOVELTY - Soil regulator comprises 2-8 pts. wt. Angelica, 3-5 pts. wt. radix bupleuri, 1-5 pts. wt. Astragalus membranaceus, 5-10 pts. wt. straw, 8-12 pts. wt. wheat, 10-15 pts. wt. inorganic fertilizer, 1-3 pts. wt. trace element fertilizer, 1-2 pts. wt. microbial inoculum, 2-3 pts. wt. nanosilicon oxide and 15-20 pts. wt. deionized water.    USE - Soil regulator used for planting (claimed) melon and its fruit.    ADVANTAGE - The soil regulator is prepared in a simple, eco-friendly and cost-effective manner, reduces attack of insect pests and increases stress resistance of melon and fruit while growing, ensures no toxicity, and improves physical and chemical properties of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing soil regulator, which involves:    (A) crushing wheat straw and fermenting it;    (B) mixing and stirring inorganic fertilizer, trace element fertilizer and then dissolving deionized water to obtain fertilizer solution;    (C) spraying the fertilizer solution on fermented wheat straw, and then dissolving microorganism microbial inoculum with deionized water and spraying it;    (D) crushing Angelica, radix bupleuri and Astragalus membranaceus and extracting with deionized water at 60-80 degrees C for 30-80 minutes to obtain extraction liquid; and    (E) mixing remaining components with extraction liquid to obtain final product.
NOVELTY - A hardwood biomass fuel is prepared by performing primary crushing in hardwood, performing secondary crushing to obtain sawdust, adding coal slime, uniformly stirring to obtain mixture, and thermoforming.    USE - Preparation of hardwood biomass fuel for boiler.    ADVANTAGE - Process is environment-friendly and has reduced production cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram for preparation of hardwood biomass fuel. (Drawing includes non-English language text).
NOVELTY - Cultivation of golden needle mushroom involves weighing Ginkgo biloba leaf, corn cobs, wheat bran and gypsum, crushing, adding 15-25 wt.% parent cellulase, performing enzymatic biodegradation to obtain base material, adding binder, gypsum, sugar and water, adjusting pH to 4-6 to obtain cultivation matrix, inoculating bacteria, standing for 7-15 days at 20-26 degrees C to obtain mycelium with diameter of 4-5 cm with 10 layers and harvesting.    USE - Method for cultivating golden needle mushroom (claimed).    ADVANTAGE - The method is inexpensive, simple, efficient, and environmental-friendly and has high biological conversion rate.
NOVELTY - A metal organic frame adsorbent comprises active ingredient e.g. silver(I) (Ag(I)) loaded on carrier e.g. sulfonic acid-functionalized metal organic frame (MIL-101(Cr)-SO3H) with loading amount of 10-40 wt.%.    USE - A metal organic frame adsorbent for separating alkene/alkane mixed gas and removing sulfur-containing compounds in fuel (all claimed).    ADVANTAGE - Metal organic frame adsorbent has high alkene/alkane mixed gas separation selectivity, good desulfurizing effect, strong adsorption effect, large adsorption amount, and improved water stability, and preparation is simple and has mild conditions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for:    (1) preparation of metal organic frame adsorbent which involves preparing MIL-101(Cr)-SO3H, mixing with Ag(I), and performing ion exchange reaction to obtain adsorbent (MIL-101(Cr)-SO3Ag);    (2) use of metal organic frame adsorbent for separating alkene/alkane mixed gas in which alkene is ethylene, propylene, and/or butene, and alkane is ethane, propane, and/or butane; and    (3) use of metal organic frame adsorbent for removing sulfur-containing compounds in fuel in which sulfur-containing compound is thiophene, benzothiophene, dibenzothiophene, or 4,6-dimethyl dibenzothiophene.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the x-ray diffraction (XRD) of metal organic frame adsorbent and sulfonic acid-functionalized metal organic frame.
NOVELTY - Livestock and poultry breeding manure is treated by collecting livestock and poultry breeding manure through grid, flowing into sedimentation tank to remove large impurity, flowing into jet mixing digester to remove manure particulate matter, converting manure which is rich in ammonia nitrogen into nitrogen, aerobically digesting, lifting submersible pump, entering into anaerobic reactor with anaerobic microorganism to generate methane and water, adding converted nitrogen denitrifying bacteria, and reducing anaerobically treated manure chemical oxygen demand (COD) to 2000 mg/L.    USE - Treatment of livestock and poultry breeding manure for agricultural irrigation.    ADVANTAGE - Process is low cost and environment-friendly, does not need to add medicament, and has simple operation and maintenance, and product has active promoting effect.    DETAILED DESCRIPTION - Livestock and poultry breeding manure is treated by collecting livestock and poultry breeding manure through grid, flowing into sedimentation tank to remove large impurity, flowing into jet mixing digester to remove manure particulate matter, converting manure which is rich in ammonia nitrogen into nitrogen, aerobically digesting, lifting submersible pump, entering into anaerobic reactor with anaerobic microorganism to generate methane and water, adding converted nitrogen denitrifying bacteria, reducing anaerobically treated manure COD to 2000 mg/L, flowing into combined jet aeration tank, discharging manure having COD of 200 mg/L into discharging tank, and inspecting in which jet mixing digester is provided with jet mixing aerator and circulating submersible pump, generated biogas is used as manure, and jet aeration tank is provided with jet aerator and circulating pump.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram for treatment of livestock and poultry breeding manure. (Drawing includes non-English language text).
NOVELTY - An air pressure promoting biogas slurry circulation methane generating device comprises feeding pipe (11), discharging pipe (12), horizontal U-type fermentation pipeline (20) vertically connected to feeding pipe and discharging pipe at its 2 ends in which U-type fermentation pipeline is provided with hydraulic pressure part (30) at upper part, discharge hole (32) set in middle of feeding pipe and hydraulic pressure part, and below discharging pipe draining hole, draining hole, feeding pipe blocking plate, gas collecting pipe blocking plate, and gas collecting manifold.    USE - Air pressure promoting biogas slurry circulation methane generating device.    ADVANTAGE - The device controls water pressure, achieves sufficient methane liquid flow in system, uniformly distributes strain, and effectively prevents crusting phenomenon.    DETAILED DESCRIPTION - An air pressure promoting biogas slurry circulation methane generating device comprises feeding pipe, discharging pipe, horizontal U-type fermentation pipeline vertically connected to feeding pipe and discharging pipe at its 2 ends in which U-type fermentation pipeline is provided with hydraulic pressure part at upper part, discharge hole set in middle of feeding pipe and hydraulic pressure part, and below discharging pipe draining hole, draining hole set in middle of discharging pipe and hydraulic pressure part, feeding pipe blocking plate connected to feeding pipe, gas collecting pipe blocking plate connected to discharging pipe, and gas collecting manifold, and feeding pipe is provided with one-way check valve which controls room pressure as slurry flows to discharge holes.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural schematic diagram of air pressure promoting biogas slurry circulation methane generating device.    Feeding pipe (11)    Discharging pipe (12)    Horizontal U-type fermentation pipeline (20)    Hydraulic pressure part (30)    Discharge hole (32)
NOVELTY - Preparation of sludge compost includes adding chitosan, iron salt and lime conditioning agent-containing sludge mixture into filter press to carry out dewatering sludge; adding into rapid fermentation equipment with crushed straw or grass and mushroom soil, fermenting with organic manure fermentation agent, stirring, heating, and degrading using mesophilic bacteria; and distributing into fermentation groove to carry out ripening, adding fungicide and humic acid chelate, mixing, granulating, naturally drying, and packing.    USE - Method for preparation of sludge compost (claimed).    DETAILED DESCRIPTION - Preparation of sludge compost comprises:    (A) adding chitosan, iron salt and lime conditioning agent-containing sludge mixture having 95-99% moisture content into filter press to carry out dewatering sludge until moisture content is 60-70%;    (B) adding into rapid fermentation equipment with crushed straw or grass and mushroom soil at volume ratio of 1:2-3:1 or mass ratio of 1:1-5:1, fermenting with 0.5-1 wt.% organic manure fermentation agent, stirring using rotating blade, opening heating and ventilation system equipment to carry out rapid increasing of temperature to 50-70 degrees C for 2 days to kill harmful microorganisms, and degrading using mesophilic bacteria; and    (C) distributing into fermentation groove to carry out ripening while turning the material to cool down, adding 1-2 wt.% fungicide and 0.5-1 wt.% humic acid chelate after 3 weeks, mixing, granulating, naturally drying, and packing.
NOVELTY - The application method of wine lees as replacement for coal in combustion process involves manually collecting waste lees and loading, transferring collected waste lees to dry plate of waste distiller, evenly apportioning waste lees to each plate, then stirring waste lees to spread uniformly, drying spread waste lees, and storing dried waste lees in bag for use as fuel for combustion.    USE - Application method of wine lees as replacement for coal in combustion process (claimed).    ADVANTAGE - The method enables easy, convenient, practical and affordable processing of wine lees as replacement of coal for combustion and enhances utilization of waste lees, production efficiency and drying rate.
NOVELTY - Producing methane using methane generation system, comprises passing fermenting material from the feed tube into the fermentation pipeline for fermenting methane, collecting the methane in the inlet/outlet pipe and between the adjacent air resistance plates or fermentation area, extruding the methane in the fermentation area to form biogas slurry, passing the slurry into feed tube, discharge pipe, strain containing cloth device, and discharging the biogas slurry through the feed tube drain holes in unidirectional inflow, at room pressure.    USE - The method is useful for producing methane using methane generation system (claimed).    DETAILED DESCRIPTION - Producing methane using methane generation system, comprises passing fermenting material from the feed tube into the fermentation pipeline for fermenting methane, collecting the methane in the inlet/outlet pipe and between the adjacent air resistance plates or fermentation area, extruding the methane in the fermentation area to form biogas slurry, passing the slurry into feed tube, discharge pipe, strain containing cloth device, and discharging the biogas slurry through the feed tube drain holes in unidirectional inflow, at room pressure; (b) storing the methane in the fermentation zone, dropping the pressure in the fermentation zone, allowing the biogas slurry to flow into the fermentation zone, and completing the biogas slurry circulation; and (c) using the methane.
NOVELTY - Sludge fermentation agent comprises 15-25 pts. Bacillus subtilis, 10-20 pts. Bacillus stearothermophilus, 8-15 pts. lactic acid bacteria, 5-10 pts. silicate bacteria, 4-10 pts. Nocardia actinomycetes, 9-16 pts. Azotobacter chroococcum, 1-6 pts. Saccharomyces cerevisiae, 1-5 pts. yellow rice, 2-3 pts. photosynthetic bacteria, 1-3 pts. Streptomyces, 6-13 pts. cellulose, 5-12 pts. amylase and 5-6 pts. xylanase.    USE - Used as sludge fermentation agent.    ADVANTAGE - The sludge fermentation agent: does not cause environmental pollution, and has low operating costs; kills pathogens in sludge and parasite eggs; degrades toxic and harmful substances; accelerates sludge deodorization and dehydration; and decomposes crops that have difficulty in absorbing nutrients.
NOVELTY - Preparing biogas, comprises processing solid household rubbish sorted by sieving the material, and pre-processing kitchen rubbish, sludge and feces, and then transferring the pre-processed organic material into a biogas anaerobic fermentation reactor, subjecting the fermented material to solid-liquid separation, and storing 20-30% biogas in a sewage collection pool, refluxing, and quenching.    USE - The method is useful for preparing biogas (claimed).    ADVANTAGE - The method can utilize various organic material during treatment process; prevents the shortcomings of existing single anaerobic fermentation engineering problem of raw materials caused by urbanization; can reduce water consumption of the system while refluxing biogas slurry; and improves the performance of fermentation system, gas production rate, and system stability.
NOVELTY - Preparing biodiesel, comprises (i) culturing microalgae; and (ii) fermenting the cultured microalgae by using fermentation bacteria, namely Trichoderma species and Rhizopus, and taking fermentation culture medium includes 20-30 g/l microalgae, 3-5 g/l sodium citrate, 1.5-2.5 g/l toluidine, 10-15 g/l sodium chloride, 0.5-1 g/l potassium dihydrogen phosphate and 3-5 g/l magnesium sulfate; (iii) extracting oil from the fermented product; and (iv) carrying out enzyme catalytic reaction.    USE - The method is useful for preparing biodiesel (claimed).    ADVANTAGE - The method has rapid production rate, and is economical.
NOVELTY - Device comprises a carbon dioxide cylinder, an algae holding container (preferably, sterilized bottles), an air and carbon dioxide carrying tubes, an air pump, a nutrient carrying tubes, a nutrient input basin, a wooden casing side, a wooden casing top and an acrylic sheet cover.    USE - The device is useful in the production of algae fuel by fabrication of algae-breeder, photo-bioreactor and oil-extraction system (claimed).    ADVANTAGE - The device produces low cost algae bio-fuel available in every household, and comprising wooden casing side reduces heat exchange with surroundings, and acrylic sheet cover reduces the contamination of the inner components, and tubes or containers utilized in algae growth; and has compact design (claimed); and is suitable for easy industrial growth of algae.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device.    Carbon dioxide cylinder (1)    Algae holding container (2)    Air and carbon dioxide carrying tubes (3)    Air pump (4)    Nutrient carrying tubes (5)
NOVELTY - Hassle free, convenient and odor free composting process of organic material, is claimed. The composting of organic material is even performed in domestic environment.    USE - The composting process of organic material is useful for producing organic manure used for enhancing soil fertility, and in growing medium used in home gardens for growing vegetables and flowers (all claimed).    ADVANTAGE - The composting process absolutely causes no foul smell, enables biodegradable waste generating foul smell when introduced into composting medium, to lose foul smell immediately, produces no leachate during process, prevents breeding of flies by maintaining moisture at optimum level, eliminates need of frequent turning of material and thus reduces cost incurred for turning, avoids frequent watering of heap as compositing media has excellent water retention properties, utilizes composting media that ensures optimum temperature for most efficient composting, exhibits efficient and complete breakdown of organic material to prevent possibility of evolution of any unwanted gases like carbon monoxide, and hydrogen sulfide, requires no capital investment, and produces high quality organic manure with pleasant odor and that can be handled very conveniently. The organic manure ensures quality and safety, and healthy plant growth which is not easily susceptible to pest and disease, and enables to easily maintain crops having very high nutritive value.
NOVELTY - Composition comprises sewage and liquefied fertilizer as active ingredients.    USE - The composition is used for cultivating microalgae, preferably Micractinium inermum strain NLP-F014 (all claimed) which is used in biofuel composition.    ADVANTAGE - The composition enables to improve lipid productive capacity and 16-18C fatty acid content of microalgae.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for cultivating microalgae; and    (2) method for recycling composition.
NOVELTY - Cultivation and fertilization of blueberry comprises collecting cow dung, covering with corn, fermenting for 2-3 months; collecting pine sawdust, stacking, fermenting for 8-9 months; collecting pine needle and raw humus soil as source materials; uniformly mixing cow dung, pine sawdust, pine needle and raw humus soil at mass ratio of 5:3:3:15, taking 38 kg fertilizer, placing into planting hole, transplanting blueberry seedlings for 2 months/hole, applying to 50 g nitrogen fertilizer for 8 months/hole, and adding 50 g nitrogen fertilizer as topdressing.    USE - Method for cultivating and fertilizing blueberry (claimed).    ADVANTAGE - The method increases yield to 15-20% and improves taste of the fruit and soil annually.
NOVELTY - Scientifically cultivating kidney beans comprises plowing soil rich in organic matter, drying for 3-5 days, building ridge, adding fermented slow-release fertilizer, soaking seed in diluted fungicide, planting, irrigating and spraying liquid fertilizer.    USE - Method for scientifically cultivating kidney beans (claimed).
NOVELTY - A neem pixel effervescence piece comprises 0.1-3 wt.% azadirachtin, 1-20 wt.% neem oil, 6-45 wt.% disintegrant, 1-20 wt.% wetting agent, 1-20 wt.% dispersant and balance filler.    USE - Neem pixel effervescence piece used for family gardening (claimed).    ADVANTAGE - The piece completely contacts target, has low toxicity, and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of neem pixel effervescence piece comprising taking each raw material, mixing, air flow pulverizing, sieving through 75 mu m, wet kneading with binder, tableting, drying, temperature controlling at 18-21 degrees C and humidity of 20-25%, evaporating, and packing.
NOVELTY - Cultivating Chinese cabbage comprises soaking seeds in water at 30 degrees C, cooling to 20 degrees C for 2 hours, adding 0.4% chlorothalonil and 0.5 wt.% potassium permanganate for 20 minutes, washing at 20 degrees C, selecting greenhouse, irrigating, plowing, sprinkling organic slow-release fertilizer, adding nutritional fertilizer and watering.    USE - Method for cultivating Chinese cabbage (claimed).    ADVANTAGE - The method is environment-friendly and has reduced fertilizer usage.
NOVELTY - Cultivating tomato comprises building greenhouse with 3-4 layers plastic film, irrigating, adding organic soil, sprinkling potassium permanganate solution on seedling pot, planting, adding slow-release fertilizer, mixing with soil, irrigating, controlling amount of sunlight in greenhouse, and controlling temperature at 20-25 degrees C during daytime and 13-18 degrees C at nighttime.    USE - Method for cultivating tomato (claimed).
NOVELTY - A crop waste straw stick adsorbent is prepared by selecting lignified or fibrosis crop waste straw stick, removing impurity and crushing to 1-2 cm, drying to obtain 1st material, smashing 1st material by pulverizer, sieving into 80-120 meshes screen to obtain powdered blank, placing into crucible, heating to 450 degrees C under anaerobic condition, preserving heat for 40 minutes, and cooling to room temperature.    USE - Preparation of crop waste straw stick adsorbent for processing of chromium containing sewage and regeneration adsorbent (claimed).    ADVANTAGE - Product reduced production cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) processing of chromium containing sewage which involves adding acid, controlling pH to 2, controlling chromium concentration to 95-105 mg/L, using 0.38-0.42 g adsorbent per 1 L of chromium salt containing wastewater, stirring, removing 80% of pollutants containing chromium salt; and    (2) processing of regeneration adsorbent which involves preparing 0.1 mol/L hydrochloric acid (HCl), adding 0.4 g adsorbent per 1 L of HCl, stirring at room temperature for 2.5 hours, filtering, washing, and drying.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of laser particle size distribution measurement results. (Drawing includes non-English language text).
NOVELTY - Preparing compound fertilizer and cogeneration of dihydrogen phosphate involves reacting urea and phosphoric acid in molar ratio of 1.3:1.6-2.1 at 121-126 degrees C. The mixture is stirred at speed of 60-65 revolutions per minute fort 2.4 hours to obtain intermediate compound. Intermediate compound is reacted with sodium hydroxide for 86-94 minutes and maintained pH at 3.4-4 to obtain sodium dihydrogen phosphate containing nitrogen, phosphorus and mother liquid of sodium carbonate. Mother liquid of sodium carbonate is crystallized in a cooling crystallizer to obtain crystal.    USE - Method for preparing compound fertilizer and cogeneration of dihydrogen phosphate used for fennel (claimed).    ADVANTAGE - The method enables to prepare compound fertilizer and cogeneration of dihydrogen phosphate in a cost-effective and eco-friendly manner, and produces pure dihydrogen phosphate.    DETAILED DESCRIPTION - Preparing compound fertilizer and cogeneration of dihydrogen phosphate involves reacting urea and phosphoric acid in molar ratio of 1.3:1.6-2.1 at 121-126 degrees C. The mixture is stirred at speed of 60-65 revolutions per minute fort 2.4 hours to obtain intermediate compound. Intermediate compound is reacted with sodium hydroxide for 86-94 minutes and maintained pH at 3.4-4 to obtain sodium dihydrogen phosphate containing nitrogen, phosphorus and mother liquid of sodium carbonate. Mother liquid of sodium carbonate is crystallized in a cooling crystallizer to obtain crystal. The crystal is analyzed which comprises 15.4-15.9% nitrogen, 7.4-7.9% phosphorus pentoxide and 4.4-4.9% sodium. Crystal is filtered to obtain a filter cake, and then heated at 28 degrees C for 40 minutes to carry out drying to obtain compound fertilizer with water content 4%.
NOVELTY - Ventilation of sludge compost is regulated by fermenting sludge and wood material for 5-7 days, adding crushed straw, furfural slag, rice hull and plant ash, stirring uniformly, constantly raising temperature to 60-65 degrees C, and stacking fermenting for 8-10 days.    USE - Method for regulating ventilation of sludge compost (claimed).    ADVANTAGE - The method has short fermentation time and reduced cost.
NOVELTY - Organic manure fertilizer fermentation equipment comprises fermentation tank (1) that is provided with inner coil, axis and fermentation tank plate pipe. The plate pipe has coil plate pipe inlet and plate pipe outlet that is connected with water pipe and orderly connected with water heater, water heating room (2), water pump (4), boiler room (5), boiler water pump (3) and fermentation tank inlet. The fermentation tank inlet is connected with marsh gas tank and marsh gas boiler that is provided with speed reducing motor and stirring shaft set with stirring blade.    USE - Organic manure fertilizer fermentation equipment.    ADVANTAGE - The equipment ensures low energy consumption and high income.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of organic manure fermentation equipment.    Fermentation tank (1)    Water heating room (2)    Boiler water pump (3)    Water pump (4)    Boiler room (5)
NOVELTY - Preparing foliar fertilizer involves crushing 100 kg fermented dry cow dung and 500 mg sodium silicate, where crushed materials are diluted with water. The obtained mixture is matured for 60 days. The obtained material is washed with water. The washed material is decomposed with olive oil for 48-72 hours at room temperature. The decomposed material is mixed with leavening agent for 24 hours to obtain product.    USE - The method enables to prepare effective foliar fertilizer that increases selenium content in soil, and ensures simple preparation.
NOVELTY - Preparing organic fertilizer involves sterilizing 90-110 pts. wt. crop residues, 30-40 pts. wt. poultry manure, 4-6 pts. wt. yeast, 3-5 pts. wt. crushed organic fertilizer, 4-6 pts. wt. soybean lecithin, 8-12 pts. wt. glutamic acid mother liquid, 9-11 pts. wt. nutshell, 4-6 pts. wt. red yeast rice, 2-4 pts. wt. zinc carbonate, 1-3 pts. wt. tea saponin, 1-3 pts. wt. radix sophorae flavescentis aqueous extract, 2-4 pts. wt. jujube core powder, 0.5-2 pts. wt. Osmanthus aqueous extract, 2-4 pts. wt. sawdust, 1-3 pts. wt. starch glucoamylase and 1-3 pts. wt. lees for 40 minutes.    USE - Method for preparing organic fertilizer composition (claimed).    DETAILED DESCRIPTION - Preparing organic fertilizer involves sterilizing 90-110 pts. wt. crop residues, 30-40 pts. wt. poultry manure, 4-6 pts. wt. yeast, 3-5 pts. wt. crushed organic fertilizer, 4-6 pts. wt. soybean lecithin, 8-12 pts. wt. glutamic acid mother liquid, 9-11 pts. wt. nutshell, 4-6 pts. wt. red yeast rice, 2-4 pts. wt. zinc carbonate, 1-3 pts. wt. tea saponin, 1-3 pts. wt. radix sophorae flavescentis aqueous extract, 2-4 pts. wt. jujube core powder, 0.5-2 pts. wt. Osmanthus aqueous extract, 2-4 pts. wt. sawdust, 1-3 pts. wt. starch glucoamylase and 1-3 pts. wt. lees for 40 minutes at 90-110 degrees C. The sterilized materials are kneaded in vacuum for 5-10 minutes. The obtained material is fermented at 70 degrees C. The fermented material is coo1ed and then maintained at 20 degrees C for 2 hours. The obtained material is dried at 50-60 degrees C with hot air. The dried material is pelletized and packaged.
NOVELTY - Organic foliar fertilizer comprises 10 wt.% bone powder, 20 wt.% onion leaves, 20 wt.% rapeseed residue, 10 wt.% edible vinegar, 30 wt.% water hyacinth, 10 wt.% Rhodospirillum rubrum extract and 0.1 wt.% fermentation agent comprising 20 wt.% actinomycete, 10 wt.% Monascus, 10 wt.% Aspergillus niger, 10 wt.% white Geotrichum candidum, 10 wt.% Bacillus megaterium, 5 wt.% Bacillus subtilis, 10 wt.% Bacillus altitudinis, 5 wt.% Bacillus benzoevorans, 10 wt.% Saccharomyces cerevisiae yeast and 10 wt.% Candida.    USE - Organic foliar fertilizer used for promoting rice spike (claimed).    ADVANTAGE - The organic foliar fertilizer increase rice quality and reduces chalkiness and prevents rice from Aspergillus infection, and is rich in zinc and selenium.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic foliar fertilizer, which involves:    (A) fermenting water hyacinth, rapeseed residue and onion leaves fermentation kettle with fermentation agent at 110 degrees C for 24 hours;    (B) soaking bone powder in edible vinegar for 3 days;    (C) mixing fermented materials soaked bone powder and water for 2 days; and    (D) mixing obtained mixture with rubrum extract to obtain product.
NOVELTY - Pit well-type nutritional soil comprises 62.0-66.0 sandstone and shale, 10.0-12.0 sand, 10.0-12.0 plant residue, 4.5-5.0 rotten rapeseed cake fertilizer, 5.0-5.5 calcium superphosphate, 2.0-2.2 potassium nitrate and 1.8-2.0 potassium chloride. Sandstone and shale are broken to obtain mixture of quartz, feldspar, kaolin, montmorillonite and water. Sand is river sand. The pit well-type nutritional soil pH value is 7.5-8.5, is prepared by utilizing a coal burning power generation plant, which is made of silicon dioxide, aluminum oxide, ferric oxide, calcium oxide.    USE - Pit well-type nutritional soil used for planting and transplanting flue-cured tobacco seedling, and used in agricultural fertilizers (all claimed).    ADVANTAGE - The pit well-type nutritional soil improves soil and quality flue-cured tobacco, promotes survival rate of tobacco seedling in early stage, and has improved air permeability and hydrophobic property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing pit well-type nutritional soil, which involves:    (A) crushing sandstone and shale, sand, plant residue, calcium superphosphate and potassium nitrate through 18 meshes sieve to obtain powder; and    (B) fermenting rapeseed cake fertilizer for 3-4 months, and then mixing powder to obtain final product.
NOVELTY - Fertilizer comprises 40-50 pts. wt. organic matter, 15-20 pts. wt. urea, 8-12 pts. wt. ammonium nitrate, 5-8 pts. wt. calcium superphosphate, 10-20 pts. wt. potassium chloride, 5-10 pts. wt. diammonium phosphate, 1-2 pts. wt. magnesium sulfate, 1-2 pts. wt. ferrous sulfate, 1-2 pts. wt. copper sulfate, 1-3 pts. wt. soil conditioner and 1-3 pts. wt. microbial inoculum.    USE - Fertilizer used for planting tobacco (claimed).    ADVANTAGE - The fertilizer is nutritious, and resolves low soil organic matter content and soil compaction problems.
NOVELTY - Synthesis of diisopropyl azodicarboxylate comprises adding alkali and solvent to isopropyl hydrazine and diethyl carbonate, heating and reacting under inert gas protection at 100-180 degrees C for 2-6 hours, regulating pH to 4.5-7.5 filtering to obtain hydrogenated diisopropyl azodiformate, adding 40-50% sulfuric acid solution at - 20 to 25 degrees C, dissolving, adding catalyst, reacting at - 15 to - 5 degrees C, adding dropwise 10-15% hydrogen peroxide, continuously reacting for 5-10 hours, quenching, extracting, water washing to neutral, drying, filtering and concentrating.    USE - Method for synthesizing diisopropyl azodicarboxylate (claimed).    ADVANTAGE - The method has clean and environment-friendly raw materials, mild reaction condition, little by-product, high product yield, and good implementation for industrial production.
NOVELTY - Preparation of 2-(2-N-butyl-4-hydroxy-6-methyl-pyrimidin-5-yl)-N, N-dimethylacetamide (I) comprises reacting 2-(2-N-butyl-4-hydroxy-6-methyl-pyrimidin-5-yl)-acetic acid (II) and carbonyl diimidazole (III) with solvent in the presence of base; and reacting with dimethylamine.    USE - Method for preparing 2-(2-N-butyl-4-hydroxy-6-methyl-pyrimidin-5-yl)-N,N-dimethylacetamide used as fimasartan intermediate (claimed).    ADVANTAGE - The method restrains urea by-product, is simple and easy, increases production efficiency, saves large amount of extracting solvent and energy consumption, and reduces production cost.    DETAILED DESCRIPTION - Preparation of 2-(2-N-butyl-4-hydroxy-6-methyl-pyrimidin-5-yl)-N, N-dimethylacetamide (I) comprises reacting 2-(2-N-butyl- 4-hydroxy-6-methyl-pyrimidin-5-yl)-acetic acid (II) and carbonyl diimidazole (III) with solvent in the presence of base; and reacting with dimethylamine.
NOVELTY - Preparation of 2-(3-cyano-4-hydroxy)phenyl-4-methyl-5-thiazole formate (I) comprises reacting 4-cyanophenol (II) with curing agent to prepare 4-hydroxythiobenzamide (III) and reacting with 2-chloro-3 ethyl acetoacetate to prepare 2-(4-hydroxyphenyl)-4-methyl-thiazole-5-carboxylicacid ethyl ester (IV); reacting with hexamethylenetetramine to prepare 2-(4-hydroxyphenyl)-4-methyl-thiazole-5-carboxylicacid ethyl ester derivative (V); and carrying out reduction reaction.    USE - Method for preparing 2-(3-cyano-4-hydroxy)phenyl-4-methyl-5-thiazole formate (claimed).    ADVANTAGE - The method has high yield and no tertiary waste discharge and recovers solvent.    DETAILED DESCRIPTION - Preparation of 2-(3-cyano-4-hydroxy)phenyl-4-methyl-5-thiazole formate (I) comprises reacting 4-cyanophenol (II) with curing agent to prepare 4-hydroxythiobenzamide (III) and reacting with 2-chloro-3 ethyl acetoacetate to prepare 2-(4-hydroxyphenyl)-4-methyl-thiazole-5-carboxylicacid ethyl ester (IV); reacting with hexamethylenetetramine to prepare 2-(4-hydroxyphenyl)-4-methyl-thiazole-5-carboxylicacid ethyl ester derivative of formula (V); and carrying out reduction reaction.
NOVELTY - Manufacture of xylan-containing composition involves heat-treating herbal biomass in an H-factor of 3-3000 using 8-70 parts mass alkali and 10-10000 parts mass water with respect to 100 parts mass solid content of the herbal biomass, obtaining alkali primary-treated biomass, soaking resultant product in aqueous solution comprising 5 %mass or more alkali hydroxide and 60 %mass or less alkali metal hydroxide or alkaline-earth metal hydroxide at 0-50 degrees C, obtaining alkali secondary-treated biomass and extracting water-soluble components of resultant product.    USE - Manufacture of xylan-containing composition used as raw material for foodstuff and cosmetics.    ADVANTAGE - The method enables manufacture of xylan-containing composition with high recovery rate and excellent productivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of glucan-containing composition, which involves separating water-insoluble component form alkali secondary-treatment biomass; and    (2) manufacture of glucose, which involves carrying out saccharification process of the glucan-containing composition using enzyme.
NOVELTY - Hydroquinone (II) and concentrated sulfuric acid are added to three-necked flask, heated, hydroquinone is dripped, stirred, distilled water and activated carbon are added, and filtered, to obtain solution of 2,5-dihydroxybenzene-1-sulfonic acid (III). Obtained filtrate is added to three-necked flask, cooled, diethylamine (IV) is dripped, reacted, crystallized, filtered, washed, and dried, to obtain crude etamsylate. Crude etamsylate is dissolved in anhydrous ethanol, activated carbon is added, decolorized, filtered, precipitated, filtered, and dried, to obtain etamsylate (I).    USE - Preparation of etamsylate (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly preparation of etamsylate with high quality without using organic solvent and within short period of time.    DETAILED DESCRIPTION - Hydroquinone of formula (II) and concentrated sulfuric acid are added to a three-necked flask, heated in water bath, hydroquinone is dripped until the mixture completely melts, stirred, heat-preserved for 1 hour, the temperature decreased to 35-45 degrees C, distilled water and activated carbon are added, temperature is increased to 55-65 degrees C, stirred for 30 minutes, and filtered, to obtain solution of 2,5-dihydroxybenzene-1-sulfonic acid of formula (III). The obtained filtrate is added to three-necked flask, cooled to 25-35 degrees C, diethylamine of formula (IV) is dripped, reacted, cooled, crystallized, filtered, washed, and dried, to obtain crude etamsylate. Crude etamsylate is dissolved in anhydrous ethanol, small amount of activated carbon is added, decolorized, filtered, ice-cooled, precipitated, filtered, and dried at 50 degrees C, to obtain etamsylate of formula (I).
NOVELTY - The production method of nitrophosphate fertilizer involves decomposing phosphate rock with nitric acid, filtering resulting solution using filter aid, stirring to remove acid insoluble components and organic floats, and purifying filtrate acid hydrolyzate solution; then adding sulfuric acid or ammonium sulfate to mother liquor to form calcium sulfate dihydrate crystals; classifying the reaction slurry using grading equipment according to the size of the particles of calcium sulfate crystals; and filtering calcium sulfate.    USE - Method is useful for production of nitrophosphate fertilizer (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly production of nitrophosphate fertilizer.    DETAILED DESCRIPTION - The production method of nitrophosphate fertilizer involves decomposing phosphate rock with nitric acid, filtering resulting solution using filter aid, stirring to remove acid insoluble components and organic floats, and purifying filtrate of acid hydrolyzate solution, and removing suspended solids of more than 99% to obtain purified acid hydrolyzate with solids content of 50 mg/l or less; then adding sulfuric acid or ammonium sulfate to mother liquor so that calcium ions in the mother liquor and sulfate ions react to form calcium sulfate dihydrate crystals at 90 degrees C for 3-6 hours, and stirring at 200-400 rpm; classifying the reaction slurry using grading equipment according to the size of the particles of calcium sulfate crystals; and filtering calcium sulfate, filtering reaction slurry with large particles of calcium sulfate, discharging calcium sulfate and washing slurry.
NOVELTY - Fermented organic fertilizer comprises 2-6 pts. wt. liquid enzyme concentrate, 45-56 pts. wt. wheat bran, 16-19 pts. wt. vermicompost, 8-13 pts. wt. bean cake, 25-30 pts. wt. chicken manure, 15-35 pts. wt. rice bran, 3-9 pts. wt. jasmine flowers, 5-14 pts. wt. Cudrania, 40-45 pts. wt. bean straw, 9-12 pts. wt. Gardenia sawdust, 15-20 pts. wt. potato stalks, 0.01-0.03 pt. wt. lactic acid powder, 0.01-0.04 pt. wt. nitrifying bacteria powder, and 20-30 pts. wt. charcoal ash.    USE - The fermented organic fertilizer is useful for promoting flowering and fruiting in plants.    ADVANTAGE - The fermented organic fertilizer is rich in active proteins, growth hormones, antibiotics, deworming factors and other substances including iron, calcium and trace elements, makes roots and stems stronger, enhances color, increases yield, improve quality and other complex functions, strengthens immunity and controlling ability of plants against several pests and diseases, and effectively degrades harmful heavy metals in soil that cause injury to the plants.
NOVELTY - A shepherd's purse fertilizer comprises 20-22 pts. wt. pea green manure, 13-15 pts. wt. tea seed cake fertilizer, 14-16 pts. wt. ammonium sulfate, 12-14 pts. wt. ore powder, 9-11 pts. wt. calcium nitrate, 7-9 pts. wt. potassium magnesium chloride fertilizer, 6-8 pts. wt. boron fertilizer, 3-5 pts. wt. ammonium molybdate, 2-4 pts. wt. Cycocel (RTM: plant growth regulator), 1-3 pts. wt. sodium nitrophenolate, 2-4 pts. wt. ectomycorrhizal fungi, and 50-70 pts. wt. water.    USE - Shepherd's purse fertilizer used in enhancing stress resistance.    ADVANTAGE - The fertilizer can increase yield of shepherd's purse and can provide deep green colored shepherd's purse leaves with smooth surface.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, comprising mixing raw materials, stirring for 20 minutes, then standing for 1.5 days, and drying.
NOVELTY - Carbon-based compound fertilizer comprises urea-formaldehyde 10-20%, dispersant 15-25% and phosphate fertilizer or potassium fertilizer 50-70%. Dispersant is obtained from livestock and poultry fermented manure powder, biomass feedstock powder and biological toner mixture. Phosphate fertilizer or potassium fertilizer is obtained from urea 3-5% and wood vinegar 0.5-1.5%, calcium phosphate, magnesium phosphate, phosphate, phosphoric acid, amine or diamine, and potash is obtained from potassium sulfate or potassium chloride.    USE - Carbon-based compound fertilizer.    ADVANTAGE - The carbon-based compound fertilizer is cost-effective, reduces preparing steps and amount of urea, enriched in nitrogen-phosphorus-potash fertilizer, and has wide industrial applicability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing carbon-based compound fertilizer, which involves:    (A) adding urea containing 46% nitrogen and 37% of multi-concentrated formaldehyde solution in a reaction kettle;    (B) heating and stirring urea and formaldehyde at less than or equal to 60 degrees C and adding potassium hydroxide through addition reaction to regulate pH value at alkaline range not less than 8 to obtain N,N'-bis(hydroxymethyl)urea;    (C) cooling N,N'-bis(hydroxymethyl)urea to 40 degrees C, injecting boric acid powder to regulate pH value in acidic range; and    (D) performing condensation reaction to obtain water containing 30-35% of urea-formaldehyde, and then mixing remaining components to obtain final product.
NOVELTY - This new utility model relates to one of using coke furnace coal and blast furnace coal unite production natural gas and liquid ammonia and device. The device comprises natural gas/liquefied natural gas production device, blast furnace coal purification device and anhydrous liquid ammonia production device, natural gas/liquefied natural gas production device comprises screw compressor or a Roots blower, a variable temperature adsorption system, the first reciprocating compressor, the first pressure swing adsorption decarburization system, coke oven gas device, methane synthesis system and pressure swing adsorption system or cryogenic separation system, blast furnace coal purification device comprises the second reciprocating compressor, sulphur tolerant conversion device, blast furnace gas desulphurization device, the second pressure swing adsorption decarburization system and pressure swing adsorption remove nitrogen system, anhydrous liquid ammonia production device comprises methanation system and synthesis ammonia system, after pressure swing adsorption system or cryogenic separation system through pipeline and pressure swing adsorption remove nitrogen system connected with, again connected to methanation system. The device not only solves of blast furnace coal use is, then can produce out high value products.
NOVELTY - The processing firewood has firewood connection portion that is connected with multiple firewood portions and are arranged in firewood form of the component. The firewood connection portion is provided with cut-away portion that is arranged for moving the firewood portion to up and down at optimal interval. The firewood portion is provided with the pillar type whose thickness is reduced. The cut-away portion is formed with circular form, the ellipse or the polygon.    USE - Vertical injection combustion processing firewood.    ADVANTAGE - The combustion output and the uniform stable continuous combustion can be made, after the combustion of the firewood connection portion and the various types of the wooden charcoal material are provided within the combustion chamber. The conversion process of the timber and charcoal material can be rapidly progressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of vertical injection combustion Processing firewood.    Thickness of firewood portion (10)    Firewood portion interval (20)    Firewood cross-sectional diameter (30)    Firewood piece connection portion diameter (40)
NOVELTY - The fermenter (1) has a stirring rotation unit (40) that stirs the raw material. An outlet (110b) exhausts the air inhaled to an inlet (110a) in which a blower (110) is inserted to a fermenter (10). The inlet (110a) is connected to the entrance of a recycle pipe (200) which is arranged parallel to the fermenter. An inlet (120a) which inhales the air of a blower (120) connected to a pipe exit (200b) is combined in the upper portion of a hollow shaft (20). An outlet (120b) is provided to exhaust the air inhaled in the inlet (120a).    USE - Live-stock manure fermenter.    ADVANTAGE - Since the aerobic fermentation action occurs due to the aerial pressurizing with the rotation of the agitating blade, the fermentation heat is produced easily. Hence the need for separate heater is prevented, and manufacturing cost of the fermenter is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the live-stock manure fermenter.    Live-stock manure fermenter (1)    Fermenter (10)    Hollow shaft (20)    Stirring rotation unit (40)    Blowers (110,120)    Inlets (110a,120a)    Outlets (110b,120b)    Recycle pipe (200)    Pipe exits (200b)
NOVELTY - Preparation of compost comprises mixing mushroom waste and kitchen waste and aerobically fermenting the obtained mixture.    USE - Method for preparing compost (claimed).    ADVANTAGE - The method reduces gas pollution, resolves China mushroom waste processing of about 900 million tons, has low cost and simple operation, and relieves agricultural waste treatment.
NOVELTY - Apixaban precursor compound (I) is prepared by taking sulfur-containing apixaban precursor compound (V), and performing cyclization reaction with sodium ethoxide in organic solvent at 35 degrees C for 2-3 hours.    USE - Method for preparing apixaban precursor compound (I) (claimed).    ADVANTAGE - The method has yield of 87%. It avoids using expensive catalysts and environment-polluting reagents.    DETAILED DESCRIPTION - Apixaban precursor compound of formula (I) is prepared by taking sulfur-containing apixaban precursor compound of formula (V), and performing cyclization reaction with sodium ethoxide in organic solvent at 35 degrees C for 2-3 hours.    INDEPENDENT CLAIMS are included for:    (1) preparation of compound (V) which comprises reacting 4-(2-hydroxy-ethyl)-1-(4-methoxy-phenyl)-5-(4-nitro-phenylcarbamoyl)-1H-pyrazole-3-carboxylic acid ethyl ester of formula (IV) with methanesulfonyl chloride and diisopropylethylamine in organic solvent at 0-5 degrees C for 2-3 hours;    (2) preparation of compound (IV) which comprises reacting 4,5-dihydro-furan-2-carboxylic acid (4-nitro-phenyl)-amide of formula (II) with ((4-methoxyphenyl)hydrazino)chloroethyl acetate in solvent in the presence of triethylamine and reacting the obtained ((4-methoxy-phenyl)-hydrazono)-(2-(4-nitro-phenylcarbamoyl)-4,5-dihydro-furan-3-yl)-acetic acid ethyl ester of formula (III) with hydrochloric acid at 40-60 degrees C;    (3) preparation of compound (II) which comprises reacting p-nitroanline with triphosgene in the presence of triethylamine and reacting the obtained 4-nitrophenylisocyanate with 2,3-dihydrofuran in the presence of tert-butyl lithium at -78 degrees C.
NOVELTY - The apparatus has a mixing drum (30) whose one end is provided with shaft rod (31) while other end is provided with vent (32) for circulating gas in the inner side. A mount portion is arranged below the mixing drum. A heater (60) is installed on conveyance tube furnace (50) and blower which blows the hot air to specific direction. An inlet port (40) is provided on side circumference portion to perform opening and closing operation so as to deliver the power from drive motor which rotates the mixing drum.    USE - Waste drying fermentation apparatus for fermenting organic waste such as carcass of excrements, fish residue, sewage sludge, food waste.    ADVANTAGE - The carcass of the excrements, fish residue, sewage sludge, and food waste are fermented easily by regularly maintaining the temperature of the mixing drum to collect the hot air in the gas component. The environment-friendly of the fermentation apparatus is ensured. The cost of the apparatus is reduced. The generation of odor during fermentation process is reduced by circulating the air of the mixing drum to the inside. The power consumption of the apparatus is reduced. The fermentation efficiency of the waste product is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the waste drying fermentation apparatus.    Mixing drum (30)    Shaft rod (31)    Vent (32)    Inlet port (40)    Conveyance tube furnace (50)    Heater (60)
NOVELTY - Producing biogas by anaerobic fermentation of lignocellulosic feedstock, by (a) crushing the lignocellulosic feedstock, adding the crushed product into continuous stirred tank reactor after addition of inoculum, adjusting using water or biogas slurry, and performing anaerobic fermentation at 34-37 degrees C for 15-20 days, and (b) dehydrating discharged biogas until moisture content reaches 75-85%, transferring to semi-continuous solid substrate anaerobic reactor, and fermenting at 34-37 degrees C for 30-35 days, where the fermented product has TS concentration of 15-25%.    USE - The method is used for producing biogas by anaerobic fermentation of lignocellulosic feedstock (claimed).    ADVANTAGE - The method increases anaerobic reactor processing ability and yield, and is suitable for mass production.    DETAILED DESCRIPTION - Method for producing biogas by anaerobic fermentation of lignocellulosic feedstock, involves (a) crushing the lignocellulosic feedstock to size of 5 cm or less, adding the crushed product into continuous stirred tank reactor after addition of inoculum, adjusting using water or biogas slurry, and performing anaerobic fermentation at 34-37 degrees C for 15-20 days, and (b) dehydrating discharged biogas until moisture content reaches 75-85%, transferring to semi-continuous solid substrate anaerobic reactor, and fermenting at 34-37 degrees C for 30-35 days, where the fermented product has TS concentration of 15-25%.
NOVELTY - Fertilizer comprises 30-40 pts. wt. fermented cow dung, 10-12 pts. wt. vermiculite, 15-17 pts. wt. peat soil, 8-10 pts. wt. pine needles, 10-12 pts. wt. moss, 18-20 pts. wt. calcium superphosphate, 2-4 pts. wt. biological enzyme, 0.4-0.6 pt. wt. iron, 0.2-0.4 pt. wt. zinc, 0.1-0.3 pt. wt. copper, 0.6-0.8 pt. wt. magnesium and 0.5-0.7 pt. wt. manganese.    USE - As fertilizer for blueberry (claimed).    ADVANTAGE - The fertilizer improves quality of blueberry.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing the fertilizer, which involves adding the above-mentioned materials into kneading machine, preheating at 100-120 degrees C, mixing the preheated product using mixer, adding starch, melting, maintaining at die pressure of 1.4-1.6 MPa, and spray-drying obtained product.
NOVELTY - Invention relates to the hydrolysis industry, particularly methods of removing acetone-butyl-alcohol fermentation inhibitors from hydrolysates of lignocellulose material, and can be used in preparing culture media for producing biethanol, biobutanol and acetone. The method includes treating hydrolysates with a group of microorganisms, wherein the consortium of microorganisms used is active sludge from sewage treatment facilities which is pre-adapted to a growth substrate based on substances which inhibit acetone-butyl-alcohol fermentation. The method employs active sludge from urban sewage treatment facilities, the bacterial component of which is represented by Pseudomonas (64%), Bacillus (18%), Zooglea (7%), Micrococcus (5%), Chromobacterium (3%), Acinetobacter (2%) and Citrobacter (1%) bacteria. The method also employs active sludge from sewage treatment facilities of pig-breeding farms, the bacterial component of which is represented by Nocardia (35%), Rhodococcus (28%), Micrococcus (18%), Pseudomonas (13%) and Bacillus (6%) bacteria.    USE - Chemistry.    ADVANTAGE - Invention eliminates inhibiting factors in the process of fermentation of hydrolysates of lignocellulose material, enables to avoid corrosion of the hydrolysis equipment and enables to optimise the microbial culture.3 cl, 4 ex
NOVELTY - Method of extraction of lipids from the biomass is proposed. The method comprises destruction of the cell membranes of microalgae Chlorella in a vortex electromagnetic field with ferromagnetic particles followed by extraction of the lipid fraction. Extraction of the lipid fraction is carried out in a multistage extraction device with swirl flow of inert bodies, using an organic solvent.    USE - Biotechnology.    ADVANTAGE - Invention enables to reduce the extraction time and to increase the output of the lipid fraction from the microalgae biomass.2 tbl
NOVELTY - Recovery of vegetable oil from waste clay involves extracting vegetable oil in waste clay by desorption, separating extraction solvent and oil by fractionation, recovering solvent and oil, adding ethanol and sulfuric acid to oil, carrying out esterification to reduce free fatty acid content to 2%, adding ethanol and alkaline catalyst to oil after esterification process, performing transesterification at 60-80 degrees C for 30 minutes to convert oil into ethyl ester and glycerol, separating ethyl ester and glycerol, neutralizing, washing, carrying out oil-water separation and distilling.    USE - Method for recovering vegetable oil from waste clay (claimed).    ADVANTAGE - The method is low-cost and has high yield and conversion rate of higher than 84%.    DETAILED DESCRIPTION - Recovery of vegetable oil from waste clay comprises extracting vegetable oil in waste clay by desorption where waste clay oil rate is less than 2%, separating extraction solvent and oil by fractionation, recovering solvent and oil, adding ethanol and sulfuric acid to oil where molar ratio of ethanol to oil is 8-9 and weight ratio of sulfuric acid to oil is 0.01-0.02, carrying out esterification to reduce free fatty acid content to 2%, adding ethanol and alkaline catalyst to oil after esterification process where molar ratio of ethanol to oil is 12 and weight ratio of alkaline catalyst to oil is 0.01-0.02, performing transesterification at 60-80 degrees C for 30 minutes to convert oil into ethyl ester and glycerol, separating ethyl ester and glycerol, neutralizing, washing, carrying out oil-water separation and distilling at 105-120 degrees C to remove residual alkaline catalyst, ethanol and water where weight ratio of acetic acid and oil is 0.015-0.03 and molar ratio of water and oil is 3-9.
(TW498622-U)   NOVELTY - A hydrogen rich water generator includes a container, a hydrogen input, a dividing tube, a vibrator, and a passing structure. The container is used for containing water. The hydrogen input interconnects the inside and the outside of the container. The dividing tube is configured in the container and connected to the hydrogen input. The vibrator is used for vibrate the water. The passing structure is configured on the container and used for adding water or taking hydrogen rich water out. The hydrogen input receives hydrogen from a hydrogen source and guides the hydrogen into the dividing tube, having a plurality of nano-holes on the tube wall, and the hydrogen passes through the nano-holes into the water to become hydrogen micro bubbles in the container. The vibrator assists the hydrogen micro bubbles mixed with the water well to generate hydrogen rich water and humidified hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic perspective view of the gas generator.    Gas generator (1)    Humidification device (9)    Hollow body (90)    Second pipe (92)    Outputting pipe (94)    Oscillation device (95)
NOVELTY - Provided is a system structure of powdery solid catalyst transesterification equipment for biodiesel, in which the powdery solid catalyst is added to mix and circulate with transesterification oil and methanol to bring about a catalytic reaction by means of microwave heating mechanism, and quickly achieve a transesterification purpose. After a transesterification reaction, the heating temperature is directly increased to make methanol distilled and separated, and condensed and recycled through a heat exchanger. After removing the methanol, the reactant is directly moved out of the reaction system and will be separated through a setting precipitation so that the upper layer is biodiesel, the lower layer is glycerol and the sediment is powdery solid catalyst, which can be directly separated for use without using such procedure to wash for releasing the catalyst. It can increase the reaction efficiency of solid catalytic transesterification, reduce the manufacturing cost and build environmental-protected production techniques in line with the power-saving and low carbon emission.
NOVELTY - The method involves separating a first gas mixture (11) into a first permeate (13) and a first non-permeate (15) by using a first gas separation membrane (9). A second gas mixture (21) is separated into a second permeate (19) and a second non-permeate (5) by a second gas separation membrane (7). The second permeate is divided into first and second portions (17, 27). The first permeate is compressed with the second portion by a compressor to produce the second gas mixture. The second non-permeate and source gas e.g. natural gas, are combined to produce the first gas mixture.    USE - Method for recovering first gas e.g. methane and Helium, from source gas e.g. natural gas (all claimed), from natural or industrial sources.    ADVANTAGE - The method enables using particular gas membrane separation scheme to allow first product gas to be obtained at relatively high recovery and purity and second product gas to be obtained at satisfactory recovery.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for separating Helium from natural gas using three gas separation membrane stages.    Non-permeates (5, 15)    Gas separation membranes (7, 9)    Gas mixtures (11, 21)    Permeates (13, 19)    Portions (17, 27)
NOVELTY - Producing biodiesel and alcohol involves performing transesterification of Cyperus esculentus through acidic route and enzymatic route.    USE - Method for producing biodiesel and alcohol for use in alcoholic beverages and non-alcoholic beverages (all claimed).    ADVANTAGE - The method enables to produce biodiesel and alcohol simultaneously in a cost-effective manner.
NOVELTY - A simple electrolytic-type hydrogenous water-generation device comprises electrolytic-type hydrogenous water-generation portion which converts raw water into hydrogenous water, fuselage portion which stores hydrogenous water, and cap portion which seals hydrogenous water. The hydrogenous water generator portion is arranged at bottom portion of fuselage portion in longitudinal direction. An electrolysis portion which set porous electrode plate of metal mesh on up-and-down both sides of insulating spacer is horizontally placed in bottom portion.    USE - Simple device is used for generating electrolytic-type hydrogenous water for preparing hot green tea, black tea and coffee.    ADVANTAGE - The simple device efficiently generates electrolytic-type hydrogen water economically by simple process. The products made using the water are consumable.    DETAILED DESCRIPTION - A simple electrolytic-type hydrogenous water-generation device comprises an electrolytic-type hydrogenous water-generation portion which converts raw water into hydrogenous water, a fuselage portion which stores the hydrogenous water, and a cap portion which seals the hydrogenous water. The hydrogenous water generator portion is arranged at the bottom portion of fuselage portion in longitudinal direction. An electrolysis portion which set the porous plate of metal mesh on up-and-down both sides of insulating spacer is horizontally placed in bottom portion. Even 100 degrees C boiling water electrogenerates hydrogenous water because common allowable temperature limit uses resin material and material (a) with heat resistance of 100 degrees C or more. The material (a) is chosen from glass, ceramic, metal, polycyclohexylene dimethylene terephthalate, polycarbonate, melamine resin, polypropylene, polyimide resin, phenol resin, silicone resin and epoxy resin.
NOVELTY - The utility model is new type biomass particle fuel production process device technology field, it claims a novel plant biomass particle fuel forming device, a feeding device, an extruding device and receiving device, the feeding device comprises raw material converying belt, the extrusion device comprises conveying belt, extrusion forming mould and roller shaft, the extrusion forming mould is located on the conveying belt, the raw material converying belt end is located above a conveying belt of the front end of the roller shaft distance of the conveying belt and the extrusion forming mould is equal to height, end of a conveying belt provided with a material receiving device. The utility model is new type structure is simple, the automatic degree high, the energy consumption is low, using suitable, forming, forming high rate.
NOVELTY - Processing electrocell dyeing waste water involves removing ions using electrochemical and chemical process using cathode and anode in presence of direct current electric field. The waste water is hydrolysed to discharge oxygen at anode. The hydrogen iron is generated at cathode having strong reducing capacity for removing hexavalent chromium in water. Iron ion and metal ions are removed by sedimentation process. The obtained solution is filtered using ultra-filter to remove micro-organism and algae. The obtained liquid is finally treated with sodium bisulfite as oxidizing agent.    USE - Method for processing electrocell dyeing waste water (claimed).    ADVANTAGE - The method enables to process electrocell dyeing waste water that removes dissolved salts, colloids, micro-organism and organic matter in waste water.
NOVELTY - Production of high density coal comprises entering biomass raw material into low-temperature charring furnace, precarbonizing, removing oxygen and water; crushing to obtain coal powders, adding adhesive, stirring, extruding, pressing into coal block; and entering into high temperature kiln carbonizing furnace and baking.    USE - Method for producing high density coal (claimed).    ADVANTAGE - The method increases coal quality and density.
NOVELTY - A low-temperature methanation catalyst comprises organic polymer material as carrier, and Raney alloy particles supported on carrier surface of organic polymer material. The Raney alloy comprises nickel, iron, chromium, lanthanum and aluminum.    USE - Low-temperature methanation catalyst is used for cryogenic hydrogen removal of trace carbon monoxide during methanation reaction (claimed).    ADVANTAGE - The low-temperature methanation catalyst has excellent activity at low temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catalyst.
NOVELTY - Method (M1) for producing substantially racemic lactic acid, or its derivative, involves (a) fermenting a slurry of biomass material comprising solids in a membrane bioreactor using at least one microbial strain that converts carbohydrates into substantially racemic lactic acid, and (b) recovering the substantially racemic lactic acid, or its derivative, from or downstream from the membrane.    USE - The methods are useful for producing substantially racemic lactic acid, or its derivative, PLA and/or PDA, PDLLA, and product comprising PDA, PLA or PDLLA. The substantially racemic lactic acid is in the form of a mixture with at least one other carboxylic acid (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) for producing poly-L-lactic acid (PLA) and/or poly-D-lactic acid (PDA), involves obtaining L-lactic acid and/or D-lactic acid by the above-mentioned method (M1), and polymerizing the L-lactic acid and/or D-lactic acid to obtain PLA and/or PDA;    (2) method (M3) for producing poly(D,L)lactide (PDLLA), involves (a) obtaining PLA and PDA by the method (M1), and mixing the PLA and PDA to obtain PDDLA, or (b) obtaining PLA or PDA by the method (M1), and mixing the PLA or PDA with PDA or PLA respectively to obtain PDDLA; and    (3) product comprising PDA, PLA or PDLLA obtained by above-mentioned method (M2) or (M3).
NOVELTY - The utility model is new type relates to a plant for processing sewage of sequencing batch reactor, comprising a reaction pool, b. water inlet pipe mounted on the reaction pool, a to the air inlet tube in the reaction pool from sewage water, some aerators are a plurality of gas distribution pipe b. air inlet pipe on a, b. distributing tube mounted on the, the sequencing batch reactor also comprises mounting b.... a separating plate, a reaction pool for dividing into water inlet area and reaction area, an aerobic Anaerobic facultative microorganism can carry out biochemical reaction in a one of a reaction pool, which saves the occupied square meter of reaction pool, strengthening the effect of biochemical processing sewage, using suitable operation, b.
NOVELTY - The utility model is new type relates to a plant used for sewage treatment is from a microorganism carrier, comprising a open mouth of a web or net, it can cover with a network or a network box cover, in a network of a carrier material layer can adhere the microorganism, a a a a a a a a a a a a a a a a under layer, a filter material layer is a specific gravity larger than a a a a a specific gravity, a filter carrier material under a height less than the height of screen 1/2, the microorganism is a density less than a density sewage. The utility model is new type solves the problem that the existing technology in a mounted complex microorganism, microorganism and a carrier material affinity is small, a problem is easy to fall off.
NOVELTY - The utility model is new type relates to a plant used for sewage treatment of microorganism contact carrier device, comprising a net two end opening, upper end cover, lower end cover and microorganism contact, the upper end cover is covered at upper end of a network, under a cover covering a lower end of a network, the microorganism contact piece is located at the cylinder lumen and fixed at upper end cover and lower end cover on. The new type utility especially claims a a U type of microorganism contact, when using a to b contact a microorganism, a microorganism in a device fixed in contact with bottom net and a fixed net frame, a fixing frame mounted to a use in a reaction groove. When need a change, it only needs to detachably fix the frame take out microorganism contact net carrier device. Dismounting is simple suitable mounting.
NOVELTY - The new type utility claims one below a suction FORMULA household biomass gasification furnace device, wherein is equipped with intermittent add material on a feeding port at the top of the furnace part, through a rotating assembly is can rotate intermittently a quantitative hearth in addition to biomass raw material, the biomass raw material lasting reaction in a hearth, an air outlet pipe of the furnace body bottom when in a retarding sum conveying pipe through a second filter, can effective reduce impurity of soot and tar gasification and impurity of sum, sum a. furnace reducing coal, and emission reduction. The gasification furnace device has simple structure, reasonable design, strong adaptability, can use a more biomass raw material, and using suitable, with high economic benefit and social benefit, fit in vast rural area to popularize application.
NOVELTY - The new type utility claims a transgenic rice plant seed and rapid detecting method of the parent a dedicated device, a PC machine, Raman detect device and radiation source, the PC machine through USB bus and Raman detect device connected, the radiation source is all-solid-state semiconductor laser, provide radiation for Raman detect device. The utility model is new type..., structure is simple, design, a process is simple, the detecting efficiency is high, it will not cause environmental pollute, which greatly reduce the detection cost. Establish the fast detecting a recognition precision of transgenic rice seed and its parent 86%, a high precision, so it comprises good application prospect and a considerable market value.
NOVELTY - The apparatus (10) has a vessel (12) whose wall portions are set with interior surfaces (22) to define a first pathway. A second pathway is formed between heat exchange medium inlet and heat exchange medium outlet. The interior wall portions of vessel are projected into an interior space of the vessel such that the first and second pathways is set to be non-linear and a heat transfer surface area is increased compared to linear first and second pathways. An agitator (50) is set to pass the carbonaceous material, produced char and volatiles through the first pathway.    USE - Apparatus for pyrolysing carbonaceous material such as biomass and coal, and producing char and volatiles. Uses include but are not limited to anthracite, semi-anthracite, bituminous coal, sub-bituminous coal, brown coal, lignite and peat, biomass, waste rubber such as vehicle tire, waste plastic material, agricultural waste and mixtures of carbonaceous materials with other substances.    ADVANTAGE - The yield of the volatile matter is increased. The heat transfer coefficient and the heat transfer rate of the heat exchange medium to the carbonaceous material are enhanced. The contact of volatiles with the oxygen containing gas is eliminated and the consumption of the oxygen-containing gas is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a gasification system for producing product gas from carbonaceous material.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the apparatus for pyrolysing carbonaceous material.    Apparatus for pyrolysing carbonaceous material and producing char and volatiles (10)    Vessel (12)    Interior surface (22)    Projecting surface (30)    Agitator (50)
NOVELTY - Extraction and purification of taurine comprises removing ammonia by cation exchange membrane with hydrogen ions and sodium ions to obtain taurate aqueous solution and sulfur dioxide, taking taurate aqueous solution, cooling, crystallizing, concentrating, taking aqueous solution of sodium bisulfite as raw material and reacting with ethylene oxide to prepare sodium isethionate.    USE - Method for extracting and purifying taurine (claimed).    ADVANTAGE - The method is simple, energy-saving, low-cost, safe and environment-friendly and has high yield.
NOVELTY - Odorless organic fertilizer comprises 20-25 pts. wt. wheat straw, 20-25 pts. wt. corn stalk, 15-16 pts. wt. bean stalk, 12-14 pts. wt. rapeseed straw, 3-5 pts. wt. soybean powder, 1-2 pts. wt. cottonseed powder, 2-4 pts. wt. lees, 1-2 pts. wt. vinegar, 3-5 pts. wt. cassava residue, 1-2 pts. wt. sugar residue, 8-10 pts. wt. dairy cow manure, 8-10 pts. wt. sheep manure, 8-10 pts. wt. horse dung, 30-35 pts. wt. black carbon powder and 30-35 pts. wt. phosphate rock powder.    USE - Odorless organic fertilizer used for reducing pests and diseases (claimed).    ADVANTAGE - The fertilizer has high nutrient content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of odorless organic fertilizer comprising taking wheat straw, corn stalk, bean stalk, rapeseed straw, soybean powder and cottonseed powder, washing, drying, sterilizing at 80-95 degrees c for 20-30 minutes and deodorizing for 10 minutes to obtain component A; taking lees, vinegar, cassava residue, sugar residue and water, primary fermenting at 60-65 degrees C for 10 days, mixing, secondary fermenting at 60 degrees C for 10 days, mixing at 30 degrees C until moisture content is 30% and ripening for 3-5 days to obtain component B; taking dairy cow manure, sheep manure and horse manure, sun drying for 4 hours, sterilizing for 1 hour and deodorizing for 20 minutes to obtain component C; and mixing components A-C, adding other remaining raw materials, stirring, granulating into 8-12 mm at 60-70 degrees C for 30 minutes, drying, sieving at 12 mm and bagging.
NOVELTY - Preparation of biological organic fertilizer involves taking sugarcane leaves, soaking in 3% calcium hydroxide solution, fermenting for 15-20 days to obtain prepared sugarcane leaves, taking animal manure, drying at below 20% moisture content, crushing to 30-40 mesh to obtain prepared animal manure, mixing 550 kg prepared sugarcane leaves, 250 kg prepared animal manure, 200 kg bagasse, 2 kg biological strain and 1000-1200 kg water, adjusting water content at 55-65%, performing anaerobic fermentation at 60 degrees C for 3-4 days, drying at 50-60 degrees C until moisture content is below 10% and packaging.    USE - Method for preparing biological organic fertilizer (claimed).    ADVANTAGE - The method is environment-friendly, and has inexpensive and wide source of raw materials.    DETAILED DESCRIPTION - Preparation of biological organic fertilizer comprises taking sugarcane leaves, drying at below 20% moisture content, soaking in 3% calcium hydroxide solution, fermenting for 15-20 days to obtain prepared sugarcane leaves, taking animal manure, drying at below 20% moisture content, crushing to 30-40 mesh to obtain prepared animal manure, mixing 550 kg prepared sugarcane leaves, 250 kg prepared animal manure, 200 kg bagasse, 2 kg biological strain and 1000-1200 kg water, adjusting water content at 55-65%, stacking at 2-2.5 m wide and 1-1.2 m high, covering with plastic film, performing anaerobic fermentation at 60 degrees C for 3-4 days, covering with plastic cloth, fermenting continuously for 5-6 days, drying at 50-60 degrees C until moisture content is below 10% and packaging.
NOVELTY - Preparation of biogas residue fertilizer comprises taking fresh biogas residue, dewatering at 60-70% moisture content, adjusting carbon and nitrogen content at mass ratio of 25-30:1, adjusting pH value to neutral or basic, crushing, adjusting moisture content to 60-70%, stacking, fermenting at 60 degrees c for 15-20 days and turning every 2-3 days, adjusting organic matter content at greater than or equal to 35%, total nutrient content at greater than or equal to 6.0%, nitrogen content at greater than or equal to 3.0%, viable cells at greater than or equal to 6x 109/g, fecal coliform at less than or equal to 100/g and pH value at 5.5-8.0, granulating at 3-5 mm particle diameter and bagging at 25 kg/bag.    USE - Method for preparing biogas residue fertilizer (claimed).    ADVANTAGE - The fertilizer has nutrient content in accordance with NY525-2002 and NY884-2004 standards. The method is environment-friendly.
NOVELTY - Biological organic fertilizer comprises 70 wt.% waste material, 20 wt.% chicken manure, 5 wt.% phosphate fertilizer and 5 wt.% potash fertilizer. The waste material is prepared by mixing 75 pts. wt. sugarcane leaves, 22 pts. wt. filter mud, 0.5 pt. wt. calcium superphosphate, 1 pt. wt. peanut cake and 1 pt. wt. gypsum, stacking, primary fermenting twice, turning down, secondary fermenting at 58-60 degrees C, cooling to 42-52 degrees C, insulating for 6 days, cooling below 30 degrees C, feeding into edible mushroom cultivation house, harvesting edible mushroom and collecting waste material.    USE - Biological organic fertilizer used for promoting growth in fruits and vegetables (claimed).    ADVANTAGE - The fertilizer has increased organic matter content by 30%, shortens cultivation time and costs, does not contain harmful substances and improves quality and yield of fruits and vegetables.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of biological organic fertilizer comprising mixing waste material, chicken manure, phosphate fertilizer and potash fertilizer, fermenting and adjusting moisture content to 35%.
NOVELTY - Domestic fuel comprises 40-100 wt.% 5C hydrocarbon, 0.1-40 wt.% additional hydrocarbon and 0.1-40 wt.% ethanol.    USE - Domestic fuel.    ADVANTAGE - The domestic fuel is inexpensive, non-toxic and convenient to use, and saves resource.
NOVELTY - Preparation of methane-rich liquefied natural gas involves performing cryogenic liquefaction of methane-rich gas, and performing distillation in single distillation column to isolate 500 ppm hydrogen, less than 2% nitrogen and less than 2% carbon monoxide.    USE - Method for preparing methane-rich liquefied natural gas (claimed).    ADVANTAGE - The method is inexpensive and simple.
NOVELTY - Domestic garbage recycling process comprises separating garbage in container of water, extruding, heating to 250 degrees C to obtain dry solid and galvanizing to obtain solid fuel.    USE - Method for recycling domestic garbage (claimed).    ADVANTAGE - The method has simple technique, low investment, and convenient to perform.
NOVELTY - Coffee husk component-containing pellets comprise rice hulls and coffee shell powder.    USE - Coffee husk component-containing pellets (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of coffee husk component-containing pellets.
NOVELTY - The method involves cooling bio-gas in a first polymer separation membrane area. A second polymer separation membrane area is made to contact with a third polymer separation membrane area. Ratio of the first, second and third polymer separation membrane areas is 1:1:1-1:5:1. A first polymer separation membrane is connected to a second polymer separation membrane. Selectivity range of carbon dioxide about methane is 20-34. A remain part of the third polymer separation membrane is connected with a transmission part of the second polymer separation membrane to maintain pressure of the bio-gas.    USE - Method for separating methane gas from bio-gas generated in food waste and organic compound through a methane gas purifier (claimed).    ADVANTAGE - The method enables cooling and compressing the bio-gas in the first polymer separation membrane area, and connecting the polymer separation membrane to the other polymer separation membrane so as to effectively separate high-purity methane gas from the bio-gas, so that productivity and recovery rate about the high-purity methane gas can be improved, aspect ratio of the polymer separation membranes can be optimized and cost required for installing and driving a methane gas purifier can be reduced.    DETAILED DESCRIPTION - The polymer separation membranes are made of polysulfone, polycarbonate, PET, cellulose acetate, polyphenyleneoxide, polysiloxane, polyethylene oxide or polypropylene oxide material. An INDEPENDENT CLAIM is also included for a methane gas purifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a methane gas purifier.
NOVELTY - Mixed strain of Brevibacillus brevis, Micrococcus luteus, Staphylococcus epidermidis and Candida rugosa having accession number of KCTC 12601BP, is new.    USE - The mixed strain is useful for processing food waste (claimed).    ADVANTAGE - The mixed strain has excellent growing capacity in at least 2% salinity environment, pH of less than or equal to 5 and temperature of 40 degrees C, and high cellulose, amylose, protein and fat decomposing capacity.
NOVELTY - Production of product involves providing feed (f1) comprising biomass (110) into a reactor (130), providing feed (f2) comprising carbonaceous material into the reactor, providing feed (f3) comprising carbon dioxide into the reactor, and reacting feeds (f1)-(f3) in the reactor with reaction conditions required to gasify the biomass, dry reform the carbonaceous material with the carbon dioxide, and produce the product.    USE - Production of product e.g. surplus carbon dioxide used in shale fracturing, and synthesis gas (all claimed) for producing liquid fuel and chemical.    ADVANTAGE - The method enables economical, simple and stable production of product with reduced water footprint, by eliminating condensable hydrocarbon formation during biomass gasification, at low pressure. The product enables efficient production of liquid fuel and chemical with reduced carbon footprint.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) conversion system for producing synthesis gas; and    (2) reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of system for co-conversion of carbonaceous material, biomass and carbon dioxide.    Biomass (110)    Feed port (114)    Reactor (130)    Catalyst (137)    Fluidized bed (139)
NOVELTY - The device (1) has a hermetically sealed vertical container (3) filled with carbonaceous fuel (2). A partial oxidation chamber (7) performs oxidation of pyrolysis products delimited by a refractory casing (8) which is basically delimited in cone, cylindrical or pyramid-shaped structure. A reduction zone (10) chemically reduces oxidized product gas (11) released from the partial oxidation chamber, and is arranged under the casing. An outlet (13) of the product gas is formed beyond the reduction zone in direction of progression of the product gas out of the device.    USE - Device for multi-stage gasification of carbonaceous fuels i.e. biomass, for production of generator gas in cogeneration plants with low content of tar and impurities.    ADVANTAGE - The device is simple in structure, and has prolonged service life, high electricity production efficiency, high operating performance and low operating and maintenance costs, and improves conversion efficiency of the reduction zone. The device can force the product gas to leave a container of the device by passing through the reduction zone so as to reduce combustible and incombustible carbon dioxide (CO2), thus increasing heat potential of the product gas for a cogeneration unit.    DETAILED DESCRIPTION - The device is provided with an integral lining (14) that is a steel weldment unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a device for multi-stage gasification of carbonaceous fuels.    Device for multi-stage gasification of carbonaceous fuels (1)    Carbonaceous fuel (2)    Hermetically sealed vertical container (3)    Partial oxidation chamber (7)    Refractory casing (8)    Reduction zone (10)    Oxidized product gas (11)    Product gas outlet (13)    Integral lining (14)
NOVELTY - Fuel cell system (100) has desulfurizer (3) having catalyst container (32) which accommodates desulfurization catalyst (31) for removing sulfur compound in raw material, fuel cell (1) which generates electric power according to electrochemical reaction using supplied air and fuel obtained by reforming sulfur compound-removed raw material, heating unit (4) which heats desulfurizer using heat generated by exhaust gas circulated inside fuel cell system and uniform-heating unit (5) for transmitting heat of heating unit to desulfurizer.    USE - Fuel cell system (claimed).    ADVANTAGE - The fuel cell system suppresses temperature irregularity arisen in heated desulfurization catalyst by effective method.    DETAILED DESCRIPTION - Fuel cell system (100) has desulfurizer (3) having catalyst container (32) which accommodates desulfurization catalyst (31) for removing sulfur compound in raw material, fuel cell (1) which generates electric power according to electrochemical reaction using supplied air and fuel obtained by reforming sulfur compound-removed raw material, heating unit (4) which heats desulfurizer using heat generated by exhaust gas circulated inside fuel cell system and uniform-heating unit (5) for transmitting heat of heating unit to desulfurizer such that temperature difference in temperature distribution of heating unit is less.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system. (Drawing includes non-English language text)    Fuel cell (1)    Desulfurizer (3)    Heating unit (4)    Uniform-heating unit (5)    Desulfurization catalyst (31)    Catalyst container (32)    Fuel cell system (100)
NOVELTY - Producing a biofuel comprises: (a) feeding biomass to an anaerobic digester; (b) feeding digestate comprising at least one hydrolytic enzyme; (c) adding at least one polyamine; (d) allowing the resulting mass to react in anaerobic conditions; and (e) separating the obtained biofuel.    USE - The process is useful for producing a biofuel (claimed) such as biogas, biomethane, bioethanol or hydrogen.    ADVANTAGE - The process: utilizes the polyamine that is biodegradable, thus increasing the action of hydrolytic enzymes, facilitating and promoting the process of hydrolysis and saccharification, and especially increasing the final yields in biofuels by reduction of the output nondigested biomass; does not require dedicated facilities or equipment, nor particular modifications for the addition of the polyamine to pre-existing biofuel production plants; and does not cause the formation of substances considered detrimental to the environment, where the waste products coming from the anaerobic digester, do not show risk indicators for the health or the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a composition consisting of at least one hydrolytic enzyme, at least one polyamine, and/or cationic or anionic polyacrylamide and/or carboxymethyl cellulose.
NOVELTY - Discharging contaminants of a carburetor for carbonaceous material, preferably a fluidized bed reactor (6), comprises converting biomass and/or coke in an influx of a gasification agent into product gas, maintaining the biomass and/or coke in the influx of a gasification agent as a fixed bed (12) in the fluidized bed reactor, allowing contaminants to sink or move in a space (16) beneath the fixed bed against the influx of the gasification agent and collecting contaminants.    USE - The method is useful for discharging contaminants of carburetor for carbonaceous material, preferably fluidized bed reactor (claimed).    ADVANTAGE - The device ensures reliable, safe and long-term operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for discharging contaminants of a carburetor for carbonaceous material, where the carbonized biomass in the influx of the gasification agent is arranged as a fixed bed within the fluidized bed reactor and a space is provided below the fixed bed for collecting contaminants.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the a cross sectional view of a section of the reduction unit.    Fluidized bed reactor (6)    Fixed bed (12)    Inlet region (14)    Space (16)    Lifting unit (27)
NOVELTY - Enzyme-composition comprises at least one cellulase, at least one hemicellulase and at least one pectinase, where the hemicellulase comprises an arabinan endo-1,5- alpha -L-arabinosidase with an arabinan degrading activity of at least 10 U/mg protein.    USE - The enzyme-composition is useful for hydrolyzing biomass, where the biomass is sugar-beet, sugarcane, straw, maize, wood, and/or oilseed (all claimed).    ADVANTAGE - The enzyme-composition: enables the complete degradation and/or hydrolysis of saccharide and/or polysaccharide containing biomass within reasonable time; exhibits high performance; and is obtained in cost efficient manner in high quantities.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for hydrolyzing biomass comprising contacting the biomass with the enzyme-composition, and subjecting at least one part of the biomass to a filtration and separating the permeate.
NOVELTY - A center c. dispensing a according to state vein medicine collective configuration centre and, wherein a and b. dispensing product design, by a dispensing needle head... a low-drag syringe composed of, when dispensing needle head solves the problem that the penicillin bottle and ampoule medicine series arrangement is convenient, problem of pollute and foreign matter, an injector solves the problem that the low-resistance injector, glue plug to failure after a water overflow problem is.
NOVELTY - The new type utility claims a biomass solid fuel forming a system, referring to solid forming a field, a pulverizer, a conveyor belt machine, forming machine, and comprising a mixer, blender motor, a rotating rod, a chain box, a rotating rod and stirrer bracket, hopper on the machine bracket, a is ladder-shaped funnel, in a side fixed has a chain box, a chain box provided with a chain transmission mechanism, the machine is a motor and a chain transmission mechanism connecting the first rotating rod and the second rotating rod parallel set at a bottom end of a material wherein two side, a rotating rod and a second rotating pole is a chain transmission mechanism through connecting, the first rotating rod and the second rotating pole respectively provided with a first rotating rod and the second rotating rod and a series of a vertical stirring teeth. The utility model is new type can save labour, increase working efficiency, reduce a wear rate, it can further protect device, ensuring normal operation of device, further reducing maintain cost, realize automatic.
NOVELTY - A planting energy grass alcohol combustion and then circulation of marsh gas pool, comprising reaction between a and a catalyst, a reaction catalyst and a set with clapboard, a reaction part set with a reservoir, a reaction pool equipped with a feeding port, a catalytic pool equipped with a feeding port, a bottom part catalytic heater, a heat pump heater, a catalytic a mounted power generation unit and power generation unit connected a, b. connecting gas-guide tube and a water pressure controller. The utility model is new type extracting alcohol, belongs to biomass energy, because of biomass fuel does not contain thio phosphorus, not a thio dioxide and phosphorus pentoxide when burning, not caused by a rain product does not pollute atomphere does not pollute environment. Biomass fuel clean and sanitary, convenient feeding, reducing the labour intensity of the worker, large of improves the working environment, the enterprise will used for the aspect of the labor cost, ethyl alcohol also easy storage and transfer, by using relative safety.
NOVELTY - Method for producing lipids, involves (i) providing a cultivation medium comprising a lignocellulosic hydrolysate, (ii) providing a fermentation broth by inoculating the cultivation medium of (i) with a first microbe, where the first microbe is an oleaginous microbe, and (iii) incubating the medium inoculated with the first microbe allowing lipids to accumulate under aerobic conditions, where the fermentation broth comprises at least one microbial growth inhibitor, and the first microbe is tolerant to the microbial growth inhibitor(s).    USE - The method is used for producing lipids (claimed) which is used as raw material for production of biofuels such as biodiesel, renewable diesel or jet fuel.
NOVELTY - Pre-composting drum (10) comprises a main body (11), an inlet shutter (12), an outlet shutter (13), and optionally a supply chute (14). The pre-composting drum further comprises at least one inlet, at least one ventilation device, and a selective blocking device per inlet for selectively uncovering or covering the inlet, where the blocking device comprises a flange inserted into an inlet and a mobile stopper mounted on the flange, and the mobile stopper comprises a guide element configured to come into contact with a guide rail.    USE - Used as pre-composting drum.    ADVANTAGE - The pre-composting drum allows for controlling ventilation or exhaust air and can be rotated by be closed by trapping a quantity of air that can be injected and extracted in a controlled manner, thus improving the fermentation day and night, while avoiding the drum going into anaerobic mode. The support and the movable shutter both have a substantially planar form and tangent to circumference of the drum, thus allowing for easy manufacturing, good sealing and simpler operation.    DESCRIPTION OF DRAWING(S) - The figure shows a longitudinal section of the pre-composting drum.    Pre-composting drum (10)    Main body (11)    Inlet shutter (12)    Outlet shutter (13)    Supply chute (14)
NOVELTY - A combustion fuel product (32) is produced by (i) providing 1st fibrous wetland biomass (10), (ii) squeezing (12) 1st fibrous wetland biomass to produce liquid (14) and fibrous plant residue (16,18), (iii) using slow pyrolysis (22) to produce biochar (24) and heat (26), (iv) using the heat to produce dried wetland biomass (30), and (v) compacting biochar with dried wetland biomass.    USE - Production of combustion fuel product.    ADVANTAGE - The washing and pressing process used to product the fibrous fraction significantly reduces the mineral content compared to the 1st raw feedstock, resulting in reduced emissions and better quality combustion fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram of the production method of combustion fuel product.    1st fibrous wetland biomass (10)    Squeezing step (12)    Squeezed liquid (14)    Liquid and fibrous plant residue (16,18)    Slow pyrolysis (22)    Biochar (24)    Heat (26)    Dried wetland biomass (30)    Combustion fuel product (32)
NOVELTY - Method for preparing ethanol, involves preparing liquid mixture by adding additional liquid comprising at least one acetic acid, formic acid, furfural and hydroxymethyl furfural to saccharide, adding microorganism to the mixture, and fermenting the mixture.    USE - The method is useful for preparing ethanol (claimed).
NOVELTY - The new type utility claims water amphibious harrow tooth type modified bottom machine, comprising water amphibious walking module and raking module; the water amphibious walking module comprises a ship body, a paddle wheel and motor, motor installation body. b, two side symmetrical installation has N to paddle, N is not less than 1, the motor drives the paddle wheel rotating, the raking module comprises underwater harrow teeth, harrow teeth connecting rod, a bolt, a walking universal; a underwater harrow tooth rake teeth connecting rod by a universal to walking, running between a universal structure and the ship body through a spring, the device can move a floor flexible and not limited by the limit is not limited by the lake size limit, but also can move in water, sludge of water is easy to stir, complete a shelter.
NOVELTY - The new type utility claims a water amphibious double wherein with a modified bottom machine, comprising water amphibious walking component and the sludge and spray component; the water amphibious walking module comprises a ship body, a paddle wheel and motor, motor installation body. b, two side symmetrical installation has N to paddle, N is not less than 1, the motor drives the rotating paddle, the sludge suction and spray component comprises sucking pump motor, sewage pump, the water dirt suction plate, spray sucking pipe and mud-water spray head, sucking pump sucking pipe through a water suction sewage disk, sucking pump sucking spray pipe through a water spray head, suction sewage pump by sucking pump.; sucking pump motor installation body. b, the device can move a floor flexible and not limited by the limit is not limited by the size limit lake, can freely move in the water surface, a complete amphibious.
NOVELTY - Industrial-scale production of natural gas comprises processing biomass from food waste, dead animals, algae, grasses, rice husks, sewage and other biomass residues in two pyrolysis furnaces using catalysts. The natural gas comprises 97% methane and balance butane, propane, ethane, pentane and other gases.    USE - Method for industrial-scale production of natural gas (claimed).
NOVELTY - The utility model is new type relates to a garbage percolate a zero discharging device, a water collecting well, a water collecting well set has a used for collection the percolate collection pipe, a water collecting well and tempering with a tempering liquid is connected with, a pool and a fermentation room connected with, a... and a. spray into a fermentation chamber,... a. t. used for producing hot water evaporation of a biological matrix, and the existing technology, the utility model is new type comprises the following beneficial effect: the structure is simple, the operation cost low, a garbage percolate complete zero discharge,... a biological matrix using the accumulated slag material after a long time after, also a municipal green as a fertilizer or landfill.
NOVELTY - The new type utility claims a. treating pollute water body ecological floating island, comprising a floating bed, planting basket, aquatic plant, planting basket equipped with a floating bed on the planting basket in planting aquatic plant. A water floating bed contact surface connecting a immobilized microorganism microbial inoculum is added device. A water floating bed contact surface also a biological elastic three-dimensional filler. The utility model is new type agricultural waste as a filler matrix, which is good for recycling the waste using; when the agricultural waste supply denitrification bacteria taking ammonia nitrogen degradation of carbon source needed to promote degradation of pollutant, increase water quality purification efficiency, adopts a water body of upper, middle and lower a a feeding method of immobilized microorganism microbial inoculum, which is good for enhancement in a degradation of water body and the bottom layer and pollutant in mud, increase purification efficiency of pollute water body, at the same time comprises a lasting time is.
NOVELTY - The utility model relates to a marsh gas pool, especially a plant can automatically for increasing and preserving temperature of the marsh gas pool. A. warming and heat-preserving biogas pool, comprising biogas pool main body, set has header at the top part of the marsh gas pool main body, said header including inner layer and outside layer, outside cover b... a,... a is double layer vacuum transparent material, the outer layer is sun-shading material. The utility model is new type and existing technology, comprises following advantages: structure is simple, durable, increasing heat preservation effect is good, and no need increase.
NOVELTY - The new type utility claims one kitchen garbage Anaerobic fermentation tank for the mud blowing system, wherein, water supply pipe, water supply pipe and the tank body are concentric ring. Anaerobic fermentation tank comprises tank body, annular structure is on the tank body outside; ring water pipe connected with the water pipe, water supply ring pipe is four quadrant point position of the branch connected with the centre pipe, the branch pipe valve and a water supply pipe connection or closed, internal branch pipe extends into the tank body, the branch pipe on the tank body of tank body set with internal vertical pipe is branch pipe, branch pipe for pipe; on tube are cloth set multi-purging group, each group is two of purging, purging is 45 degrees downwards.
NOVELTY - The new type utility claims a reflux filter. Anaerobic fermentation tank, belongs to device field, the device comprises tank body, driving device, stirring device, filtering device, three-way valve, return circulation device, heating coil, feeding port, an air outlet, the utility model is new type equipped with a stirring leaf at the upper part in the tank body is radial force with strong cutting effect, large particle diameter solid object is dispersed and biogas slurry the full mixing, at the same time the material crust, and biogas tank body bottom to force the slurry circulation tank body of internal flow, forming liquid stirring, increase stirring effect, effective reduce consume power under stirring action of screw pump, equipped with two of discharging port, the biogas and slag discharge in tank, increase the fermentation efficiency, device can save raw material, further reducing cost, the utility model is new type has simple structure and easy operation.
NOVELTY - A novel efficient solid fermentation tank, relating to biological fermentation engineering equipment field, especially a novel efficient of a livestock and poultry excretion object to carry out microorganism strain fermentation process is solid fermentation tank. A vertical tank body setting on a jacket, speed reducing electric machine is fixed on the top of the machine frame end, a hollow stirring shaft by a speed reducing motor output hole after a charging rotary joint, lower end connected with stirrer and a bottom bearing support, when... and a material of high warm, tank body material to carry out continuous stirring and oxygen, a oxygen fermentation process. a material from the material inlet of the jacket of the jacket bottom pump jacket, after a material for slowly cooling along with the spiral plate inner jacket from jacket upper jacket material outlet to the inner tank, a heating process. The utility model is new type, a simple and compact structure, reasonable distributing, manufacturing cost low, stirring uniformly, oxygen effect is good, the suitable operation, a waste sum collective processing is equal.
NOVELTY - The utility model claims a water collecting groove of blood sampling vessel, the collecting groove bottom provided with micro-pore, the micro-hole are a blind hole and annular distribution in bottom water collecting groove, the water collecting groove is provided with a parting strip and for the two divided a number a, in the water collecting groove has a hydrophilic coating material. The sample vessel of the water groove by the siphon effect and hydrophilic material is lyophilic, water adsorption fixing for a collection of, and thus avoids a water outflow pollute working environment and in using process.
NOVELTY - The utility model relates to a kit for detecting PRKAA1, used for detecting reagent kit of PRKAA1, main comprising a box body, a box cover, a box cover switch, a support, PRKAA1 forward primer reagent tube, PRKAA1 reverse primer reagent tube, containing Mg2 + buffer solution reagent tube, PCR amplification agent reagent tube, agarose cream agent tube, a contrast card, tube cover, combined RT-PCR technology for storing pig PRKAA1 carrying out a check, thus carrying out research of low oxygen capacity suitable for plateau animal, a positive and reverse primer of PRKAA1 gene and a split charging of different reagent tube, combined with Mg2 + buffer solution reagent tube, PCR amplification agent reagent tube, agarose cream agent pipe to PRKAA1 carry out a check, the utility model is new type structure is simple, design is reasonable, suitable operation, suitable carry, not easy to pollute, and obviously increase the PRKAA1 gene detection efficiency.
NOVELTY - The new type utility claims a series-wound cell culture bag, comprising: a bag body, input pipe, input pipe and a bag body connected, a nutrient solution used for input to the first bag body and the second bag body, bag body the second volume larger than the first volume bag, a pipe, a pipe set in the first bag body and the second bag body between, used for connecting the first bag body and the second bag body, a tube, a tube equipped with a bag body in a, for a nutrient solution. According to a FORMULA a culture bag of the utility model is new type can make immune cell culture experiment operation is simple and easy to use,. bacteria or fungi reduce pollute is a possibility.
NOVELTY - Biomass-derived pyrolysis oil is contacted with deoxygenating catalyst (C1) in presence of hydrogen at predetermined hydroprocessing condition (P1) to form low-oxygen biomass-derived pyrolysis oil effluent (16). The deoxygenating catalyst (C1) comprises neutral catalyst support comprising titanium oxide in anatase phase, nickel, cobalt and molybdenum. The content of nickel in deoxygenating catalyst (C1) is 0.1-1.5 wt.% based on conversion of oxide.    USE - Deoxygenation of biomass-derived pyrolysis oil during manufacture of biofuel used in boiler and furnace applications.    ADVANTAGE - The biomass-derived pyrolysis oil is deoxidized by effective method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for catalyst for deoxygenating biomass-derived pyrolysis oil, which comprises neutral catalyst support comprising titanium oxide in anatase phase, nickel, cobalt and molybdenum. The content of nickel, content of molybdenum and content of cobalt in deoxygenating catalyst (C1) is 0.1-1.5 wt.%, 10-20 wt.% and 2-4 wt.%, respectively, based on conversion of oxide. The neutral catalyst support is chosen from titanium dioxide support, zirconium dioxide support, niobium pentoxide support and theta alumina support.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for deoxygenating biomass-derived pyrolysis oil.    Feed stream (12)    Hydrogen-containing gas (13)    Hydroprocessing reactors (14,28)    Low-oxygen biomass-derived pyrolysis oil effluents (16,32)    Water-depleted low-oxygen biomass-derived pyrolysis oil effluent (22)
NOVELTY - A device comprises fatty acid sorbitan ester (I) which is solid or semi-solid, and a container for holding the fatty acid sorbitan ester. The container is configured to allow the lubricant to flow therethrough. The device is configured to allow the lubricant to pass over and/or through the fatty acid sorbitan ester, such that fatty acid sorbitan ester is released into the lubricant.    USE - Device is used for providing additive to lubricant. The fatty acid sorbitan ester composition can also be used in fuel compositions e.g. hydrocarbon fuels, gasoline, diesel fuels, and biodiesel, for improving friction reducing ability.    ADVANTAGE - The reduction of lubricating properties of the lubricant over time can be replenished or enhanced.    DETAILED DESCRIPTION - A device comprises fatty acid sorbitan ester of formula (I) which is solid or semi-solid, and a container for holding the fatty acid sorbitan ester. The container is configured to allow the lubricant to flow therethrough. The device is configured to allow the lubricant to pass over and/or through the fatty acid sorbitan ester, such that fatty acid sorbitan ester is released into the lubricant.    n=6-22.
NOVELTY - This utility new model relates to upper part of one rotary kitchen waste biochemically, upper bracket set with motor, motor through speed reducer and driving shaft connected with the driving shaft and driving roller wheel is installed on the connecting bracket, driving roller wheel and roller set on outside wall of the exterior material, the bracket, upper bracket mount and roller tangent with the supporting roller wheel, front end is set with storage hopper can rotate around the storage chamber body axis relative rotation of rotary joint, the rotary joint is set with upper with hopper, back end is equipped with storage hopper can rotate around the storage chamber body with relative rotation axis and swing joint, upper swing joint has set up for gas/water pipe and returning gas/water pipe, air inlet pipe and discharge pipe. This new utility model adopt rotary bin body structure, rotary stirring material bin body, rotary joint and swing joint can ensure normal feedstock, discharging, air inlet, and normal discharge of steam/water, returning gas/water, normal input measurement data one time processing amount large, needed drive power small, high efficiency, high efficient energy saving.
NOVELTY - The utility model is new type relates to pollute soil ectopic curing stabilizing device and repairing kit, the kit device by soil, quantitative feeder, a solid medicine preparation chamber, weigh spiral feeder, a liquid medicine preparation tank, medicament pump, a spray, soil crusher, a feeding belt machine, cutting crushing mixing device, soil mixer, a discharging belt machine, scattering mixing a crushing one, according to a different pollute the soil, a solid or liquid medicine preparation for repairing heavy metal pollute soil a rapid repair, to pollute soil and soil water content suitable for range is wide, a large capacity, adding drug measuring precision high, crushing mixing effect is good, the automatic degree high, b heavy metal pollute soil ectopic curing stabilized repairing process, and a used for organic pollute soil ectopic chemistry oxidation repairing process, comprises a good environment protection benefit and social benefit.
NOVELTY - Carbonization system comprises multiple valves (41) for adjusting the movement direction of gas and carbonization heat, multiple carbonization furnaces for producing charcoal, and multiple heat transferring pipes (21) for circulating gas and carbonization heat of the carbonization furnace. The system carbonizes and dries wood by circulating carbonization heat.    USE - The system is useful for carbonizing and drying wood (claimed).    ADVANTAGE - The system reduces charcoal manufacturing cost by reducing the cost and time of the wood movement within the drying chamber and the carbonization furnace, recycles the energy by using the carbonization heat which is waste heat source from the charcoal production process, and does not require separate drying chamber for drying the essential elements wood.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the carbonization system.    Combustion port (11)    Heat transferring pipe (21)    Outlet port (31)    Valve (41)    Panel (51)
NOVELTY - A composite microorganism fertilizer comprises 4-6 pts. wt. organic manure, 2-4 pts. wt. humic acid, 0.7-3 pts. wt. agricultural organic waste, 0.2-0.4 pt. wt. seafood organic waste, 0.01-0.02 pt. wt. liquid microbial inoculum and 0.005-0. 01 pt. wt. solid microbial inoculum.    USE - Composite microorganism fertilizer.    ADVANTAGE - The fertilizer provides easy absorption of nutrient, promotes healthy growth, produces fulvic acid as plant growth regulator, is environment-friendly and harmless, has organic matter content, and sets with improved soil structure effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite microorganism fertilizer comprising taking agricultural organic waste, solid microbial inoculum, mixing to obtain compound, mixing organic manure, seafood organic waste and agricultural organic waste, adding liquid microbial inoculum and premix, mixing uniformly, aerobic fermenting, adding humic acid to obtain mixture, aerobic fermenting for 21-35 days, adjusting water content to less than 35%, and sieving.
NOVELTY - An organic fertilizer is prepared by taking 25 wt.% rice hull and 35 wt.% livestock manure, mixing uniformly, stacking to prepare material A, mixing 20 wt.% rice bran, 10 wt.% bone meal and 10 wt.% peat to prepare mixture B, mixing uniformly, adding fermentation bacteria at ratio of 1:90-110 for 24 hours to obtain material C, mixing materials A and C, and stack fermenting for 60 degrees C for 8 hours.    USE - Organic fertilizer.    ADVANTAGE - The fertilizer has less harmful substances, and is absorbed by crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of organic fertilizer comprising mixing organic fertilizer and nitrogen, phosphorus, potassium inorganic fertilizer to prepare formulated fertilizer prescription, granulating, separation filtering 5 mm, drying, separation filtering 3 mm, coating, and coloring using colorant.
NOVELTY - A straw decomposition agent comprises 20-40 pts. wt. biogas sludge, 30-60 pts. wt. organic waste and 5-15 pts. wt. composite microorganism strain.    USE - Straw decomposition agent.    ADVANTAGE - The agent accelerates decomposition time, satisfies crop growth need, reduces fertilizer use, has wide material source, low cost and active high strain, and increases decomposing effect of straw.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of straw decomposition agent comprising mixing all raw materials, fermenting for 3-6 days, crushing, and drying.
NOVELTY - Stack-type composting of livestock corpse comprises premixing organic carbon source material, regulating water content to 40-50%, spreading on floor, spreading livestock corpse, mixing, regulating carbon/nitrogen ratio of 25-40%, stacking at 45 degrees C for 30-35 days, decomposing, composting for 1.5-2 months, fermenting and sieving.    USE - Method for stack-type composting of livestock corpse (claimed).    ADVANTAGE - The simple, economical and safe method saves resources and reduces cost.
NOVELTY - A fertilizer formulation comprises 20-25 wt.% straw, 15-20 wt.% nitrogen fertilizer, 15-20 wt.% phosphate fertilizer, 15-20 wt.% potassium fertilizer, 5-8 wt.% probiotic solution, 1-2 wt.% urea, 2-3 wt.% ammonium nitrate, 1-2 wt.% calcium superphosphate, and 0.5-1 wt.% potassium sulfate.    USE - Fertilizer formulation used for Althaea (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer formulation comprising taking straw, cutting to length of 1-3 cm, adding soybean meal, organic solution, and probiotic solution turn, mixing, piling to width of 2 m, and height of 1 m, covering with plastic sheeting, fermenting for 12-24 hours, reacting at 50 degrees C, fermenting, reacting at 65 degrees C, crushing, sieving, sprinkling nitrogen fertilizer, phosphate fertilizer, and potassium fertilizer, and adding remaining raw materials.
NOVELTY - Compound fertilizer comprises 30-35 pts. wt. sheep manure, 15-20 pts. wt. straw, 10-15 pts. wt. pumpkin vine, 7-10 pts. wt. tea leaf, 4-6 pts. wt. chitosan, 6-10 pts. wt. hydrated lime, 10-12 pts. wt. potassium fulvate, 7-10 pts. wt. nano non-metal mineral material, 1-2 pts. wt. sodium selenite, 3-5 pts. wt. amino acid, 1-2 pts. wt. Trichoderma, 0.5-1 pts. wt. Saccharomyces cerevisiae and 0.5-2 pts. wt. effective microorganisms.    USE - Compound fertilizer used for preventing and treating southern blight disease of Clivia miniata (claimed).    ADVANTAGE - The compound fertilizer reduces use of fungicide, and restrains generation of plant diseases and insect pests.
NOVELTY - High-calorie granule fuel comprises 20-30 pts. wt. crop straw, 30-40 pts. wt. wood meal, 10-15 pts. wt. pine wood meal, 5-10 pts. wt. bagasse, and 1-2 pts. wt. calcium oxide. It is prepared by pulverizing all components to obtain particles; uniformly mixing components according to proportion; further pulverizing; drying until moisture content is 6-13%; and granulating to obtain granule fuel.    USE - High-calorie granule fuel.    ADVANTAGE - The high-calorie granule fuel uses different waste fuels, does not use chemical additives, and uses reasonable fuel feed ratio. The fuel heat can be fully released by calcium oxide to effectively prevent slagging combustion and achieve bonding through pine combustion.
NOVELTY - Stable particle fuel comprises 25-30 pts. wt. wood meal, 5-10 pts. wt. crop straw, and 2-4 pts. wt. biomass combustion binder. It prepared by drying crop straw to moisture content of 8-14% and wood meal to moisture content of 5-8%; mixing crop straw, wood meal and biomass combustion binder according to proportion; and extrusion molding to obtain particle fuel.    USE - Stable particle fuel.    ADVANTAGE - The stable particle fuel improves utilization of renewable raw materials, can fully release contained heat, has firm structure, and is non-friable.
NOVELTY - The method involves measuring catalytic reactivity of a front side of an article e.g. catalyst (15), with a test medium such as propane or carbon monoxide, with defined composition by an integrated diagnostic and cleaning device (2) through an opening (5). Concentration of reduced or oxidized part of the test medium is measured at a downstream position after passing through an object. The measurement of the quality is carried-out through a medium or an electromagnetic radiation. Counter-pressure and/or pressure loss and/or change of volume flow are measured on the article.    USE - Method for diagnosing a gas-permeable article e.g. catalyst or filter (all claimed), in a vehicle.    ADVANTAGE - The method enables measuring catalytic reactivity of the front side of the article with the test medium with a defined composition by integrated diagnostic and cleaning device through the opening so as to determine aging behavior of catalyst and quality of catalytic coating in a present condition in automated and accurate manner at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for diagnosing an article.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a device for diagnosing a gas-permeable article.    Integrated diagnostic and cleaning device (2)    Housing (3)    Opening (5)    Catalyst (15)    Valve (17)
NOVELTY - A. composite type straw forming machine, it comprises saw pressing roller (1), pressing forming roller (2), pressure plate (3), a cross plate (4), a power shaft (6), an extruding mould (7), wherein, at the same time set with extrusion forming and cutting a pre-pressing component, a squeezing mould (7) centre is equipped with vertical power shaft (6), a horizontal cross connecting plate set on a power shaft (6), (4), set with two molding pressure roller of a cross connecting plate (4) on (2) symmetrically and two saw tooth of pressure roller (1), a squeezing mould (7) upper part is set with horizontal saw tooth pressure plate (3), a power shaft (6) drives the cross connecting plate (4), pressing forming roller (2), pressure roller (1) rotating. The advantage is as follows: taking raw material cutting, rolling, increase the adaptability of raw material, reduces the idle work consumption, reduce the abrasion of forming part, improves the forming effect through pressure roller and saw tooth pressure plate.
NOVELTY - This utility new type claims a. organic waste harmless, comprising feeding a fermentation unit. C,.... unit middle part upper pneumatic discharging door 9... groove body upper layer 3 and the lower layer groove body. 8, the lower groove body. 8. the lower pneumatic discharging door bottom 10, the lower discharge air 10 is set with the discharge conveyor belt 11, wherein the upper groove body. 3 and lower groove body. 8 respectively equipped with two electrical machine group 4, each driving one of double-propeller; in addition, also equipped with the hot water and hot air pipe. groove in. This utility new type aiming at harmless treatment of organic waste and the research and development of. device, aiming to provide a effective reduce a harmless treatment device of organic waste of energy consumption, thus to save the can, the purpose of environmental protection.
NOVELTY - Producing a yield increasing material comprises composting waste sludge from a mixture of cellulose containing wastes and a vaccine containing microorganisms. 38-50 pts. wt. Municipal waste sludge is mixed with a 40-55 pts. wt. waste material mixture which contains 50-90 pts. wt. saw dust and/or wooden cuts and hay, straw, plant stalks (preferably sunflower stalks and maize stalks), 5-60 pts. wt. green waste in public area, preferably grass, scything product, cut boughs or other uncontaminated green wastes added to 0-10 pts. wt. coffee lees and 100 pts. wt. fruits or vegetables mixed with it.    USE - The process is useful for producing a yield increasing material.    DETAILED DESCRIPTION - Producing a yield increasing material comprises composting waste sludge from a mixture of cellulose containing wastes and a vaccine containing microorganisms. 38-50 pts. wt. Municipal waste sludge is mixed with a 40-55 pts. wt. waste material mixture which contains 50-90 pts. wt. saw dust and/or wooden cuts and hay, straw, plant stalks (preferably sunflower stalks or maize stalks), 5-60 pts. wt. green waste in public area, preferably grass, scything product, cut boughs or other uncontaminated green wastes added to 0-10 pts. wt. coffee lees and the necessary amount of 100 pts. wt. fruits or vegetables mixed with it. A 4-5 pts. wt. known vaccine is added and then it is composted in a prism in a known manner, and 0.5-5 pts. wt. optionally yellow light-pre-treated microorganism is blended at 6-12x 105-1012 living cell/g and applied onto a porous sweet water limestone carrier, which contains microorganisms of Actinomyces sp., Cellulomonas flavigena and Azotobacter chroococcum. The composting is continued in the known manner after blending in the second vaccine and then the compost is packaged.
NOVELTY - Propagation of purple potato involves taking purple potato seed, and performing potato cultivation of 85% local sweet potato of various type and 15% sweet potato propagated on culture matrix in cold environment at 7-20 degrees C.    USE - Method for propagating purple potato (claimed).    ADVANTAGE - The method is safe, environmental-friendly and does not need pesticide. The purple potato is rich in protein, potassium, calcium, iron and vitamins A, B1, B2, B3 and B6.
NOVELTY - A bean planting method involves selecting cold resistant, strong disease resistant and high yield, better quality bean seeds, adding base fertilizer to soil, turning deep soil after fertilization, and adding manure, gas liquid, slow release granular fertilizer and soil conditioners to the field. The fertilizer is uniformly mixed with soil. The bean seeds are sown and allowed to grow. The beans are harvested, followed by performing pest control.    USE - Method for planting bean.    ADVANTAGE - The method enables planting bean without any diseases and with excellent market value in a safe, cost-effective and environmental-friendly manner.    DETAILED DESCRIPTION - A bean planting method involves selecting cold resistant, strong disease resistant and high yield, better quality bean seeds, adding base fertilizer to soil, turning deep soil after fertilization, and adding 600-640 kg/acre manure, 80-100 kg/acre gas liquid, 280-320 kg/acre slow release granular fertilizer and 100-140 kg/acre soil conditioners to the field. The fertilizer is uniformly mixed with soil by tractor with a groove length of 1.5 m and groove depth of 20 cm. The bean seeds are sown into each hole with a spacing distance of 35-40 cm, where each hole is filled with 4 seeds. The bean seeds are allowed to grow to a length of 18-22 cm, and stacked in each rack to grow to a length of not less than 2.5 m. The beans are harvested when the flat and round beans are tender and produced at high yield, followed by performing pest control by spraying 2-3 times of mixed solution containing chlorothalonil, thiophanate, deltamethrin, dichlorvos, sumicidin and other insecticides.
NOVELTY - A lead ion imprinted membrane separation and enrichment of lead(II) ion in biogas slurry comprises preparing lead ion imprinted membrane, taking livestock pollutants of biogas residual slurry, filtering via quartz sand, removing suspended solids, passing through lead ion imprinted membrane, and separating.    USE - Lead ion imprinted membrane separation and enrichment of lead(II) ion in biogas slurry.    ADVANTAGE - The method is simple and low-cost.
NOVELTY - The micro-tunnel has an anaerobic reaction tank (1) whose top portion is provided with a flexible floating cover. The biogas is produced by anaerobic reaction tank through gas collection system which collects the biogas in the biogas tank (8). The partition curtain walls are arranged in staggered arrangement of the anaerobic reaction tank. S-shaped flow channel is formed inside the anaerobic reaction tank.    USE - Micro-tunnel for biomass processing of anaerobic bioreactor.    ADVANTAGE - The residence time of reaction liquid in the anaerobic reaction tank is increased. The re-use portion of the biogas system is reused. The cost of the anaerobic bioreactor is reduced. The efficiency of the anaerobic bioreactor is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the micro-tunnel for biomass processing of anaerobic bioreactor.    Anaerobic reaction tank (1)    Pump station (7)    Biogas tank (8)    Water pipe (103)    Gas discharging system (204)
NOVELTY - The method involves obtaining crushing product (3) by entering the coal (1) into the feeding crusher (2). The petrochemical wastewater (6) is provided in the stirring bucket (7), when the biochemical process is performed. The value of the water portion is adjusted by adding acid solution to stirring bucket. The dehydrated cake (15) is inserted into the stirring bucket from barrel. The pulping bucket (17) is provided with the water-coal-slurry additive. The water-coal-slurry (18) is obtained from water-coal-slurry boiler (19).    USE - Petrochemical waste water treating process.    ADVANTAGE - The petrochemical waste water treating process is performed at low coast and operated easily and conveniently. The consumption of the water in the chemical industry is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the petrochemical waste water treating process. (Drawing includes non-English language text)    Coal (1)    Feeding crusher (2)    Crushing product (3)    Petrochemical wastewater (6)    Stirring bucket (7)    Dehydrated cake (15)    Pulping bucket (17)    Water-coal-slurry (18)    Water-coal-slurry boiler (19)
NOVELTY - Plasma pyrolysis sludge syngas device comprises plasma reactor for supplying high voltage power supply; where the plasma reactor includes a quartz vessel, polytetrafluoroethylene flange, stainless steel frame, graphite electrode tip, flat graphite electrode, copper ring, ceramic crucible disaster, inlet channel and outlet channel. The graphite electrode tip and the flat graphite electrode are connected by high-voltage wire and high pressure supply.    USE - Used as plasma pyrolysis sludge syngas device.    DETAILED DESCRIPTION - Plasma pyrolysis sludge syngas device comprises plasma reactor for supplying high voltage power supply; where the plasma reactor includes a quartz vessel, polytetrafluoroethylene flange, stainless steel frame, graphite electrode tip, flat graphite electrode, copper ring, ceramic crucible disaster, inlet channel and outlet channel. The graphite electrode tip and the flat graphite electrode are connected by high-voltage wire and high pressure supply. The graphite electrode tip and flat graphite electrode are coaxially disposed within a quartz container; where the quartz vessel is fixed to the stainless steel stent via polytetrafluoroethylene flange. The flat graphite electrode is fixed on the upper flange of the copper polytetrafluoroethylene seal loop fasteners, where the tip of the graphite electrode is fixed to copper ring by polytetrafluoroethylene lower flange. The inlet channel is connected to the polytetrafluoroethylene flange, and the polytetrafluoroethylene flange is connected to the outlet channel. The bottom opening of the ceramic crucible is placed in a graphite electrode tip and flat graphite electrodes, for loading sludge, and when the device is working, and the sludge in the ceramic crucible will be fully exposed to the non-thermal arc plasma region.
NOVELTY - The system has a dehydration device (4) that is provided with a bucket which is set with a filtering hole. A belt driving device is mounted at a platform to drive the bucket centrifugally. A conveyer is equipped with a urine pool. A conveying device is arranged with dehydration device. A carrier (2.2) is arranged on a wall of the urine pool. A stage is equipped with a collection bucket (9). A window (2.3) is opened in the collection bucket at height same as urine pool. The window is closed or opened through a window cover plate (11).    USE - Public toilet excrement anhydrous comprehensive treatment recovery system.    ADVANTAGE - The energy saving effect of the recovery system is ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the public toilet excrement anhydrous comprehensive treatment recovery system.    Carrier (2.2)    Window (2.3)    Dehydration device (4)    Collection bucket (9)    Window cover plate (11)
NOVELTY - Biological fertilizer is prepared using brown sugar, fresh fruit or vegetable, and water.    USE - As biological fertilizer.    ADVANTAGE - The biological fertilizer ensures to improve soil fertility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the biological fertilizer, which involves (a) dissolving brown sugar in water, and (b) adding remaining raw materials to the resulting mixture and fermenting the mixture for 80-100 days to obtain product.
NOVELTY - Method for aerobic fermentation of sewage residue involves using mineral admixture comprising diatomaceous earth having diameter of 3-30 mm.    USE - The method is useful for aerobic fermentation of sewage residue using mineral admixture (all claimed).    ADVANTAGE - The method is cost-effective and reliable.
NOVELTY - A preset amount of octacosanol, fatty acid, dehydrating agent and catalyst are added to dry round-bottomed flask, preset amount of organic solvent is added, stirred in magnetic stirrer, temperature and stirring speed is controlled, and reacted for preset time. The resulting mixture is filtered, and organic solvent is removed by rotary evaporation to obtain crude octacosanol ester. The crude product is separated to obtain pure octacosanol ester.    USE - Preparation of octacosanol ester used in food, chemical, medicine and cosmetic application.    ADVANTAGE - The method provides octacosanol ester with less side reactions under mild reaction condition, by environmentally-friendly process. The octacosanol ester is easily separated.
NOVELTY - The preparation of isonicotinic acid by hydrolysis involves adding 4-cyanopyridine, sodium hydroxide and purified water to a multi-neck flask, stirring the mixture and then heating, performing hydrolysis reaction for 1-3 hours to obtain 4-pyridinecarboxylate, adding activated carbon to 4-pyridinecarboxylate, heat preserving the mixture for 0.5-1.5 hours and then filtering to obtain a filtrate, dripping hydrochloric acid to the filtrate, crystallizing the mixture and then washing, filtering the mixture and then placing in a drying oven, and drying.    USE - The method is useful for preparation of isonicotinic acid by hydrolysis (claimed).    ADVANTAGE - The energy-saving method enables economical preparation of isonicotinic acid with high purity.    DETAILED DESCRIPTION - The preparation of isonicotinic acid by hydrolysis involves adding 4-cyanopyridine, sodium hydroxide and purified water in a mass ratio of 1:0.39-0.80:2-4 to a multi-neck flask, uniformly mixing, stirring the mixture and then heating, increasing the temperature at 90-115 degrees C, adding purified water to the mixture, controlling the temperature at 90-115 degrees C, performing hydrolysis reaction for 1-3 hours to obtain 4-pyridinecarboxylate, increasing the temperature at 70-80 degrees C, adding activated carbon to 4-pyridinecarboxylate and then stirring, heat preserving the mixture for 0.5-1.5 hours, controlling the temperature at 70-80 degrees C, bleaching the mixture and then filtering to remove activated carbon to obtain a filtrate, dripping hydrochloric acid to the filtrate, adjusting pH value to 3.5-4 for 5-15 minutes, crystallizing the mixture and then washing using water, filtering the mixture to obtain a wet product and then placing in a drying oven, and drying.
NOVELTY - An abamectin ester derivative (I) is new.    USE - Abamectin ester derivative used as active component or agent of pesticide (claimed) for killing moth, miner, and aphids.    ADVANTAGE - The compound has high efficacy, long duration, no residue, pollution-free characteristic, high insecticide activity, poisoning and killing effects, and low dosage and is stable, quick and non-resistant.    DETAILED DESCRIPTION - An abamectin ester derivative of formula (I) is new.    R=OCCH2Ph or OCCH3;    R1=CH2CH3 or CH3; and    X-Y'=CH=CH or CH2CH(OH).    An INDEPENDENT CLAIM is included for the preparation of compound (I).
NOVELTY - A fracturing fluid crosslinking agent comprises 25-50 parts mass trivalent iron salt, 6-25 parts mass complexing agent, 2-8 parts mass crosslinking accelerator, 8-23.3 parts mass alcohol and 26.67-56 parts mass water.    USE - Fracturing fluid crosslinking agent is used for crosslinking dialkyl phosphate in lower hydrocarbon (claimed).    ADVANTAGE - The lower hydrocarbon can be prepared rapidly using fracturing fluid crosslinking agent.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of fracturing fluid crosslinking agent;    (2) use of fracturing fluid crosslinking agent for crosslinking dialkyl phosphate in lower hydrocarbon. The dialkyl phosphate is of formula: PO(OH)(OR1)(OR2). The lower hydrocarbon is propane, butane, pentane, hexane, heptane or octane. The content of crosslinking agent in lower hydrocarbon is 0.5-2 %mass; and    (3) preparation of dialkyl phosphate-crosslinked lower hydrocarbon, which involves adding dialkyl phosphate to lower hydrocarbon, and adding fracturing fluid crosslinking agent.    R1,R2=linear 2-12C hydrocarbyl.
NOVELTY - Producing biomass fuel gas comprises crushing, gasification, dust-removing, cooling, and purifying by using tar catalytic cracking process.    USE - The (claimed).    ADVANTAGE - The method: has high yield; causes no secondary pollution; and is suitable for large scale production.
NOVELTY - Coal-bed methane deoxidizer comprises 5-15 wt.% active component and balance amount of carrier. The active component is sulfides. The carrier is active carbon, sodium-yttrium molecule sieve or alumina.    USE - Coal-bed methane deoxidizer.    ADVANTAGE - The coal-bed methane deoxidizer is cost-effective and ensures high oxygen removing rate and high deoxidizing activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing coal-bed methane deoxidizer, which involves using active component and carrier.
NOVELTY - Machine-made charcoal comprises 40-50 pts. Chinese herbal medicinal residue, 2-5 pts. combustion improver, 35-52 pts. biomass waste and 6-10 pts. adhesive. The Chinese herbal medicinal residue includes 60-65 pts. wormwood, 10-15 pts. lavender bellflower, 4-6 pts. dried orange peel, 2-4 pts. lotus leaf and 10-24 pts. mixture of fructus momordicae and its leaves.    USE - Used as a machine-made charcoal.    ADVANTAGE - The charcoal utilizes waste as raw material, and has a healthcare effect on cough, sore throat and bronchial asthma.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the machine charcoal, comprising: (a) sterilizing the Chinese herbal medicinal residue and biomass waste respectively; (b) drying the Chinese herbal medicinal residue, combustion improver and biomass waste to obtain a moisture content of 30-40%, 2-5% and 20-30% respectively; (c) crushing the dried materials separately; (d) drying again to obtain 8-10% moisture content Chinese herbal medicinal residue, less than 1% moisture content combustion improver and 5-8% moisture content biomass waste; (e) mixing the dried material with adhesive by stirring uniformly, then molding via molding machine; and (f) carrying out carbonization.
NOVELTY - Agricultural waste fuel device comprises a drying tower (1), a pulverizer (2), a hardening and tempering tank (3) and extrusion molding machine (4) that is set at bottom side of the hardening and tempering tank, where feeding port (20) is provided with the drying tower. An exit (22) is formed at bottom of the drying tower.    USE - Agricultural waste fuel device.    ADVANTAGE - The agricultural waste fuel device ensures high combustion efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an agricultural waste fuel device.    Drying tower (1)    Pulverizer (2)    Hardening and tempering tank (3)    Extrusion molding machine (4)    Feeding port (20)    Exit (22)
NOVELTY - Fuel comprises 20-30 wt.% combustion improver, 1-5 wt.% sodium perchlorate, 1-3 wt.% potassium permanganate, 0.1-0.5 wt.% ferrocene, 0.5-1.2 wt.% Tween (RTM: Non-ionic surfactant)-80, 1-5 wt.% ferric nitrate, 0.5-3 wt.% alcohol and 100-200 wt.% water.    USE - Fuel for boiler (claimed).    ADVANTAGE - The fuel is non-toxic, cost-effective and eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fuel, which involves using combustion improver, sodium perchlorate, potassium permanganate, ferrocene, Tween-80, ferric nitrate, alcohol and water.
NOVELTY - Biogas system comprises a feeding pipe (11), a discharging pipe (12), and U type pipe (20). The feeding pipe and discharging pipe are connected to vertical U type pipe. The U type pipe is provided with hydraulic part. The feeding pipe is provided with water discharging hole (32), which is provided with discharging pipe drain hole (30). The U type pipe and feeding pipe are connected to sets of feed tube plate. The discharging pipe is provided with plate discharging pipe, which is provided with air-blocking plate and feeding pipe blocking plate.    USE - Biogas system.    ADVANTAGE - The biogas system distributes bacteria uniformly, and produces biogas at uniform rate, and is suitable for large scale production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biogas system.    Feeding pipe (11)    Discharging pipe (12)    U type pipe (20)    Discharging pipe drain hole (30)    Water discharging hole (32)
NOVELTY - The device has a U-type pipe (20) that is connected with discharge pipe (12) having air-blocking plates. The fermentation areas are provided between blocking plates. The top portion of fermentation area is provided with a gas collecting pipe (40) equipped with a valve. A drain pipe (50) is provided with biogas liquid one-way valve. The feeding tube drainage hole (32) is higher than lowest point in horizontal plane. The water pressure between lowest points at a position of horizontal pipe drain hole is higher than lowest point in horizontal plane.    USE - Curved liquid turbulent flow type methane biogas generating device.    ADVANTAGE - The uniform distribution of strain is obtained, and crusting phenomenon is effectively prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the curved liquid turbulent flow type methane biogas generating device.    Discharge pipe (12)    U-type pipe (20)    Feeding tube drainage hole (32)    Gas collecting pipe (40)    Drain pipe (50)
NOVELTY - Biogas generation system comprises a feeding pipe (11), a discharging pipe (12), and U type pipe (20). The feeding pipe and discharging pipe are connected to vertical U type pipe. The U type pipe is provided with hydraulic part. The feeding pipe is provided with water discharging hole (32), which is provided with discharging pipe drain hole (30). The U type pipe and feeding pipe are connected to sets of feed tube plate. The discharging pipe is provided with plate discharging pipe, which is provided with air-blocking plate and feeding pipe blocking plate.    USE - Biogas generation system.    ADVANTAGE - The biogas generation system distributes bacteria uniformly, and produces biogas at uniform rate, and achieves sufficient flow of biogas in system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biogas generation system.    Feeding pipe (11)    Discharging pipe (12)    U type pipe (20)    Discharging pipe drain hole (30)    Water discharging hole (32)
NOVELTY - The system has fermentation region that is formed between adjacent block plates. The flow of gas in feed pipe (11) and outlet pipe is according to fermentation space and squeeze slurry convection zone. The fermentation in biogas is carried out through discharging pipe drain hole with the rise of liquid level in feeding pipe and discharging pipe (12). The water slurry stored within intermediate-pressure feed pipe is passed back to the fermentation tube through drain hole. The circulation flow liquid is completed according to generation of methane gas and marsh gas.    USE - Ultra-efficient methane fermentation system for producing biogas.    ADVANTAGE - The fermentation efficiency of methane fermentation system is increased effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ultra-efficient methane fermentation system.    Feed pipe (11)    Discharging pipe (12)    Hydraulic portion (30)    Marsh gas collecting pipe (40)    Drain pipe (50)
NOVELTY - Methane generation system comprises a feeding pipe (11), a discharging pipe (12), and U type pipe (20). The feeding pipe and discharging pipe are connected to vertical U type pipe. The U type pipe is provided with hydraulic part. The feeding pipe is provided with water discharging hole (32), which is provided with discharging pipe drain hole (30). The U type pipe and feeding pipe are connected to sets of feed tube plate. The discharging pipe is provided with plate discharging pipe, which is provided with air-blocking plate and feeding pipe blocking plate.    USE - Methane generation system.    ADVANTAGE - The methane generation system distributes bacteria uniformly, and produces biogas at uniform rate, and achieves sufficient flow of biogas in system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a methane generation system.    Feeding pipe (11)    Discharging pipe (12)    U type pipe (20)    Discharging pipe drain hole (30)    Water discharging hole (32)
NOVELTY - The method involves arranging the methane collecting and fermentation area between feeding/discharging pipe (11,12) and adjacent blocking plate. The marsh gas fermentation pipe is configured to pass marsh gas through drain hole (32) into water pressure chamber. The methane storage area is configured to send fermented marsh gas to the neighboring area. The biogas slurry is made to flow in fermentation area from drain hole through feeding pipe for fermentation to generate methane using marsh gas.    USE - Method for generating marsh gas using dragon type sub-ultra efficient cloth of marsh gas fermentation system.    ADVANTAGE - The uniform distribution and effective stirring are achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of marsh gas fermentation system.    Feeding pipe (11)    Discharging pipe (12)    Drain hole (32)    Gas collecting pipe (40)    Drain pipe (50)
NOVELTY - Amphikrikos minutum algae is preserved in China general microbiological culture collection center with preservation number CGMCC NO:9815.    USE - Amphikrikos minutum algae used for producing biological diesel oil (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for culturing Amphikrikos minutum, which involves:    (A) inoculating algae into culture medium and then illuminating culture medium with light; and    (B) culturing algae for 1-3 weeks and then centrifuged to obtain the product.
NOVELTY - Processing waste bark involves soaking waste bark in lime and water for 16-20 days and then crushing to obtain slurry. Cassava starch is added into slurry and then stirred to obtain fermentation material. The fermentation material is fermented for 15-17 days to obtain fermentation liquid. The fermentation liquid is distilled in distillation device and then separated to obtain filter liquid and filter residue. The filter residue is pressed to obtain block materials. The biochemical agent is added into filter liquid and then stirred to obtain marsh gas.    USE - Method for processing waste bark used for preparing fertilizer, marsh gas, animal feed additive and fuel for furnace (claimed).
NOVELTY - Fermenting organic domestic garbage involves crushing organic household garbage and then mixing to obtain mixed garbage. Garden fruit tree leaves are crushed and then composite microorganism is added to obtain mixture. The mixture is fermented for 20-30 days to obtain fermented leaves. The fermented leaves are mixed with garbage to obtain another mixture, where mixture pH value is adjusted to 7.2-7.5. The obtained mixture is fermented at 34-38 degrees C in anaerobic condition to obtain biogas and fertilizer.    USE - Method for fermenting organic domestic garbage used for preparing biogas and fertilizer (claimed).
NOVELTY - This utility new type claims a a novel medical waste processing device, composed of a feeding cabin (1), a feeding cabin (1) in turn has a large storage bin (4), a material pulverizer (6), a material drying machine (7), a conveyor (8), a small storage bin (11) and extrusion molding machine (14), the conveyor (8) is provided with lime tank (17), the extrusion molding machine (14) and side face provided with a multi-conveying mechanism. This utility new type can use medical waste into refuse derived fuel, a medical waste treatment target of harmless, volume reducing, reduction and energy.; this utility new type can reduce the discharge of HCL when a combustion, reduces the concentration of dioxin, thus at the same time increase in energy regeneration value of medical waste, reduce the pollute to environment is.
NOVELTY - Method for energy conversion and fuel generation, involves (a) generating at least a first portion of source waste heat and second portion of source waste heat using fuel consuming heat source, (b) converting energy in the first portion of source waste heat into organic rankine cycle (ORC) power and ORC waste heat using ORC system, and (c) generating heat source fuel using ORC waste heat and heat source fuel generation system including an anaerobic digestion component.    USE - The method, heat coupling apparatus and system are useful for energy conversion and fuel generation (all claimed).    ADVANTAGE - The method is simple, convenient to perform, and cost-effective, and enables to generate power.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) heat coupling apparatus; and    (2) energy conversion and fuel generation system.
NOVELTY - The new type utility claims a solar energy biogas unite heat pump drying system, including by solar energy heat collector, a water tank, a circulation water pump make up the solar energy supply heat system, by marsh gas pool, marsh gas tank, marsh gas internal combustion engine make up a gas supply system, by a compressor, a condensing coil, throttling valve and the evaporator compose the heat pump circulation system, by blower, an exhaust fan, a hot heat exchanger, heating room, auxiliary heating heat exchanger, drying room make up the air circulation system, by auxiliary heating plate pipe and tail pneuma purification device make up the waste heat recovery purification system. The utility model is new type of system for solar energy as heat source, using methane combustion drive compressor circulation supply high warm heat, at the same time taking out drying after the indoor air and enter into the air heat exchanging through a heat recovery heat exchanger, which is good for increase utilization rate of energy. And using the tail pneuma purification device absorbing the harmful gas in tail pneuma, finally a tail pneuma, avoids to cause pollute environment.
NOVELTY - A omni-directional zero discharge of a municipal waste treatment system, comprising in sequence a is oxygen negative pressure gas furnace, a condenser, a sprayer, a dryer pneuma storage cabinet, a negative pressure oxygen gas furnace comprises coaxial set outside layer of furnace wall and inner layer furnace wall, the inner layer furnace wall, the bottom of the outer layer furnace wall located on the same one horizontal line, the top of the inner furnace wall is lower than the top part of the outer furnace wall equipped with, between the inner layer furnace wall and outer furnace wall form has discharging channel, the inner wall of internal furnace by the following up in turn distribute a combustion area, reducing area, the bottom period feeding tray and a burning area of contact, the bottom of the top part and reducing area of the contact area, the top of the reducing area by area after gas and gas pipe. The project can at the same time having a relatively more combustible gas, a second generating dioxin, removing slag is easy.
NOVELTY - This utility new type claims a A biomass environment-friendly gasification furnace, a furnace body of the heating furnace is the water jacket structure, the furnace body comprises a furnace chamber, a furnace body set has a water inlet and a water return port, a hearth front side has set with a filler wherein, the hearth is set with the lower part has an ash ash the front side has a push and pull is set with an ash hearth and the ash room between the set has fire grate, the upper part set with smoke has chimney port, the internal chamber has heating water pipe set, a hearth inner wall coating layer has refractory mortar, above the hearth set with pneuma has one ring, the pneuma for ring has set with fire gathering basin, the inner wall of inner refractory hearth set with vent-pipe, the air pipe one end hearth, another end and the bottom of the hearth outside air are connected, the utility model is new type to solve technology problem is: a provide a safe and convenient distribution adequate, heating and cooking effect is good, the biomass to a fuel, reducing fuel cost and environment pollute is environment-friendly gasification furnace.
NOVELTY - Method for producing hydrogen, involves (a) grinding starch containing plant material, (b) inoculating Thermococcus strain into crushed material obtained in step (a), and culturing mixture, and (c) separating hydrogen from the culture and purifying hydrogen.    USE - The method is useful for producing hydrogen (claimed).
NOVELTY - This utility new type relates to a planting organic waste and Anaerobic digestion processing system, belongs to environmental protection device technology field. The processing system in, a crusher, a hydrolysis pool, second pool and hydrolysis and Anaerobic digestion tank connected in turn, a Anaerobic digestion tank at the same time is connected with the biogas pneuma tank, tank and biogas residue tank, solid-liquid separator at the same time connected and crusher and oil water separator, oil water separator, a reaction kettle, a centrifuge and decolouring reactor connected in sequence. The first processing system to only use the gravity concentrated sludge, then using the ultrasonic, microwave or heating to a sludge concentrated after equal physical method, or using acid or adding alkali equal chemistry method, using physical method or chemistry method are combined, carrying out pre-processing, waste oil in a third for kitchen garbage by the esterification treatment process, to a sewage in kitchen garbage by the discharged sewage processing, which not only increase the pre-processing effect and treatment effect, increase the methane yield and also simplify the process, reduce the occupied square meter, reducing cost.
NOVELTY - Catering garbage producing biogas pneuma of reactor, one relates to a biogas production device. This utility new type provide a catering garbage producing biogas a pneuma of reactor, using food waste the pneuma of biogas reactor to realize rational processing of food waste. Catering garbage producing biogas pneuma of reactor by seal reaction tank, the pneuma valve, a flow meter, a pneuma. purification, purification pneuma valve, purification pneuma flow meter, an air storage tank, a temperature control device, the bracket, the rotating shaft, the rotating shaft, temperature detector, an air outlet pipe and purification pneuma tube one. This utility new type with a b Anaerobic biological treatment of food waste.
NOVELTY - This utility new type claims a planting material is continuous over a suction biomass gasification furnace, it solves the problem that the suction type gasification furnace intermittent a current of air open furnace cover stop adding material cause work efficiency is low, pollute environment and labour intensity is large problem. It always use a material packing auger and the gas flow of the inner furnace body is pressed compact is to implement a continuous suction inner discharge nozzle of packing auger is mounted in furnace body upper end. Use in floating state of furnace grate acceptance gravity change and sinking or floating up of displacement driving iron touch electric appliance switch is close or open, so as to stop or a start and a finish the packing of material.
NOVELTY - The utility model relates to a. Anaerobic fermentation tank, belongs to environmental protection device technology field. Comprising a tank body, a stirring device, a baffle plate and heating pipe, tank body set with marsh gas outlet, pressure table, biogas outlet, wherein a feeding circulation wherein. A stirring motor by a top part, stirring shaft and stirring blade make up, the stirring shaft in the tank body center, stirring on a motor output shaft end part of shaft connected, stirring blade mounted at lower end part of stirring shaft, the baffle plate are symmetrically fixed at side wall on the tank body, the heating pipe is set in the tank body bottom. The utility model is new type of Anaerobic fermentation tank, through the tank body baffle plate equipped with a circulation device, a make Anaerobic fermentation raw material mixing is more uniform, more sufficient reaction, increase the reducing and recycling of organic waste, increase the methane yield and raw material use rate and a good economic benefit is, at the same time reduces the organic waste object of pollute.
NOVELTY - Method for cultivating Rubus coreanus involves (a) subjecting dried fish scales initially to pepsin treatment and finally to alkaline treatment to obtain amino acids, (b) mixing obtained fish amino acid, gelatin decomposing enzyme, molasses, and glucose, and fermenting the resulting mixture by inoculating yeast and lactic acid bacteria, (c) diluting the resulting fermentation product to obtain amino acid liquid fertilizer, and (d) cultivating R.coreanus using resulting environmentally-friendly fertilizer.    USE - The method is useful for cultivating R.coreanus using environmentally-friendly amino acid liquid fertilizer (claimed).    DETAILED DESCRIPTION - Method for cultivating Rubus coreanus involves (a) subjecting dried fish scales initially to pepsin treatment and finally to alkaline treatment to obtain amino acids, (b) mixing 40-60 wt.% obtained fish amino acid, 20-40 wt.% gelatin decomposing enzyme, 3-8 wt.% molasses, and 3-8 wt.% glucose, and fermenting the resulting mixture at 24-35 degrees C by inoculating 10-15 wt.% yeast and lactic acid bacteria, (c) diluting the resulting fermentation product to obtain amino acid liquid fertilizer, and (d) cultivating R.coreanus using resulting environmentally-friendly fertilizer.
NOVELTY - Reusing preprocessed waste solution from biomass, comprises (i) preprocessing biomass with first alkaline solution mixture in preprocessing reactor, (ii) separating solid material and waste solvent by adding the solution in solid-liquid separator, (iii) introducing the solid material in a saccharification tank, saccharifying and fermenting, (iv) introducing the separated waste solvent and a second alkaline solution in an alkali concentration regulator for adjusting concentration of waste solvent, and (v) introducing the waste solvent in the preprocessing reactor, and preprocessing.    USE - The method is useful for re-using preprocessed waste solution to produce sugar (claimed) and bio-fuel.    ADVANTAGE - The method is environmentally friendly and economical.
NOVELTY - Reduction of fossil fuel and composable biomass involves gradually expanding rice hull with oil, adding fossil fuel and enzyme, fermenting from the depletion of fossil fuels, controlling the generation of bacteria, frictionizing with non-degradable carbon and component having fermentation activity, evaporating the moisture content of the obtained mixture, and heating.    USE - Reduction of fossil fuel and composable biomass (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly reduction of fossil fuel and composable biomass.
NOVELTY - A biomass comprising lignin in particulate form, solvent mixture containing organic solvent and water, and transition-metal catalyst are mixed to obtain mixture. The mixture is heated to 160 degrees C or more, and lignin is depolymerized at a pressure of less than 50 bar, preferably 35 bar or less, and depolymerized lignin is isolated.    USE - Depolymerization of lignin used for composition for producing fuel (all claimed).    ADVANTAGE - The method enables depolymerization of lignin without using hydrogen at low pressure. Due to the addition of water the method becomes more suitable for large scale production and the risk of explosion is reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) use of composition obtained by depolymerizing lignin in fuel production;    (2) production of fuel, which involves cracking or hydrotreating compounds obtained by depolymerizing lignin in a refinery; and    (3) method of producing phenolic compounds of formula (I).    R1,R2=H, or OCH3;and    R3=(CH2)2CH3, (CH2)3OH, or (CH)2CH3.
NOVELTY - Method for producing chitosan, involves (a) growing a biomass comprising an organic acid-producing, chitosan-containing fungus in an aqueous medium under conditions to obtain a chitosan-reduced biomass and a chitosan-enriched aqueous medium, (b) separating the chitosan-reduced biomass from the chitosan-enriched aqueous medium, and (c) separating the chitosan from the chitosan-enriched aqueous medium.    USE - The method is used for producing chitosan (claimed) which is used in wastewater treatment, agriculture, medical devices, pharmaceuticals, nanotechnology and cosmetics.    ADVANTAGE - The method is cost-effective, consumes less energy, and requires acids and bases in lesser amounts.
NOVELTY - Preparation of environmental-friendly biomass fuel involves taking 67 kg corn straw powder, 10 kg charcoal powder, 5 kg bentonite, 3 kg iron oxide, 5 kg limestone powder and 10 kg animal and plant sludge, adding 15-28% water, mixing and pressing into bar-shaped coal.    USE - Method for preparing environmental-friendly biomass fuel (claimed).    ADVANTAGE - The method has high efficiency, high combustion performance, and high heat value.
NOVELTY - Biomass granule fuel production line comprises conveying device (1), filter device (2), pulverizer (3), screw conveying machine (4), granulating machine (5), and packing machine.    USE - Biomass granule fuel production line.    ADVANTAGE - The production line solves the problem of high energy consumption, and low production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biomass granule fuel production line.    Conveying device (1)    Filter device (2)    Pulverizer (3)    Screw conveying machine (4)    Granulating machine (5)
NOVELTY - Biomass briquettes comprise 30-40 pts. wt. mulberry, 20-30 pts. wt. straw, 25-40 pts. wt. tea seed shell, 2-5 pts. wt. clay and 2-5 pts. wt. binding agent.    USE - Biomass briquettes.    ADVANTAGE - The biomass briquettes are eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biomass briquettes, which involves using mulberry, straw, tea seed shell, clay and binding agent.
NOVELTY - Biomass solid fuel molding machine comprises a machine frame (1) and an upper housing (2). The upper housing is provided with a hopper (4) and an outer molding template (3). The outer molding template is provided with a die forming hole. The upper housing is provided with a middle rod power jar (5). The both ends of the middle rod power jar is provided with a pipe joint (7) and a piston rod extended into the upper housing. The piston rod is extended with a push plate.    USE - Biomass solid fuel molding machine.    ADVANTAGE - The biomass solid fuel molding machine is prepared in cost-effective manner, has simple structure and high working efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass solid fuel molding machine.    Machine frame (1)    Upper housing (2)    Outer molding template (3)    Hopper (4)    Middle rod power jar (5)    Pipe joint (7)
NOVELTY - Improving saline-alkali soil includes adding humic acid fertilizer in saline-alkali soil, adding chemical acidic fertilizer i.e. calcium superphosphate and calcium nitrate, adjusting pH, adding physiological acidic fertilizer i.e. ammonium nitrate and phosphate fertilizer, adding mineral fertilizer, adding water everyday, and fermenting; planting Suaeda salsa, treating, leveling ground, removing stones, gravel, garbage debris and iron, sowing with high potassium permanganate solution, soaking seeds, soaking in water, and adding nitrogen, potassium and potash fertilizer.    USE - Method for improving saline-alkali soil (claimed) used in coastal area.    ADVANTAGE - The method has short transformation time.    DETAILED DESCRIPTION - Improving saline-alkali soil comprises adding 200-240 kg/mu humic acid fertilizer in saline-alkali soil, adding chemical acidic fertilizer i.e. calcium superphosphate and calcium nitrate, adjusting pH, adding physiological acidic fertilizer i.e. ammonium nitrate and phosphate fertilizer, adding 50-100 kg/mu mineral fertilizer, adding 20-30 m3/acre water everyday, and fermenting for 1-2 days; planting Suaeda salsa, treating, leveling ground in early March, removing stones, gravel, garbage debris and iron, sowing with 500 mg/L high potassium permanganate solution, soaking seeds for 20 minutes, soaking in 1500-2000 g/acre water for 4 hours, maintaining moisture for 3-4 days, adding 20 kg/667 m2 nitrogen, phosphorus and potash fertilizer, and controlling aphid, and spreading S. salsa in early August containing 0.2-0.3 wt.% salt content.
NOVELTY - Treatment of medical waste comprises sorting hard object and non-combustible object in medical waste, crushing to granularity of less than 40-70 mm, crushing to granularity of 18 mm, drying to water content of 15-20%, adding 1-5% lime, and extrusion-molding to obtain refuse-derived fuel.    USE - Method for treating medical waste used for producing refuse-derived fuel (claimed).    ADVANTAGE - The method reduces harm, volume, energy, hydrochloride discharge, dioxin concentration and environmental pollution, and increases energy regeneration value of medical waste. It achieves complete disinfecting and sterilizing.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for medical waste treatment device comprising feeding cabin (1), large storage bin (4), material crusher (6), material drying machine (7), conveyor (8), small storage bin (11), extrusion-molding machine (14) and lime tank (17).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of medical waste treatment device.    Feeding cabin (1)    Large storage bin (4)    Material crusher (6)    Material drying machine (7)    Conveyor (8)    Small storage bin (11)    Extrusion-molding machine (14)    Lime tank (17)
NOVELTY - Anaerobic tubular membrane bioreactor comprises an acid-producing reactor (1), circulation pump (4) and a mixing type methanogenic reactor (2). The circulation pump is connected with a tube-type film component (3). A water port of tube type film component is connected with producing port. The acid-producing reactor is connected with the mixing type methanogenic reactor. The mixing type methanogenic reactor is equipped with a pH electrode and an electric conductivity electrode. The pH electrode and electric conductivity electrode are connected with reactor control system.    USE - Anaerobic tubular membrane bioreactor used for treating low and high concentration organic wastewater.    ADVANTAGE - The anaerobic tubular membrane bioreactor reduces the dissolved methane as a greenhouse gas emissions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for treating organic wastewater, which involves:    (A) connecting acid-producing reactor and mixing type methanogenic reactor with anaerobic sludge digestion;    (B) conveying organic wastewater to acid-producing reactor and then entering the organic wastewater into mixing type methanogenic reactor;    (C) entering the organic wastewater into tube type film component and then stirring the obtained material in a circulation reactor; and    (D) separating the obtained material to obtain produced water and methane gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an anaerobic tubular membrane bioreactor.    Acid-producing reactor (1)    Mixing type methanogenic reactor (2)    Tube-type film component (3)    Circulation pump (4)    Water outlet (7)
NOVELTY - Sludge anaerobic digestion device comprises a continuous stirring acid producing reactor and a microorganism flow producing methane reactor (2), an air outlet B (23), a three phase separator (22), a liquid outlet B (24), a reactor main body (32), a micropore distribution plate, a slag-drip opening (30), a liquid inlet B and a pedestal (31). The pedestal is provided with outside surface of reactor main body. The reactor main body is provided with a cathode and an electric source.    USE - Sludge anaerobic digestion device used for performing sludge anaerobic digestion method (claimed).    ADVANTAGE - The sludge anaerobic digestion device greatly shortens the operation period of sludge anaerobic digestion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for performing sludge anaerobic digestion, which involves:    (A) starting microbial electrolysis cell catalysis and then utilizing anode nutrient solution as a substrate;    (B) adding anode nutrient solution to the reactor of reactor main body and then applying 0.8 Volt external voltage;    (C) adding the sludge into a continuous stirring acid reactor and then fermenting the sludge for 10 days;    (D) entering the fermented material into a mixing type acid generating reactor and then subjecting the obtained sludge for solid-liquid separating centrifuge;    (E) collecting the supernatant and fermentation liquid and then heating the obtained material in a methane producing reactor at 35-37 degrees C; and    (F) adding the obtained material with sodium acetate, monosodium orthophosphate, disodium hydrogen phosphate, ammonium chloride and potassium chloride.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a sludge anaerobic digestion device.    Microorganism flow producing methane reactor (2)    Three phase separator (22)    Air outlet B (23)    Liquid outlet B (24)    Slag-drip opening (30)    Pedestal (31)
NOVELTY - Biogas generation system comprises a feeding pipe (11), a U-shaped pipe (20), a feeding pipe blocking plate, material-blocking plate, a discharge pipe (12) and a marsh gas collecting pipe. The marsh gas is flowed into an inner pipe. The feeding pipe is provided with a discharge hole (40). The lowest position of the discharging pipe drain hole is provided with a water pressure chamber (30). A gas collecting external tube is connected with a storing pipe of marsh gas. The biogas slurry is entered into the discharging pipe drain hole.    USE - Biogas generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biogas generation system.    Feeding pipe (11)    Discharge pipe (12)    U-shaped pipe (20)    Water pressure chamber (30)    Discharge hole (40)
NOVELTY - Preparing organic manure involves mixing dairy manure with 25-30% saw dust and water, where obtained mixture is fermented with 0.5% biological strain for 10 days to obtain product.    USE - Method for preparing organic manure (claimed).    ADVANTAGE - The method enables to prepare organic manure having high quality and good fertilizing effect.
NOVELTY - Composting device comprises mixing system, cooking machine, cooking chamber, sieving machine, granulator, deodorization system and self-control system. The compost material is crushed in mixing system, and then conveyed to cooking machine that is equipped with stirrer, heater, temperature sensor and ventilator. The material inlet is equipped with microwave or ultrasonic water analyzer and weighing device. The composted materials is sent to deodorizing device. The compost material is bark, charcoal, porcelain granule filler, microbial filler, humus and sandy clay.    USE - Composting device used for processing municipal sludge (claimed) and preparing nutrition soil and fertilizer.    ADVANTAGE - The composting device removes odor from municipal sludge, and ensures fast processing.
NOVELTY - Microbial organic fertilizer comprises 80-100 pts. wt. crop residue, 35-45 pts. wt. manure, 0.01-0.03 pts. wt. fermentation bacteria and 0.1-0.3 pts. wt. anti-caking agents.    USE - Microbial organic fertilizer.    ADVANTAGE - The microbial organic fertilizer promotes early growth of crops, increases quality of crop, improves soil structure and increases soil sustainable yield capacity, and ensures high fertilizer utilization rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing microbial organic fertilizer, which involves:    (A) fermenting livestock manure, crop straw and fermentation bacteria mixture in tank at 80 plus minus 5 degrees C for 3 hours;    (B) stirring fermented materials for 3-6 days;    (C) granulating and drying obtained materials;    (D) cooling and sieving dry granule to obtain microbial organic fertilizer; and    (E) coating obtained product with anti-caking agent.
NOVELTY - Slow release fertilizer comprises 12-18 parts acrylic acid, 10-15 parts 30% of potassium hydroxide solution, 10-15 parts urea, 3-5 parts diammonium phosphate, 1-5 parts potassium fulvate, 5-15 parts potassium sulfate, 0-5 parts potassium chloride, 1.5-2.0 parts sodium carboxymethyl starch, 0.1-0.2 parts initiator and 0.1-0.2 parts crosslinking agent.    USE - Slow release fertilizer used for planting sweet potato (claimed).    ADVANTAGE - The slow release fertilizer is prepared in a simple manner, and eco-friendly, and has improved water holding capacity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing slow release fertilizer, which involves:    (A) adding acrylic acid with water after in a reaction kettle, and then condensing with a condensing device;    (B) adding 30% of potassium hydroxide solution to carry out neutralization reaction and mixing and stirring urea and diammonium phosphate at 60-62 degrees C;    (C) adding sodium carboxymethyl starch and crosslinking agent to carry out polymerization reaction at 70-75 degrees C;    (D) mixing remaining components with the product to obtain gel; and    (E) drying the gel, and then crushing it.
NOVELTY - Organic fertilizer comprises 700kg fresh chicken manure, 200kg plant ash, 100kg bentonite, 50kg pig bone dry powder, 50kg glutinous rice flour, 40kg meliae cortex, 60kg bagasse, 60kg peanut shell, 50kg dandelion, 30kg Chinese prickly ash, 20kg pumpkin, 20kg rose flower, 30kg dry Enteromorpha, 100kg Capsella bursa-pastoris and 200kg water. Organic fertilizer is prepared by mixing raw materials at normal temperature and normal pressure, and then fermentation is carried out for 5-10 days. The fermented product is ground, stirred, granulated and dried.    USE - Organic fertilizer used for planting (claimed).    ADVANTAGE - The organic fertilizer reduces physiological diseases of seedling.    DETAILED DESCRIPTION - Organic fertilizer comprises 700kg fresh chicken manure, 200kg plant ash, 100kg bentonite, 50kg pig bone dry powder, 50kg glutinous rice flour, 40kg meliae cortex, 60kg bagasse, 60kg peanut shell, 50kg dandelion, 30kg Chinese prickly ash, 20kg pumpkin, 20kg rose flower, 30kg dry Enteromorpha, 100kg Capsella bursa-pastoris and 200kg water. Organic fertilizer is prepared by mixing raw materials at normal temperature and normal pressure, and then fermentation is carried out for 5-10 days. The fermented product is ground, stirred, granulated and dried to obtain granules with diameter of 5 millimeter having water content less than 4%. Granules are cooled and then packaged.
NOVELTY - Microbial fertilizer comprises 20-45 pts. wt. straw, 15-20 pts. wt. bagasse, 10-20 pts. wt. furfural slag, 5-15 pts. wt. rice husk, 10-20 pts. wt. peat, 5-10 pts. wt. micro-organism, 10-15 pts. wt. calcium superphosphate, 8-12 pts. wt. urea and 5-10 pts. wt. potassium sulfate.    USE - Microbial fertilizer.    ADVANTAGE - The fertilizer restrains soil-borne disease, and ensures soil modifying effect, improved soil structure, nutrient loss, long-acting fertilizer effect, increased quality, low cost preparation, no residue, no pollution and good popularization and application prospect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing microbial fertilizer, which involves:    (A) crushing and sieving straw, bagasse, furfural slag and rice husk using pulverizer and 80-100 meshes sieve to obtain mixed powder;    (B) fermenting one half of mixed powder in fermentation tank at 70-80 degrees C with water;    (C) cooling fermented materials to 25-30 degrees C;    (D) keeping obtained material at 30-40 degrees C for 30-40 hours to obtain liquid;    (E) mixing other half mixed powder with fermented liquid, calcium superphosphate, urea and potassium sulfate to obtain mixture; and    (F) pelletizing obtained mixture to obtain product.
NOVELTY - Saline alkali modifying agent comprises 18-22 wt.% carbon and silicon anionic solution, 19-21 wt.% organic matter, 46-52 wt.% nutrient source and 8-12 wt.% biological bacteria, and is prepared by mixing raw materials in stainless steel automatic mixer at room temperature for 1 hours to obtain product that is packed in plastic bag. The packaged bag is stored in shade at constant temperature.    USE - Saline alkali modifying agent.    ADVANTAGE - The saline alkali modifying agent promotes plant root activity and neutralizes acidic soil, and ensures biological flora soil restoration, improved soil and increased photosynthetic effect and plant vitality.
NOVELTY - Preparing soil conditioning agent involves utilizing 18-22 wt.% nano-carbon-silicon material, 19-21 organic matter, 46-52 nutrient source and 8-12 biological matter. Nano-carbon-silicon material, nutrient source and biological matter are mixed and stirred through stainless steel automatic stirrer. The mixture is subjected to aluminum packaging, and then storage at constant temperature or cool place.    USE - Method for preparing soil conditioning agent for planting (claimed).    ADVANTAGE - The method enables to prepare soil conditioning agent that increases photosynthetic effect, promotes activation of plant root and soil activity, and improve plant vitality.
NOVELTY - Extraction of ethyl linolenate from blackberry seed oil comprises mixing blackberry seed oil, ethanol and ethanol sodium at mass ratio of 1:0.6-0.8:0.01-0.03, adding into extraction vessel, and extracting to 45-55 degrees C at 25-35 MPa for 1.5-2.5 hours; adjusting extraction device temperature to 30-50 degrees C and distillation temperature gradient to 40-85 degrees C; adjusting extraction pressure to 20-35 MPa and distillation pressure to 10-18 MPa, and discharging extract; and adding into ultrasonic apparatus, and ultrasonically treating to 200-500 W/L extract.    USE - Method for extraction of ethyl linolenate from blackberry seed oil (claimed).    ADVANTAGE - The method achieves high purity ethyl linolenate of up to 92%, and it has reasonable design, easy operation, intensive purification process, simple process, short extraction time, and no harmful residues.
NOVELTY - Biomass carbonization and cooling purification device comprises a bracket (1) and a heat source. The heat source is equipped with the bracket on a carbonization drum (2). The upper part of carbonization drum comprises a thin wall cylindrical stainless steel tube. The stainless steel tube is cooled through a smoke exhaust pipe and the stainless steel tube is connected with carbonization drum and a filtering pipe. A cooling pipe is provided for internal cooling of the device. The cooling pipe is set with a water inlet and a water outlet pipe.    USE - Biomass carbonization and cooling purification device.    ADVANTAGE - The biomass carbonization and cooling purification device is environment friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass carbonization and cooling purification device.    Bracket (1)    Carbonization drum (2)    Heating ring (3)    Layer board (4)    Air inlet (8)
NOVELTY - The system has a suction type fixing bed gasification furnace whose upper part is fixed with a furnace body. An inner part of the furnace body is fixed with a separation plate that is formed with a biomass material layer. A gasification reaction area is matched with a top wall of the furnace body. The furnace body is matched with a biomass feed inlet and a water steam entrance. An inner part of the furnace body is matched with the water steam entrance. An inner part of a gasification reaction area is matched with the biomass material layer.    USE - Biomass gas preparation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gas preparation system.
NOVELTY - The method involves arranging a dual-coal lock feeding device (1) on a gasification room through a dual-channel static cloth coal distribution device (2). A burning layer is filled with carbon dioxide, hydrogen and oxygen gas. A gasification agent entrance (12) is entered into the gasification room. Raw gas (18) is separated by using a gas-liquid separator (11) based on condensation liquid during downstream process. Coal water is separated by using a circulation water pump (10). A high pressure steam (16) is generated by using a waste heat boiler (8) under 200 degree Celsius temperature.    USE - Method for processing coal synthesis gas by using a dry dust coal pressurizing gasification furnace (claimed).    ADVANTAGE - The method enables saving energy and reducing operation cost of a coal dust in a convenient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a dry dust coal pressurizing gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a dry dust coal pressurizing gasification furnace.    Dual-coal lock feeding device (1)    Dual-channel static cloth coal distribution device (2)    Waste heat boiler (8)    Circulation water pump (10)    Gas-liquid separator (11)    Gasification agent entrance (12)    High pressure steam (16)    Raw gas (18)
NOVELTY - The method involves feeding material for a feeding packing auger. The feeding material is provided with a combustion gasification furnace. Bottom of a furnace body (3) is provided with a high pressure blowing part (12). Oxygen and the feeding material are supplied to the combustion gasification furnace so as to increase a contact surface of the material and accelerate the speed. An inner part of the combustion gasification furnace is made to enter into an inner part of a burner (1) by a quadratic combustion process. The body is formed with a layer of a high temperature water jacket (8).    USE - Biomass gasification heat storage method.    ADVANTAGE - The method enables performing biomass gasification heat storage process with high process efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasification heat storage device.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a biomass gasification heat storage device.    Burner (1)    Furnace body (3)    High temperature water jacket (8)    High pressure blowing part (12)
NOVELTY - Biological diesel comprises 55-65 pts. wt. diesel oil, 35-40 pts. wt. methyl ester and 1-5 pts. wt. composite additives.    USE - Biological diesel.    ADVANTAGE - The biological diesel is prepared in a simple and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biological diesel, which involves:    (A) refining biomass refined oil in a reaction vessel with a strong acid cation exchange resin aluminum chloride catalyst; and    (B) converting fatty acid methyl ester into biological diesel in presence of lower alcohol.
NOVELTY - Raw material for blast furnace comprises not less than 60 wt.% fixed carbon as semi-coke raw material and bonding agent, where bonding agent is used for bonding semi-coke raw material.    USE - Raw material for blast furnace used for burning lime (claimed).    ADVANTAGE - The raw material for blast furnace is cost-effective, replaces block coal.
NOVELTY - Producing biomass fuel involves utilizing 40-60 pts. wt. wood shoulder, 20-30 pts. wt. wheat straw and 20-30 pts. wt. rice straw and then pulverizing the wheat straw and rice straw. The wood shoulder is sieved and then the pulverized material is crushed. The crushed material is mixed with the sieved material and then the mixed material is heated in a microwave heating device for controlling the moisture content. The heated material is pressed into a pressing forming device to obtain the desired product.    USE - Method for producing biomass fuel (claimed).    ADVANTAGE - The method enables to produce biomass fuel in cost-effective manner, with high efficiency, and improved the degree of pressing forming.
NOVELTY - Composite additive comprises active component and additive material, where the active component comprises aluminum oxide, kaolin and ammonium sulfate, and the mass ratio of aluminum oxide, kaolin and ammonium sulfate is 10-25:40-60:20-35.    USE - Composite additive used in biomass combustion process for inhibiting alkali metal vapor migration (claimed).    ADVANTAGE - The composite additive is prepared in simple and cost-effective manner, and solves the biomass boiler furnace inner coke slag and coke thermal efficiency problem.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for inhibiting alkali metal vapor migration in biomass combustion process, which involves:    (A) mixing aluminum oxide, kaolin and ammonium sulfate and then grinding the mixed material to obtain a mixture A;    (B) adding water to the ground material and then mixing to obtain the mixture B; and    (C) adding mixture B in a granulator for granulating under normal temperature.
NOVELTY - Rural biogas digester comprises a pool wall (1), a pool arc (2), a feeding pipe (3), a discharging pipe, an air guide pipe (4) and water pressure room (5). The pool wall and pool arc are made of glass material, where glass material is toughened glass.    USE - Rural biogas digester.    ADVANTAGE - The rural biogas digester enables to generate biogas efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a rural biogas digester.    Pool wall (1)    Pool arc (2)    Feeding pipe (3)    Air guide pipe (4)    Water pressure room (5)
NOVELTY - Device comprises a feeding pipe (10), a discharging pipe (20), a fermentation pipeline (30), and a hydraulic pipeline (40), which is straight pipe that is provided with an opening. Feeding pipe and discharging pipe are extended to fermentation pipeline. The feeding pipe is provided with drain pipe (42) and water pressure discharge tube. The water pressure discharge tube is provided with sets of horizontal discharge tube. The feeding pipe side wall, discharge tube side wall and blocking plate forms fermentation area. The fermentation area is connected with gas-guide tube.    USE - Device used for producing biogas (claimed).    ADVANTAGE - The device increases production rate of biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biogas production device.    Feeding pipe (10)    Discharging pipe (20)    Fermentation pipeline (30)    Hydraulic pipeline (40)    Drain pipe (42)
NOVELTY - Producing methane by fermentation involves performing fermentation by utilizing feedstock and microbial strain to produce methane as biogas in the fermentation broth, where the formed methane is passed through adjacent block plates under reduced pressure through pipeline to a methane storage chamber unidirectionally. The certain amount of biogas is then recycled into the fermenter to yield methane as the finished product.    USE - Method for producing methane by fermentation (claimed).    ADVANTAGE - The method producing methane by fermentation in an efficient manner.
NOVELTY - Fermentation system comprises a feeding pipe (10), a discharging pipe (20), a fermentation pipeline (30), and a hydraulic pipeline (40), which is straight pipe that is provided with an opening. Feeding pipe and discharging pipe are extended to fermentation pipeline. The feeding pipe is provided with drain pipe (42) and water pressure discharge tube. The water pressure discharge tube is provided with sets of horizontal discharge tube. The feeding pipe side wall, discharge tube side wall and blocking plate forms fermentation area. The fermentation area is connected with gas-guide tube.    USE - Fermentation system used for producing methane (claimed).    ADVANTAGE - The fermentation system increases production rate of methane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a methane production fermentation system.    Feeding pipe (10)    Discharging pipe (20)    Fermentation pipeline (30)    Hydraulic pipeline (40)    Drain pipe (42)
NOVELTY - Preparing biodiesel involves crushing Paulownia, radix scrophulariae, dogwoods, Flacourtiaceae, Alopecurus aequalis, oleander, pineapple, Euphorbiaceae, Lauraceae, Moraceae and woody plant to obtain pulp. Microorganism is added into mixture and then fermented to obtain low molecular alcohol and mixture of esters. Low molecular alcohol and mixture of esters are distilled to obtain the product.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method enables to prepare biodiesel in a cost-effective manner.
NOVELTY - Energy storage device comprises hydrogen making device (1), electric power system (13), first condenser (2), gas mixer (3), hydrogen storage tank (4) and steam generator (5). The hydrogen storage tank is provided with a condenser. The water entrance is connected with a steam generator. The power generating system comprises combustion room, gas turbine, waste heat boiler, steam turbine, first generator, second condenser and second generator.    USE - Energy storage device.    ADVANTAGE - The energy storage device is cost-effective and efficient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for storing energy, which involves:    (A) loading electric power;    (B) providing oxygen carrier body;    (C) introducing electric energy in electrolysis water hydrogen making device; and    (D) providing redox reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an energy storage device.    Hydrogen making device (1)    First condenser (2)    Gas mixer (3)    Hydrogen storage tank (4)    Steam generator (5)    Electric power system (13)
NOVELTY - Method for preparing fertilizer rich in amino acids, involves (a) milling seafood by-products using grinder, (b) performing enzymolysis of milled product using protease, and (c) performing fermentation of enzymolysis product using microorganism.    USE - The method is useful for preparing fertilizer rich in amino acids (claimed).    ADVANTAGE - The method is rapid and environmentally-friendly, and reduces bad smell of fertilizer.
NOVELTY - A modified activated sludge powder is obtained by mixing humus substance and clay powder with organic material.    USE - Modified activated sludge powder/liquid is used for treating sewage and producing processed water used for sterilization composition, deodorization composition, composition for accelerating growth of plant, and composition for removing heavy metal from heavy metal-contaminated soil (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) modified activated sludge liquid, which is obtained by mixing modified activated sludge powder and clay powder with organic material; and    (2) sewage treatment.
NOVELTY - The portable prefabricated anaerobic septic tank has a digester (1) that is provided with water jacket walls (2,3) in the top portion. A gas collector (4) is provided with an in-built lock system (6) to lock the gas collector in the digester of the anaerobic septic tank main portion.    USE - Portable prefabricated anaerobic septic tank installed in house for processing human excreta and generating biogas or bio energy.    ADVANTAGE - The in-built lock system in the water jacket portion of the digester and gas collector is made unique and cost effective to lock the gas collector in the digester without any external lock. The anaerobic septic tank is provided as a unique device for treating human excreta hygienically without any environmental issues. The in-built lock system in the water jacket portion of the digester and gas collector is provided to keep the digester in anaerobic condition and to prevent the leakage of biogas from the digester to the atmosphere. The compact and cylindrical shape anaerobic septic tank is user friendly and cost effective. The partition wall in the digester is provided to improve the retention time of the solid materials inside the digester. The projections in the digester are made to provide more strength.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the anaerobic septic tank.    Digester (1)    Water jacket walls (2,3)    Gas collector (4)    In-built lock system (5,6)    Partition wall (9)
NOVELTY - The system has a fluid bed reactor (100) which is provided with a gas distribution plate (110). A heater (300) is set for heating up the gas inside and outside of the fluid bed reactor provided for the biomass rapid thermal decomposition. A biomass feeder (200) is arranged at one side of the fluid bed reactor, to supply the biomass. A vent (400) is installed at upper side of the fluid bed reactor. A heat exchanger (600) is set for condensing the bio oil in a cyclone unit (500) at which cracking gas is removed. A oil discharge pipe is connected with an injection nozzle and a pump.    USE - Bio oil production system.    ADVANTAGE - The shape of the fluid bed reactor is optimized to increase the conversion ratio of the generated gas in the pyrolysis and to increase the productivity of the bio oil. The condensed water rate is enhanced in the bio oil production system. The need of electric dust collector in the bio oil production system is avoided, since filter is installed in the main portion of the heat exchanger. The installation cost and the operating cost of the bio oil production system are reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a bio oil production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the bio oil production system.    Fluid bed reactor (100)    Gas distribution plate (110)    Biomass feeder (200)    Heater (300)    Vent (400)    Cyclone unit (500)    Heat exchanger (600)
NOVELTY - Extracting saccharides, comprises (a) exposing radiation on biomass for changing molecular structure, and (b) mixing the biomass with N-methylmorpholine N-oxide mixed solvent to increase reaction area of the biomass, and swelling the biomass.    USE - The method is useful for extracting saccharides (claimed).    ADVANTAGE - The method improves yield of sugars from the biomass.
NOVELTY - The apparatus has a feeding mixture inlet port (60) which is connected to a mixer (50) for providing mixture which includes liquid metal. The dissimilar liquid metal is segmented with different catalysts and is provided with different specific gravities. A catalyst regenerator (40) is configured to reproduce the catalyst which is separated from liquid metal is collected in furnace (10) from circulation pump (30) by separator. The mixer is arranged for mixing the catalyst reproduced in catalyst regenerator with the different liquid metal and is connected to furnace.    USE - Pyrolysis and gasifier apparatus for biomass gasification system.    ADVANTAGE - The mixer is arranged for mixing catalyst reproduced in catalyst regenerator with liquid metal having different specific gravities and connected to furnace, so that the biomass gasification reaction is efficient.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of pyrolysis and gasifier apparatus.    Furnace (10)    Circulation pump (30)    Catalyst regenerator (40)    Mixer (50)    Feeding mixture inlet port (60)
NOVELTY - Invention relates to a method of deep processing of wood sawdust and leaves without chemical cementing components, characterized by that they are sieved for removal of large-size elements, loaded into a dryer for decrease of humidity down to 10%, crushed until obtaining of a mix of particles with the size less than 15 mm and the volume no more than 0.5-1.0 cm3, formed, pressed at the pressure 120-140 kg/cm2 and the temperature 250-350 degrees C without air access. The invention describes also the briquette obtained by the named method.    USE - Wood working industry.    ADVANTAGE - Obtaining robust briquettes from wood sawdust and leaves, without using the chemical cementing components.5 cl, 8 ex
NOVELTY - An organic composite waste fuel manufacturing method involves metering 80 vol.% wood chips and 18-48 vol.% lignin, and maintaining moisture content of the wood chips and lignin to 12%. The metered chips are fed into a conditioner comprising 98% raw material mixture. 2 wt.% glycerin in form of pellets or briquettes is added with mixture of sawdust and lignin. The mixture is homogenized in a mixer for 4 minutes and homogenizer is added at pressure of 6-8 bars. The mixture is pressed under pressure of 400 bar for and cooled to obtain a finished product.    USE - Method for manufacturing organic composite waste fuel.
NOVELTY - The method involves injecting fracturing waste in which dehydration is made. The fracturing waste in which anaerobic digestion is comprised is dehydrated. The electricity is produced through generation of electricity produced using fuel and biomass. The organic waste is transferred from waste pit in which waste is stored. A crusher crushes the waste to crushing unit in anaerobic digestion unit. The biogas is produced in aerobic fermentation tank. The fracturing waste is dried through aerobic fermentation drying process with aerobic fermentation in electricity production process.    USE - Organic waste energization method.    ADVANTAGE - The organic waste is processed in MBT mode. The energy consumption of organic waste energization system is reduced effectively. The production cost of organic waste energization system is reduced efficiently. The amount of waste is reduced through stabilization of organic waste, such that environmental contamination is minimized effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic waste energization system.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the organic waste energization method. (Drawing includes non-English language text)
NOVELTY - Manufacture of grass briquet involves harvesting grass, naturally drying or hot-air drying to moisture content of 3-7%, cutting to length of 0.1-2 cm, mixing 75-85 wt.% obtained product, 8-10 wt.% seeds, 2-4 wt.% carbonized charcoal powder, 2-4 wt.% anthracite, 1-3 wt.% yellow soil powder and 2-4 wt.% oil sludge, compression-molding in a mold, and naturally drying for 1-2 days.    USE - Manufacture of grass briquet (claimed).    ADVANTAGE - The method enables environmentally-friendly and economical manufacture of grass briquette.
NOVELTY - The method involves providing cyanogen chloride and sulfur trioxide raw material into pipe-type reactor (1) at preset molar ratio. The material tubular product is entered to decomposing reactor (2) and crude product separating device (3) for separating crude chlorosulfonic isocyanate and by-product impurities. The stripping and refining of chlorosulfonyl isocyanate are performed in chlorosulfonic isocyanate purifying tower (4) to obtain finished product. The non-conversion raw material is entered into purifying tower for distillation and to separating device for removing impurities.    USE - Method for preparing chlorosulfonyl isocyanate used as chemical intermediate, medicine, pesticide, fiber and resin modifier from cyanide chloride and sulfur trioxide.    ADVANTAGE - The product quality is high and preparation process is stable and easy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of pipe-type reactor. (Drawing includes non-English language text)    Pipe-type reactor (1)    Decomposing reactor (2)    Crude product separating device (3)    Chlorosulfonic isocyanate purifying tower (4)    Dispersion diluting pipe (5)
NOVELTY - The treating apparatus has porosity rounded structure (20) and leachate (40) that are evenly dispersed in anaerobic reactor (110). A hydrogen peroxide injection system is set to jet the hydrogen peroxide on solid material (30) through spraying device which is set inside a vibration transfer apparatus (170). The top unit of the anaerobic reactor is selectively supplied with the leachate through leachate feeder (152). A methane gas reservoir (150) is set to collet the generated methane gas (50) from the organic waste (10) in the anaerobic reactor.    USE - Organic waste treating apparatus.    ADVANTAGE - The impediment by the propionic acid and hydrogen is provisionally suppressed. The organic waste treating efficiency is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an organic waste treating method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic waste treating apparatus.    Organic waste (10)    Porosity rounded structure (20)    Solid material (30)    Leachate (40)    Methane gas (50)    Anaerobic reactor (110)    Methane gas reservoir (150)    Leachate feeder (152)    Vibration transfer apparatus (170)
NOVELTY - Producing low carbon high quality screen coal, comprises (a) simultaneously supplying hot air and fresh paste into a drum, rotating the preheated drum in filling condition of paste, and spraying hydrophilic biomass for coating the paste, (b) stirring the paste in the drum, and drying the paste by evaporating volatile components and moisture content using transfer process, (c) impregnating the hydrophilic biomass on the paste surface, and (d) carbonizing the hydrophilic biomass.    USE - The method is useful for producing low carbon high quality screen coal (claimed).    ADVANTAGE - The method improves improves thermal power, heat and quality of the coal, relieves problems of spontaneous combustion, reduces cost for fuel transport, reaffirms reliability and coal industry stability, and is convenient to process and environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for low carbon high quality screen coal producing device comprising a paste supply unit (110), a heating unit (140) for providing hot air, an injection unit (130) for ejecting the liquid biomass, and a mixing unit (120) for coating and impregnating the biomass on the paste surface, drying the moisture and volatile matter contained in the paste, stirring the paste by moving a buckets, provided into the rotational drum which receives paste, biomass and hot air via the supply unit, heating unit and injection unit.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the low carbon high quality screen coal producing device (Drawing includes non-English language text).    Supply unit (110)    Mixing unit (120)    Injection unit (130)    Heating unit (140)    Blower (141)
NOVELTY - Biocompost obtaining method includes adding to compost-containing substratum of the rain compost worm Eisenia foetida, and the substratum is obtained by mixing of the decomposed poultry dung with cattle manure in the ratio 1: (1.8-2.2) by volume with addition of an organic filler amounting 30-40% of substratum volume.    USE - Agriculture.    ADVANTAGE - Invention allows to increase intensity of processing of waste and to obtain valuable fertiliser from organic waste with the smallest expenses for processing of manure and dung and the maximum effect connected with increase of yield of ready biocompost from the substratum.3 cl, 2 tbl
NOVELTY - Organic or inorganic fertilizer comprises 250-290 pts. wt. carbamide, 115-160 pts. wt. ammonium phosphate, 140-160 pts. wt. potassium sulfate, 370 pts. wt. organic manure and 120 pts. wt. filler.    USE - As organic or inorganic fertilizer.    ADVANTAGE - The application amount of the fertilizer is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic or inorganic fertilizer, which involves (a) mixing dairy manure with saw dust, and adding water to obtained mixture, and (b) stacking the mixture for 10 days, and fermenting the mixture using biological strains.
NOVELTY - An organic fertilizer comprises 40-60 pts. wt. straw, 15-25 pts. wt. goose droppings, 5-15 pts. wt. cow dung, 5-15 pts. wt. sheep manure, 15-25 pts. wt. donkey bone meal, 20-40 pts. wt. rapeseed cake, 10-15 pts. wt. peanut cake, 20-30 pts. wt. trace elements and 10-20 pts. wt. composite probiotic bacteria.    USE - Organic fertilizer is used for redwood.    ADVANTAGE - The organic fertilizer has high nutritive value for regulating soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of organic fertilizer.
NOVELTY - Turning machine comprises housing unit, punching plate, and wind duct, where the housing unit is provided with spring seat fixed to perforated plate vibrating feeder, vibration motor, discharge port.    USE - The turning machine is useful for preparing bioorganic fertilizer (claimed).    ADVANTAGE - The turning machine is cost-effective and easy to operate.
NOVELTY - Producing bio-coal comprises (a) producing pulverized coal and pulverized marine algae raw material, (b) introducing the raw material in a microwave and drying for predetermined time, (c) introducing coal in the microwave during mixing the raw material, and blending to form mixed fuel, and (d) introducing the mixture of coal and algae in the microwave at lower energy level than previous level, and simultaneously introducing hot air at more than predetermined temperature.    USE - The method is useful for producing bio-coal (claimed).    ADVANTAGE - The bio-coal is environmentally friendly and economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for bio-coal having modified hydrophobic surface with carbon components coated surface, obtained by the above method.
NOVELTY - The system has a sub-critical water preprocessing apparatus that is comprised with a sub-critical water pretreatment reaction bath. A blade for mixing is mounted in the crankshaft, and a horizontal mixer is directly connected with the shaft of a motor. The motor and crankshaft are equipped in the outer side of the sub-critical water pretreatment reaction bath. A connecting rod is equipped inside the sub-critical water pretreatment reaction bath. The organic waste of the sub-critical water pretreatment reaction bath is stirred in the horizontal direction.    USE - System for treating organic waste matter.    ADVANTAGE - The solubilization rate of the organic waste is improved, and the biogas production is increased. The reaction speed of the anaerobic digestion process is increased, and the efficiency enhancement is ensured. The solubilization rate and the gas generation rate are increased. The construction and management expense about the bi-gas production equipment are reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for treating organic waste matter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for treating organic waste matter. (Drawing includes non-English language text)    Organic waste reservoir (1)    Sub-critical water pre processor (2)    Anaerobic absorption apparatus (4)    Biogas reservoir (5)    Digested sludge reservoir (6)
NOVELTY - Producing biological methane, comprises (a) providing phenol-containing wastewater as substrate into a bottom-up reaction tank, (b) injecting granulated methanogenic anaerobic inoculum into the phenol-containing wastewater, (c) anaerobically culturing phenol-containing wastewater and inoculum mixture at 30-40 degrees C, and (d) recirculating the effluent generated during the anaerobic culture at constant speed.    USE - The method is useful for producing biological methane (claimed).    ADVANTAGE - The method is economical, produces energy resources, utilizes waste product, and decomposes phenol without any pre-treatment process.    DETAILED DESCRIPTION - Producing biological methane, comprises (a) providing phenol-containing wastewater as substrate into a bottom-up reaction tank, (b) injecting granulated methanogenic anaerobic inoculum into the phenol-containing wastewater, (c) anaerobically culturing phenol-containing wastewater and inoculum mixture at 30-40 degrees C, and (d) recirculating the effluent generated during the anaerobic culture at constant speed. The phenol-containing wastewater further comprises lactic acid, acetic acid or methanol as substrate when the organic loading rate by the phenol-containing wastewater exceeds 5 g chemical oxygen demand/l /day. The organic loading rate is adjusted based on the chemical oxygen demand (COD) decomposition rate of the substrate.
NOVELTY - Biomass non-condensable gas utilization system comprises dried biomass raw material, a circulation fluidization bed reactor for producing pyrolysis gas, a gas-solid separator for separating pyrolysis gas and solids, a spray tower for condensing ecological oil cracked gas and a secondary reactor for burning solid matter. The spray tower outlet pipe is provided between air outlet of the air inlet furnace and the circulation fluidization bed reactor.    USE - Biomass non-condensable gas utilization system.    ADVANTAGE - The biomass non-condensable gas utilization system recovers non-condensable gas effectively, and improves recycling of non-condensable gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass non-condensable gas utilization system. (Drawing includes non-English language text).
NOVELTY - Biomass raw materials are added to gasification furnace, pressurized, and high-temperature steamed, to produce raw synthesis gas including hydrogen, carbon monoxide, carbon dioxide and methane. Raw synthesis gas is centrifuged, filtered, gas particles are removed, supplied to fixed bed reactor, and crude syngas, hydrogen sulfide gas and other acid gases are removed. Then, raw synthesis gas is acid-preheated, purified and supplied to methanation reactor and three-stage adiabatic fixed bed reactor, allowed to react in presence of catalyst and natural gas is produced.    USE - Preparation of biomass gas (claimed).    ADVANTAGE - The method efficiently and economically provides biomass gas, by simple process.    DETAILED DESCRIPTION - Biomass raw materials are added to a gasification furnace, pressurized under aerobic conditions, and high-temperature steamed, to produce raw synthesis gas including hydrogen, carbon monoxide, carbon dioxide and methane. The raw synthesis gas is centrifuged, filtered, gas particles are removed, supplied to fixed bed reactor for absorption, and crude syngas, hydrogen sulfide gas and other acid gases are removed. Then, the raw synthesis gas is acid-preheated to 280-360 degrees C, purified and supplied to methanation reactor and three-stage adiabatic fixed bed reactor, and allowed to react in presence of catalyst. Hydrogen is supplied, hydrogen/carbon monoxide ratio is adjusted, reacted for 4-6 hours and natural gas with methane concentration of 95-99% is produced.
NOVELTY - Concentration and separation of methane from low-concentration coal-bed methane involves compressing and purifying low-concentration-methane coal bed, and carrying out primary stage pressure swing absorption-deoxygenation method and secondary stage pressure swing absorption-nitrogen-enrichment method.    USE - Concentration and separation of methane from low-concentration coal-bed methane (claimed).    ADVANTAGE - The method efficiently and economically increased the concentration of methane gas in feed gas from 20-40% to 80-90%.
NOVELTY - An inhibitor is obtained by adding raw material comprising 25-35 wt.% castor oil, 40-50 wt.% naphtha, 15-20 wt.% light solvent oil, 2-3 wt.% penetrating agent, 0.5-1 wt.% biocide (A) and 0.5-1 wt.% biocide (B) to reactor and stirring at 10-20 degrees C and 1 atm for 1.5-2.5 hours. The light solvent oil is 120-type solvent oil, 200-type solvent oil or D40-type solvent oil. The penetrating agent is ethyl silicone or 10#-type white oil. The biocide (A) is chosen from tetrachlorophthalonitrile, A1-type dry film fungicide and B1-type dry film fungicide.    USE - Inhibitor is used for inhibiting moss growth on insulator surface (claimed).    ADVANTAGE - The inhibitor having excellent long-term inhibition with respect to moss growth, is manufactured by simple and environmentally-friendly process.    DETAILED DESCRIPTION - An inhibitor is obtained by adding raw material comprising 25-35 wt.% castor oil, 40-50 wt.% naphtha, 15-20 wt.% light solvent oil, 2-3 wt.% penetrating agent, 0.5-1 wt.% biocide (A) and 0.5-1 wt.% biocide (B) to reactor and stirring at 10-20 degrees C and 1 atm for 1.5-2.5 hour. The light solvent oil is 120-type solvent oil, 200-type solvent oil or D40-type solvent oil. The penetrating agent is ethyl silicone or 10#-type white oil. The biocide (A) is chosen from tetrachlorophthalonitrile, A1-type dry film fungicide and B1-type dry film fungicide. The biocide (B) is chosen from 4,5-dichloro-2-n-octyl-3-thiazolinone and bis(tributyltin)oxide.
NOVELTY - Processing kitchen waste comprises packaging, filtering, crushing and composting.    USE - The method is useful for processing kitchen waste (claimed).    ADVANTAGE - The method is simple, has convenient operation, and is suitable for waste transfer station and residential area.
NOVELTY - Pre-processing sludge compost feed material comprises adding auxiliary material including more than 7% peanut shell into the sludge before composting, stirring to uniformly mix sludge and auxiliary material, increasing ventilation of compost, reducing water content, and optimizing composting effect.    USE - The method is useful for pre-processing sludge compost feed material (claimed).    ADVANTAGE - The method: increases the air permeability of sludge, which overcomes the single sludge composting efficiency difference; ensures that the sludge compost reaches 93%; improves processing efficiency of sludge compost; carries out compost stacking; reduces energy consume; shortens the composting period; and utilizes low cost peanut shell, which increases the engineering practicability and increases compost product nutrient index, thus recycling the product.
NOVELTY - A fertilizer compound is prepared by mixing 65 wt.% dry chicken manure, 15 wt.% mushroom residue, 10 wt.% tobacco powder, 9.9 wt. reed, and 0.1 wt.% feedstock composition, adjusting moisture content to 40-45%, stacking at 60-65 degrees C, composting to obtain organic matter content of 75% containing effective number of viable cells of 30000000/g, and nitrogen-phosphorus-potassium (NPK) content of greater than or equal to 10% at NPK ratio of 4:3:3, adjusting moisture to less than or equal to 25% and pH value to 7, and treating to NPK ratio of 8.5-10.5:4-5:14-16, moisture content of less than or equal to 12%, and trace elements content of greater than or equal to 3%.    USE - Method for preparing fertilizer compound used for watermelon (claimed).
NOVELTY - A manure-based vegetable seedling matrix comprises composting manure, vermiculite, perlite and peat composition.    USE - Manure-based vegetable seedling matrix.    ADVANTAGE - The manure-based vegetable seedling matrix improves manure harmless treatment, improves breeding environment for the aquaculture industry, and promotes comprehensive utilization of manure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of manure-based vegetable seedling matrix comprising: (A) taking fresh livestock and poultry excrement after dehydration to form livestock manure containing 50-60% moisture; (B) stacking fermentation of manure containing 50-60% moisture, and every 3 days, turn polishing, completely stacking to form a complete maturity reached NY525-2012 required standards, where the manure contains 10-30% water content; and (C) mixing the decomposed livestock and poultry excrement, vermiculite, perlite, and peat composition, and stirring uniformly to obtain vegetable seedling matrix.
NOVELTY - A controlled release fertilizer planting system comprises a urea metering and conveying system, a powder metering and conveying system, a liquid measuring and conveying system, a multiple round disc machine (4), a material receiving belt machine (5), a finished product packing device (6), and a computer. The material receiving belt machine is set on the round disc machine. The finished product packing device is set on the material receiving belt machine.    USE - Controlled release fertilizer planting system used in the field of capsule production.    ADVANTAGE - The system saves energy and human resources to improve production efficiency and reduce production costs.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the controlled release fertilizer planting system.    Multiple round disc machine (4)    Material receiving belt machine (5)    Finished product packing device (6)    Heat preservation device (31)    Liquid metering device (32)
NOVELTY - A loquat special fertilizer comprises 26-28 parts mass water lettuce green manure, 21-23 parts mass urea, 16-18 parts mass calcium magnesium phosphate, 13-15 parts mass potassium nitrate, 11-13 parts mass cottonseed cake, 7-9 parts mass yeast fertilizer, 5-7 parts mass forchlorfenuron, 6-8 parts mass composite manure, 4-6 parts mass organic chelated iron, 3-5 parts mass ammonium molybdate, 1-3 parts mass manganese chloride, 4-6 parts mass ammonium humic acid, 2-4 parts mass diatomite and 50-60 parts mass water.    USE - Loquat special fertilizer (claimed).    ADVANTAGE - The loquat special fertilizer is rich in nutrients, improves the quality of loquat fruit, promotes peel strength and toughness of loquat, and has delicate juicy flesh and sweet flavor, and has excellent stress resistance and disease resistance.
NOVELTY - A caraway fertilizer comprises 19-21 pts. wt. ammonium nitrate, 16-18 pts. wt. phosphate fertilizer, 13-15 pts. wt. potassium dihydrogen phosphate, 10-12 pts. wt. Lathyrus sativus green manure, 11-13 pts. wt. rotten duck manure, 7-9 pts. wt. kiln dust, 6-8 pts. wt. potassium nitrate, 4-6 pts. wt. ferrous sulfate, 5-7 pts. wt. copper sulfate, 2-3 pts. wt. growth-promoting agent, 1-3 pts. wt. sodium humate, 1-3 pts. wt. rooting powder, 2-4 pts. wt. strong stem-promoting agent, and 50-70 pts. wt. water.    USE - Caraway fertilizer.    ADVANTAGE - The fertilizer contains balanced nutrition, is capable of promoting sturdy stems, thick leaves and lush plants, and can increase caraway yield and quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the caraway fertilizer, comprising uniformly mixing raw materials, stirring, sealing and then fermenting for 5.5 days.
NOVELTY - A rhizoma arisaematis fertilizer comprises 27-29 pts. wt. ammonium chloride, 24-26 pts. wt. monoammonium phosphate, 21-23 pts. wt. calcium magnesium phosphate, 18-20 pts. wt. cake fertilizer, 15-17 pts. wt. zinc carbonate, 12-14 pts. wt. ammonium phosphate, 10-12 pts. wt. chelated copper, 8-10 pts. wt. manganese oxide, 5-7 pts. wt. silicon, 3-5 pts. wt. Cycocel (RTM: plant growth regulator), 4-6 pts. wt. boron, 2-4 pts. wt. molybdenum trioxide, 1-3 pts. wt. organophosphorus-degrading bacteria, and 40-50 pts. wt. water.    USE - Rhizoma arisaematis fertilizer used for increasing lodging resistance and promoting rhizoma arisaematis stem growth.    ADVANTAGE - The fertilizer is rich in nutrients, has simple preparation, and can increase organic substance content in soil and increase yield of rhizoma arisaematis.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, comprising mixing raw materials, stirring for 10 minutes to obtain mixture, standing the mixture, then sealing and fermenting for 2 days, and drying fermented material and granulating to obtain the fertilizer.
NOVELTY - Preparation of grape fertilizer comprises adding plant straw and animal excrement into pulverizer, crushing to obtain mixed material, adding humic acid, mixing, adding water, grinding into slurry, adding urea, diammonium phosphate, potassium chloride, calcium superphosphate, magnesium sulfate, ferrous sulfate, copper sulfate, zinc sulfate, trace elements and synergistic agent, uniformly mixing, naturally fermenting at room temperature for 50-60 days, drying and granulating to obtain granule fertilizer.    USE - Preparation of grape fertilizer (claimed).    ADVANTAGE - The grape fertilizer has rich nutrients and high utilization rate.    DETAILED DESCRIPTION - Preparation of grape fertilizer comprises adding 10-15 pts. wt. plant straw and 5-10 pts. wt. animal excrement into pulverizer, crushing to obtain mixed material, adding 3-5 pts. wt. humic acid, mixing, adding water, grinding into slurry, adding 10-20 pts. wt. urea, 5-15 pts. wt. diammonium phosphate, 10-20 pts. wt. potassium chloride, 5-8 pts. wt. calcium superphosphate, 1-2 pts. wt. magnesium sulfate, 1-2 pts. wt. ferrous sulfate, 0.5-1 pt. wt. copper sulfate, 0.5-1 pts. wt. zinc sulfate, 2-3 pts. wt. trace elements and 0.1-0.15 pt. wt. synergistic agent, uniformly mixing, naturally fermenting at room temperature for 50-60 days, drying and granulating to obtain granule fertilizer.
NOVELTY - A microbial organic fertilizer comprises 30-50 pts. wt. animal manure, 30-50 pts. wt. rice hull, 10-20 pts. wt. humic acid, 10-30 pts. wt. potassium carbonate, 5-10 pts. wt. chitosan, 10-20 pts. wt. peat, 1-10 pts. wt. polyacrylamide, 10-20 pts. wt. calcium superphosphate, 3-10 pts. wt. urea, and 10-20 pts. wt. composite microbial inoculum.    USE - Microbial organic fertilizer.    ADVANTAGE - The fertilizer is rich in nutrients to greatly improve soil structure, has long fertilizer effect, and can increase crop yield. The preparation method of the fertilizer has short process, low investment and low energy consumption, and does not cause pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the microbial organic fertilizer, comprising:    (A) drying animal manure and rice hull, and then crushing animal manure, rice hull and peat to obtain;    (B) adding composite microbial inoculum, peat powder, rice hull powder, and chitosan together in a fermentation tank, fermenting for 30 hours at 30 degrees C, to obtain composite liquid; and    (C) adding animal excrement powder, the composite liquid, humic acid, potassium carbonate, chitosan, polyacrylamide, calcium superphosphate, and urea, uniformly mixing, drying and pelletizing.
NOVELTY - Foliar fertilizer comprises 80-90 pts. wt. sisal hemp waste, 5-10 pts. wt. composite amino acid, 0.5-1 pts. wt. trace element, 0.1-0.5 pts. wt. agent, 0.1-0.5 pts. wt. water retaining agent and 0.005-0.1 pts. wt. pest repellent agent. The sisal hemp waste is extracted from sisal hemp slag water and then filtered to obtain the sisal hemp waste.    USE - Foliar fertilizer used for promoting growth of folium llicis latifoliae.    ADVANTAGE - The foliar fertilizer is economic and improves yield of folium llicis latifoliae.
NOVELTY - Biological fertilizer comprises 50-60 pts. wt. soybean straw, 25-30 pts. wt. potato straw stick, 14-23 pts. wt. sodium pyrophosphate, 50-65 pts. wt. duck manure, 25-30 pts. wt. shell powder, 13-18 pts. wt. diammonium phosphate, 9-15 pts. wt. manganese hypophosphite, 0.01-0.02 pts. wt. silicate solubilising bacteria, 0.03-0.06 pts. wt. Bacillus cereus, 5-9 pts. wt. humic acid and 0.1-0.3 pts. wt. Verticillium spore powder.    USE - Biological fertilizer used for improving soil plate structure (claimed).    ADVANTAGE - The biological fertilizer enriched in minerals, inhibits lumps formation in soil, and is eco-friendly.
NOVELTY - Microbial fertilizer comprises 300-320 pts. wt. rice straw, 90-120 pts. wt. corn stover, 30-60 pts. wt. bean straw, 50-60 pts. wt. chicken manure, 0.03-0.06 pts. wt. Rhodococcus powder, 0.09-0.2 pts. wt. bun powder, 0.1-0.2 pts. wt. Escherichia coli powder, 0.1-0.2 pts. wt. Bacillus subtilis powder, 15-20 pts. wt. ammonium dihydrogen phosphate, 12-23 pts. wt. calcium biphosphate and 1-2 pts. wt. fungus.    USE - Microbial fertilizer.    ADVANTAGE - The microbial fertilizer is non-toxic and harmless, and ensures no soil compaction, improved soil structure, strong water retention capacity especially for dryland crops supply of nitrogen, phosphorus, potassium and necessary trace elements to crop for long times.
NOVELTY - Compound fertilizer comprises 15-20 pts. wt. ammonium sulfate, 20-30 pts. wt. potassium chloride, 15-20 pts. wt. potassium sulfate, 20-30 pts. wt. monoammonium phosphate, 10-15 pts. wt. diammonium phosphate, 5-12 pts. wt. pre-gelatinized starch, 2-5 pts. wt. Bacillus spore, 15-20 pts. wt. feather powder, 15-20 pts. wt. monosodium glutamate, 25-30 pts. wt. starch, 15-20 pts. wt. sugar, 3-5 pts. wt. tung oil, 6-10 pts. wt. disproportionated rosin, 4-7 pts. wt. lignosulfonate, 2-6 pts. wt. polyvinyl alcohol, 5-8 pts. wt. carboxymethyl cellulose and 10-18 pts. wt. active carbon.    USE - Compound fertilizer used for planting wheat (claimed).    ADVANTAGE - The compound fertilizer improves soil by improving utilization rate of fertilizer.    DETAILED DESCRIPTION - Compound fertilizer comprises 15-20 pts. wt. ammonium sulfate, 20-30 pts. wt. potassium chloride, 15-20 pts. wt. potassium sulfate, 20-30 pts. wt. monoammonium phosphate, 10-15 pts. wt. diammonium phosphate, 5-12 pts. wt. pre-gelatinized starch, 2-5 pts. wt. Bacillus spore, 15-20 pts. wt. feather powder, 15-20 pts. wt. monosodium glutamate, 25-30 pts. wt. starch, 15-20 pts. wt. sugar, 3-5 pts. wt. tung oil, 6-10 pts. wt. disproportionated rosin, 4-7 pts. wt. lignosulfonate, 2-6 pts. wt. polyvinyl alcohol, 5-8 pts. wt. carboxymethyl cellulose, 10-18 pts. wt. active carbon, 15-20 pts. wt. organic carbon, 8-12 pts. wt. kaolin, 10-16 pts. wt. attapulgite powder, 2-5 pts. wt. silicon, 15-20 pts. wt. zeolite powder and 10-15 pts. wt. calcium disodium edetate.
NOVELTY - Composite organic fertilizer comprises 40-50 pts. wt. organic matter raw material, 5-8 pts. wt. humic acid, 6-10 pts. wt. urea, 6-10 pts. wt. calcium carbonate, 5-7 pts. wt. ammonium phosphate, 10-15 pts. wt. potassium chloride, 0.6-1 pts. wt. trace elements and 0.3-0.5 pts. wt. micro-organism.    USE - Composite organic fertilizer used for planting rice (claimed).    ADVANTAGE - The composite organic fertilizer provides nutrients and organic matter for rice growth, and ensures improved soil plate and fertility.
NOVELTY - Oleic acid, phosphotungstic acid catalyst and benzyltriethylammonium chloride are stirred, heated to 60-95 degrees C under supply of oxygen, potassium permanganate and 5-30 %mass hydrogen peroxide solution are further added during heating process and reacted for 1-8 hours. The reaction mixture is provided into separating funnel, such that manganese dioxide-containing aqueous phase and oil phase are separated. Separated aqueous phase is cooled at 0-5 degrees C, precipitated crystals are filter-separated and dried, to obtain solid azelaic acid.    USE - Synthesis of azelaic acid (claimed).    ADVANTAGE - The method enables economical, simple and rapid synthesis of azelaic acid with high productivity by environmentally-friendly process in a short period of time with reduced energy consumption.    DETAILED DESCRIPTION - Oleic acid, phosphotungstic acid catalyst and benzyltriethylammonium chloride are stirred, heated to 60-95 degrees C under supply of oxygen, potassium permanganate and 5-30 %mass hydrogen peroxide solution are further added during heating process and reacted for 1-8 hours. The reaction mixture is provided into separating funnel, such that manganese dioxide-containing aqueous phase and oil phase are separated. Separated aqueous phase is cooled at 0-5 degrees C, precipitated crystals are filter-separated and dried, to obtain solid azelaic acid. The mass ratio of oleic acid, phosphotungstic acid catalyst, benzyltriethylammonium chloride and potassium permanganate is 20-70:2-8:1-5:1-3. The mass ratio of hydrogen peroxide and oleic acid is 10-30:1.
NOVELTY - Preparation of cypermethrin involves adding water to a reactor, stirring, adding sodium cyanide, alkali metal compound or alkaline earth metal compound as acid binder, dissolving, adding solvent, m-alkoxybenzaldehyde and catalyst to the reactor, stirring for 0.5 hour, dripping cypermethrin chloride at 10-25 degrees C for 4-5 hours, reacting for 4-5 hours until the content of m-alkoxybenzaldehyde in the mixture is less than 2%, separating aqueous and oil layer, washing oil layer with water, desolventizing cypermethrin, obtaining cypermethrin as pale yellow oil and discharging aqueous layer.    USE - Preparation of cypermethrin (claimed).    ADVANTAGE - The method enables environmentally-friendly preparation of cypermethrin having high purity with high yield by reducing the use of sodium cyanide.
NOVELTY - 3-Hydroxy-5-androstene-17( beta )-carboxylic acid (I) is dissolved in strong aqueous alkali in dioxane, catalyst is added, sodium hypochlorite solution is dripped and oxidized to obtain (2R,14S,15S)-2,15-dimethyl-5-oxotetracyclo(8.7.0.02,7.011,15)heptadec-7-ene-14-carboxylic acid (II), and pH value is adjusted to 1-2 using acid and heat-refluxed. Reaction mixture is concentrated under normal pressure to recover dioxane, and remainder of reaction mixture is cooled, to obtain 3-carbonyl-4-androstene-17( beta )-carboxylic acid (III).    USE - Synthesis of 3-carbonyl-4-androstene-17( beta )-carboxylic acid.    ADVANTAGE - The method enables simple and economical synthesis of high-purity 3-carbonyl-4-androstene-17( beta )-carboxylic acid with high productivity by environmentally-friendly process with reduced energy consumption.    DETAILED DESCRIPTION - 3-Hydroxy-5-androstene-17( beta )-carboxylic acid of formula (I) is dissolved in strong aqueous alkali in dioxane, catalyst is added, sodium hypochlorite solution is dripped and oxidized to obtain (2R,14S,15S)-2,15-dimethyl-5-oxotetracyclo(8.7.0.02,7.011,15)heptadec-7-ene-14-carboxylic acid of formula (II), and pH value is adjusted to 1-2 using acid and heat-refluxed. Reaction mixture is concentrated under normal pressure to recover dioxane, and remainder of reaction mixture is cooled, to obtain 3-carbonyl-4-androstene-17( beta )-carboxylic acid of formula (III).
NOVELTY - Method for preparing granular fertilizer involves processing composted organic material in a sieved plant and then packed in a vessel. Composted organic material is pumped into autoclave containing nutrient solution by perforated walls. The product is stored in a storage tank, and mineral salt is mixed, and then vacuum dried.    USE - Method for preparing granular fertilizer (claimed).    ADVANTAGE - The method enables to prepare granular fertilizer in a cost-effective manner. Granular fertilizer has sustained release property.
NOVELTY - Percolate treatment involves adjusting pH value at 1.5-5.5 of the obtained percolate, and then adding coagulating agent for coagulation. The formed sludge is separated to form a water phase, which is concentrated.    USE - Method for treating percolate resulting from wastewater of biogas plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an equipment, which includes a container located behind percolate separator.
NOVELTY - Preparation of emulsified fuel involves obtaining bio-oil from biomass material, stirring mixture of liquid fuel including bio-oil and surfactant, emulsifying obtained mixed solution in reactor with stirring at preset temperature and speed, and obtaining emulsion fuel.    USE - Preparation of emulsified fuel (claimed).
NOVELTY - The system has crusher (110) that crushes the food waste flowed into rotary roller and the mixture mixing addition matter to setting size. First drying furnace (170) dries mixture passing the drying pan apparatus (130,160) in mobile history. Second drying furnace (190) supplies the heat used in first drying furnace and dries solid fuel. Compression molding apparatus (180) compression-molds the mixture dried in first drying furnace in the form of solid fuel through thermal transfer furnace (176). The drying pan apparatus dries the mixture passing the crusher temporary.    USE - Solid fuel manufacturing system using wood waste.    ADVANTAGE - The addition matter is dried in the food waste containing many oil after doing the mixing so that the solid fuel production of the high calorie can be possible and energy during mixing can be reduced. The heat used in the first drying can be reused effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a solid fuel manufacturing method using wood waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the solid fuel manufacturing system using wood waste.    Crusher (110)    Drying pan apparatus (130,160)    Drying furnaces (170,190)    Thermal transfer furnace (176)    Compression molding apparatus (180)
NOVELTY - An aromatic engine oil comprises 2-5 pts. wt. metal deactivator, 3-6 pts. wt. amine antioxidant, 6-7 pts. wt. sterile rust inhibitor, 5-6 pts. wt. naphthenic oil, 3-6 pts. wt. fragrance, 2.5-3.5 pts. wt. menthol and 2.5-3.2 pts. wt. methane.    USE - Aromatic engine oil (claimed).    ADVANTAGE - The aromatic engine oil has excellent aroma characteristics.
NOVELTY - Composition: comprises animal feces; plant waste; greater than 10 wt.% of final composition of bentonite; essential macronutrients; essential micronutrients; agricultural sulfur; algae; and effective microorganisms.    USE - The composition is useful as fertilizer for agricultural lands (claimed). No biological data given.    ADVANTAGE - The composition: exhibits increased cation exchange capacity of 80-120%, preferably 100% after 42 days of fermentation (claimed); provides increased yield; provides recycling of agricultural waste and prevents air and soil pollution by avoiding burning of waste that are harmful to the environment and human health; provides sustainable development and green technology; and exhibits synergistic effect and provides easy and fast fermentation without requiring specific equipment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) producing the composition, comprising cutting the animal feces and plant waste into small pieces, preferably with size of 1-2 cm, introducing the animal feces and plant waste into air- and light-tight container and mixing with bentonite and essential micro and macronutrients, humidifying with water to obtain humidity of 20-25% and mixing with algae and effective microorganisms and mixing twice a week for at least three weeks for fermentation, checking the humidity and temperature and spraying water if necessary to maintain humidity of 20-25% and temperature of 40-55 degrees C; and    (2) fertilizing agricultural land, comprising dispersing 5-7 tons of the composition on the land, turning the soil and irrigating the land with water and adding 1-1.5 l of effective microorganisms.
NOVELTY - Composite catalyst calcium-based material and transition metal-containing materials.    USE - The composite catalyst is useful in catalytic gasification of coal.    ADVANTAGE - The composite catalyst exhibits high catalytic efficiency during gasification reaction, and methanation reaction; and facilitates coupling reactions of gasification, transformation and methanation in a gasification furnace, and thus it improves the content of methane in the product gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for loading composite catalyst, comprising loading calcium-based material and transition metal-containing materials on coal particles.
NOVELTY - Preparing biomass fuel using rubbish, comprises (i) transporting rubbish from dispersed point to a rubbish storing area; (ii) automatically or manually transporting rubbish from rubbish storage area to a reaction vessel, and sealing; (iii) introducing steam to reaction vessel, and mechanically controlling change in temperature and pressure over time; (iv) reducing temperature and pressure in reaction vessel, and discharging liquefied water and gas produced during reaction; and (v) conveying carbonized mixture to a filtering device, and filtering non-flammable material of carbonized mixture.    USE - The method is useful for preparing biomass fuel using rubbish (claimed).    ADVANTAGE - The method is environmental friendly, and economical; and produces product with good combustion value, and low emissions.    DETAILED DESCRIPTION - Preparing biomass fuel using rubbish, comprises (i) transporting rubbish from each dispersed point into a rubbish storing area; (ii) automatically or manually transporting rubbish from the rubbish storage area into a reaction vessel, and completely sealing the reaction vessel; (iii) introducing steam into the reaction vessel, and mechanically controlling the change in temperature and pressure over time, to obtain carbonized mixture; (iv) reducing the temperature and pressure in the reaction vessel, and discharging liquefied water and gas produced during the reaction; and (v) conveying carbonized mixture into a filtering device, and filtering the non-flammable material of carbonized mixture, to obtain the final product.
NOVELTY - Microbial fertilizer comprises 10 wt.% organic matter, 25 wt.%, preferably 20 wt.% nitrogen, phosphorus and potassium fertilizer, 20 million/g microorganism, rooting agent, polypeptide, 2 wt.% trace elements, soil activating enzyme and water retaining agent for newly planted eucalyptus and 40 wt.% humic acid, amino acid and organic matter, preferably 10 wt.% humic acid, 3 wt.% amino acid and more tham 40 wt.% organic matter. The trace element is silicon, boron, zinc, manganese, copper and iron. More than 10 wt.% calcium, magnesium and sulfur is present.    USE - Composite microbial fertilizer.    ADVANTAGE - The fertilizer is environment-friendly, improves soil property by 70%, increases soil fertility and biological activity, and it has absorption rate of more than 80%, sugar degree of 2-3 degree, and increased soil nutrient content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer which comprises adding calcium, magnesium and organic matter into first fermentation tank to carry out deodorization treatment, and fermenting to obtain fermentation broth; decomposing organic matter until soft and flexible, adding microorganism, subjecting to harmless treatment, high-temperature fermenting to kill harmful bacteria and eggs, and drying; and mixing remaining raw materials, stirring, adding 10 kg mixture into packaging bags and 25 kg into waterproof bags, and storing into warehouse.
NOVELTY - Preparation of 6-chloronicotinic acid includes dissolving D,L-malic acid in concentrated sulfuric acid at mass ratio of 1.8-2:1 at 110-132 degrees C for 10-16 hours, performing cyclization reaction, cooling, adding water, stirring, filtering, collecting filtrate, adding sodium carbonate, adjusting pH of filtrate, stirring, introducing liquid ammonia in autoclave, performing amination reaction with sodium tungstate catalyst, adjusting pH using inorganic acid, performing crystallization for 10-12 hours, centrifuging, drying crystals under vacuum, and adding triethylamine.    USE - Method for preparing 6-chloronicotinic acid (claimed).    ADVANTAGE - The method has low cost, high economic benefit and wide application prospect.    DETAILED DESCRIPTION - Preparation of 6-chloronicotinic acid involves dissolving D,L-malic acid in concentrated sulfuric acid at mass ratio of 1.8-2:1 at 110-132 degrees C for 10-16 hours, performing cyclization reaction, cooling, adding water, stirring, filtering, collecting filtrate, adding sodium carbonate, adjusting pH of filtrate, stirring, introducing liquid ammonia in autoclave, performing amination reaction with sodium tungstate catalyst, adjusting pH using inorganic acid, performing crystallization for 10-12 hours, centrifuging, drying crystals under vacuum, adding triethylamine, dissolving in 6-hydroxy acid, adding phosphorus oxychloride dropwise and refluxing for 7-8 hours, cooling at 0-4 degrees C, adjusting pH, and performing crystallization for 15-18 hours.
NOVELTY - An ammonia-measuring fertilizer dynamic aerobic composting tank-type device comprises tank body (1), first flow meter (2), gas absorbing mechanism (3), exhaust pump (4), second flow meter (5), gas storage bag, aeration mechanism (15), air inlet (101), air outlet (102), insert bottle (302), drying tank, guide tube, aeration pipe (1501), box cover and compressing pump (1503).    USE - Used for determining ammonia in areobic composting (claimed).    ADVANTAGE - The device has high gas yield measurement accuracy and high reliability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for determination of ammonia in aerobic composting which comprising collecting gas, mixing with compost raw material, flowing into first flow meter, absorbing by absorption liquid, flowing into second flow meter, entering into gas storage bag, performing colorimetric method by Nessler reagent colorimetric method and absorbing by dilute sulfuric acid.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of ammonia-measuring fertilizer dynamic aerobic composting tank-type device.    Tank body (1)    First flow meter (2)    Gas absorbing mechanism (3)    Exhaust pump (4)    Second flow meter (5)    Aeration mechanism (15)    Air inlet (101)    Air outlet (102)    Aeration pipe (1501)    Compressing pump (1503)
NOVELTY - The machine has a feeding waste dumping unit (10) that is provided a deodorization unit, a stirring unit, a control unit (80) and a display unit (90). A heater is installed in the bottom surface of a secondary fermentation tank (40). The cover of an input hole (12a) is installed in an inlet port (12). A fodder and compost vent is installed at lower side of a drying tank (50). The food waste is fermented in the secondary fermentation tank. The shock absorbers (12b,12c') are installed in the upper portion of inlet port to open and close the cover of the input hole.    USE - Industrial production machine for producing feed and compost by recycling food waste generated in dining hall of apartment house, apartment, school dining hall, government office and hotel restaurant.    ADVANTAGE - Since the rapid fermentation degradation is removed, the bad small generation or the environmental contamination generated in the waste disposal is prevented. Hence the consumption of the energy required to the food waste treatment is reduced, and the economical efficiency is improved. Since the simple structured industrial production machine is set up in the installation place easily, the machine is maintained conveniently. Hence the machine is used safely for long term.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the industrial production machine for producing feed and compost by recycling food waste.    Feeding waste dumping unit (10)    Inlet port (12)    Input hole (12a)    Shock absorbers (12b,12c')    Secondary fermentation tank (40)    Drying tank (50)    Control unit (80)    Display unit (90)
NOVELTY - Obtaining antioxidant substances and amino acids from octopus waste, by (a) cleaning octopus waste, crushing, and homogenizing, (b) adding alkaline protease, neutral protease, papain or animal protease, subjecting to solid-liquid separation, and enzymolyzing, and (c) filtering using ultrafiltration membrane, concentrating, filtering using ultrafiltration membrane, subjecting to nanofiltration using nanofiltration membrane, performing gel column chromatography, performing liquid chromatography, and freeze-drying obtained product.    USE - The method is used for obtaining antioxidant substances and amino acids from octopus waste (claimed).    ADVANTAGE - The method is environmentally-friendly.    DETAILED DESCRIPTION - Method for obtaining antioxidant substances and amino acids from octopus waste, involves (a) cleaning octopus waste, crushing, and homogenizing to obtain product having solid-liquid ratio of 1:2.5-25, (b) adding alkaline protease, neutral protease, papain or animal protease, subjecting to solid-liquid separation by suction filtration, filtration using filter or centrifugation, and enzymolyzing at 30-70 degrees C and 4.5-10 pH for 0.25-6 hours, and (c) filtering using ultrafiltration membrane having molecular weight cut-off of 1-10 kDa, concentrating, filtering using ultrafiltration membrane at 0.1-0.4 MPa, where flow rate is 2.5-12.5 l/hour, subjecting to nanofiltration using nanofiltration membrane having molecular weight cut-off of 300-500 Da and operating pressure of 0.5-0.7 MPa, performing gel column chromatography, where filler for gel column chromatography is diethylaminoethyl (DEAE)-75, G75, G50 or G25, performing liquid chromatography, and freeze-drying obtained product at -50 degrees C.
NOVELTY - A Kyprolis intermediate is new.    USE - A Kyprolis intermediate for preparing carfilzomib (claimed).    ADVANTAGE - Process is environment-friendly, and has high yield.    DETAILED DESCRIPTION - A Kyprolis (RTM: Carfilzomib) intermediate of formula (XIII) is new. INDEPENDENT CLAIMS are included for: (1) preparation of Kyprolis intermediate; and (2) preparation of carfilzomib of formula (I) which involves carrying out epoxidation of Kyprolis intermediate using oxidizing agent.
NOVELTY - Preparing carbamate compounds (I), comprises adding sulfonylhydrazone compounds (II), amine compounds (III), a solvent and a base (as promoter) into an autoclave, passing carbon dioxide, and reacting at 50-150 degrees C for 6-72 hours, then cooling to room temperature, releasing carbon dioxide to atmospheric pressure slowly, filtering the reaction solution, evaporating the solvent under reduced pressure to obtain a crude product, and purifying the crude product by column chromatography to obtain final product.    USE - The method is useful for preparing carbamate compounds.    ADVANTAGE - The method: is safe and simple; utilizes cheap and easily available raw material; and is environment-friendly, and suitable for industrial production.    DETAILED DESCRIPTION - Preparing carbamate compounds of formula (I), comprises adding sulfonylhydrazone compounds of formula (II), amine compounds of formula (III), a solvent and a base (as promoter) into an autoclave, passing carbon dioxide, and reacting at 50-150 degrees C for 6-72 hours, then cooling to room temperature, releasing carbon dioxide to atmospheric pressure slowly, filtering the reaction solution, evaporating the solvent under reduced pressure to obtain a crude product, and purifying the crude product by column chromatography to obtain final product.    R1 = Phenyl, biphenyl, p-bromophenyl, p-chlorophenyl, p-iodophenyl, p-tolyl, p-cyanophenyl, p-(trifluoromethyl)phenyl, p-nitrophenyl, o-bromophenyl , m-bromophenyl, 3,4-dichlorophenyl, 1-naphthyl, 2-benzofuranyl, 2-thienyl or 4-pyridyl;    R2 = H, methyl, cyclopropyl or phenyl;    R3, R4 = H, methyl, ethyl, propyl, n-butyl or benzyl;    NHR3R4 = pyrrolidine, piperidine or morpholine; and    R5 = p-tolyl, phenyl, p-methoxyphenyl, 2-naphthyl, p-nitrophenyl, p-bromophenyl, benzyl, methyl or n-butyl.
NOVELTY - The method involves crushing and drying the biomass according to preset metal salt or metal oxide catalyst mass ratio. The catalyst is mixed in biomass and the heating temperature is raised to 500-700 degrees C in microwave pyrolysis reactor to obtain gaseous product and solid product. The rapid cooling of gaseous product to temperature of 5-10 degrees C and the high quality bio-oil is condensed. The soid product is cooled to furnace room temperature and the high yield biomass carbon is obtained.    USE - Microwave catalytic pyrolysis method of biomass for production of biomass carbon.    ADVANTAGE - The simple, efficient and environment-friendly microwave catalytic pyrolysis of biomass is achieved.
NOVELTY - Preparation of 5,6,7,7a-tetrahydro-4H-thieno(3,2-c)pyridin-2-one hydrochloride (I) comprises performing amino protection reaction of 4,5,6,7-tetrahydro-thieno(3,2-c)pyridine (II) with tert-butyl dicarbonate as butyloxycarbonyl (Boc) reagent to obtain Boc-protected thiophene derivative (III), halogenating compound (III) with halogenating agent to obtain Boc-protected halogenated thiophene derivative (IV), alkylating compound (IV) with sodium-reacted lower alcohol to obtain to alkoxy-containing Boc-protected thiophene derivative (V), and performing deprotection reaction.    USE - Used as a prasugrel intermediate..    ADVANTAGE - The simple method has advanced technology, less waste product production, small environmental protection pressure, high yield, and good suitability for industrial production.    DETAILED DESCRIPTION - Preparation of 5,6,7,7a-tetrahydro-4H-thieno(3,2-c)pyridin-2-one hydrochloride of formula (I) comprises performing amino protection reaction of 4,5,6,7-tetrahydro-thieno(3,2-c)pyridine of formula (II) with tert-butyl dicarbonate as butyloxycarbonyl (Boc) reagent in naphthenic solvent to obtain Boc-protected thiophene derivative of formula (III), halogenating compound (III) with halogenating agent to obtain Boc-protected halogenated thiophene derivative of formula (IV), alkylating compound (IV) with sodium-reacted lower alcohol to obtain to alkoxy-containing Boc-protected thiophene derivative of formula (V), and performing deprotection reaction with hydrochloride gas.    X=Cl or Br; and    R=6C alkoxy.
NOVELTY - Production of methane and disposal of carbon dioxide are performed by performing microbiological decomposition of organic matter under increasing pressure in tubular bioreactor divided into spontaneously separating zones, performing anaerobic digestion of organic matter in 1st bioreactor zone (4) under increasing hydrostatic pressure, removing produced methane into methane tank (7), digesting in digestion chamber (8), removing mineral and non-biodegradable constituents in last bioreactor zone (5), removing evolved gaseous carbon dioxide into gas tank, and separating digestate.    USE - Production of methane and disposal of carbon dioxide.    ADVANTAGE - Production of methane and disposal of carbon dioxide has improved bioconversion rate and efficiency, increases methane content in biogas, and reduces carbon dioxide content in biogas, and methane production and carbon dioxide disposal system has simple design and low operating cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for methane production and carbon dioxide disposal system comprising bioreactor containing 1st zone and last bioreactor zone, substrate tank (1), substrate metering pump (2), substrate valve (3), methane tank (7), gas valve (6), and digestion chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of methane production and carbon dioxide disposal system.    Substrate tank (1)    Substrate metering pump (2)    Substrate valve (3)    1st bioreactor zone (4)    Last bioreactor zone (5)    Gas valve (6)    Biogas tank (7)    Digestion chamber (8)
NOVELTY - Method for performing aerobic-anaerobic bioconversion of organic substrates, involves sequentially subjecting substrate to preliminary aeration by contacting the substrate with wet gas, performing aerobic preconditioning treatment of the substrate in direct thermal contact, and performing anaerobic process by contacting the obtained product with jet-ejecting mode, subjecting the aerobic processed substrate to flotation, subjecting suspended substances of the microflora content liquid fraction or solid fraction to anaerobic treatment, and maintaining humidity.    USE - The method is useful for performing aerobic-anaerobic bioconversion of organic substrates (claimed).    DETAILED DESCRIPTION - Method for performing aerobic-anaerobic bioconversion of organic substrates, involves sequentially subjecting substrate to preliminary aeration by contacting the substrate with wet gas, performing aerobic preconditioning treatment of the substrate in direct thermal contact, and performing anaerobic process by contacting the obtained product with jet-ejecting mode, subjecting the aerobic processed substrate to flotation and gravitational separation, subjecting not greater than 300 mg/l suspended substances of the microflora content liquid fraction or solid fraction to anaerobic treatment, blending the obtained mixture, sealing the mixture and maintaining humidity to 85-90%. An INDEPENDENT CLAIM is included for apparatus for performing the above-mentioned method, which comprises coaxial aerobic bioreactor filled with screw partitions and chamber of recirculation, gas current device in its upper portion, aeration device with branch pipe for passing compressed air, aerobic bioreactor connected along flow of substrate within the anaerobic bioreactor, anaerobic bioreactor supplied with branch pipes for withdrawal of biogas, sedimentation section, and gas current device made in form of ejector.
NOVELTY - The utility model claims an environment-friendly, sanitary and saving type meat duck bed feeding house, belonging to the technical field of poultry breeding. The main characteristics of the utility model are as follows: the duck feeding house comprises a bottom inflation fermentation bed, which comprises a fermentation mattress layer and an aeration fermentation system under the mattress; the fermentation mattress layer comprises a surface layer 20 cm of discrete character pad material layer and lower layer 15-20cm of straw layer, the inflation fermentation system comprises an inflation power device and an inflation pipe device connected with the pad layer. The utility model can effectively overcome the problems of fermentation mattress padding plate caused by duck novel biological characteristic, increase the aerobic degradation ability of duck excrement by fermented padding, reduce the discharge of malodorous gas and greenhouse gas, and improve the duck fly aerobic degradation ability; the drinking water and spraying clean device solve the problem that the water is a dry-feeding time and it saves the consume of water source.
NOVELTY - The utility model is new type provide a plant with the composite attractant bait, a body, a tail and abdomen respectively set with fishhook connecting ring, wherein a fishing head connecting ring, internal fish attractant with storage bin, for storage chamber set with connected body outside the through hole, for n storage chamber set with attractant. A select set with attractant solution and aroma of bait, pass through a slow release attractant to lure. And the existing technology, the utility model is new type. The beneficial effect is that make up the traditional analogue is not enough, can set with a fill for a storage bin, a storage bin for a surrounding slow release attractant to lure, a no pollute, pseudo bait is floating posture match with smell for enhanced fitting phagostimulant rate of bait, can by sound, light, a composite aspect FORMULA for trapping fish.
NOVELTY - This new utility model claims of one of pregnant woman health environment monitoring device, comprising shell, on the shell provided with a display screen and input device, in the shell set with microprocessor, environment monitoring module, emotion detection module, blood pressure detecting module, detecting fetal mode, sleeping quality detection module, the education module and alarm prompting module, the environment monitoring module, emotion detection module, blood pressure detecting module, detecting fetal mode, sleeping quality detection module, the education module and alarm prompting module and respectively connected with microprocessor. This new utility model beneficial effect: for pregnant woman far from the bad environment, to beyond range sign for prompting alarm, can make pregnant woman far from the known and several main pollute of environment, protect safety of fetal and pregnant woman, and ensure health of fetal growth.
NOVELTY - The new type utility claims a veterinary uses a negative pressure extraction blood vessel coagulation accelerator, wherein, comprising tube body (1) and plug cover for negative pressure vacuum cavity in the pipe plug on the tube body, tube cavity of the tube body (2), the negative pressure in vacuum in a coagulation accelerator, the spout plug is aligning cavity in vacuum in the top surface middle part set with b for aligning a needle piercing the negative pressure (3). Compared with the existing technology, the utility model is new type blood collecting operation more convenient, it can greatly simplify germ sample preparation process, and can greatly shorten the germ sample in a large, and the germ in blood from animal body after all is a possibility in the closeness in container, a furthest reduce the pollute the sample, ensuring experiment result accuracy, at the same time, the utility model is new type also reduce medical personnel a blood source infection, and a blood sample converying and save all the more suitable, more safety.
NOVELTY - This utility model claims a heating device, comprising a pipe body, a heating tube, a heating tube and a supply mechanism. Pipe body is hollow rectangular-shaped structure, two end tube body is respectively provided with a liquid inlet and a liquid outlet, pipe body form inner heating cavity, a liquid inlet and a liquid outlet are connected a heating cavity, the pipe body inner side wall comprises the first mounting face and the second mounting face is relative. The first heating pipe. b the first mounting face, a heating pipe set b the second mounting face. A mechanism for respectively and the first heating pipe and the second heating pipe connected with, for the first heating pipe and the second heating pipe. A heating device by a pipe equipped with body, the first heating tube, the second heating tube and for a machine, to a pre-processing domestic garbage can is a heating operation so as to pre-processing domestic garbage subsequent Anaerobic. provide a good condition.
NOVELTY - The utility model is new type relates to a welding technology field, especially a small plant environment-friendly hydrogen welding machine. It comprises electrolysis groove, water tank, filter, protecting tempering tank, and a backfire; a terminal of electrolytic groove and a electrically connected, electrolytic slot set has a water inlet pipe and a gas outlet pipe, a water level part of water tank and water inlet pipe connected with the high water level part and the first air outlet pipe connected the top part of water tank has a air outlet pipe set, and the second air outlet pipe connected filter, filter set has a third air outlet pipe, anti-backfire tank. b. sum pipe and third backfire between. The utility model is new type of electrolytic groove in a controller of a resonance frequency of the following can more easily of a water electrolysis for hydrogen and oxygen, a water tank by the hydrogen and oxygen through a filter after drying can effective prevent of welding machine in a warm state under the icing problem of, at the same time, formed by protecting the tempering tank and backfire can form double channel protecting device, effective of the welding machine in use when the safety and reliability.
NOVELTY - Preparation of 5-(N,N-dibenzyl amino)acetyl salicylamide comprises mixing salicylamide and chloroacetyl chloride at molar ratio of 1:2.5-5-5.5, adding into the reaction container with ionic liquid as solvent where molar ratio of ionic liquid and salicylamide is 5-10:1, reacting at 35-55 degrees C under normal pressure, extracting with organic solvent to obtain 5-chloro acetyl salicylamide, mixing with dibenzylamine at molar ratio of 1:1-1.2, adding water and methanol at volume ratio of 2-4:1, heating at 50-70 degrees C for 2-4 hours, evaporating solvent under reduced pressure and recrystallizing.    USE - Method for preparing 5-(N,N-dibenzyl amino)acetyl salicylamide (claimed).    ADVANTAGE - The method is low-cost, short and environment-friendly and has high yield.
NOVELTY - Biological fermentation of solid organic waste comprises taking tobacco stalk and distiller's grains, crushing to less than 2 mm to obtain mixed material, mixing mixed material, water and yeast at weight ratio of 5:4:1-6:3:1, fermenting for 5-10 days with aeration treatment and turning every 10-15 hours, aging for 3-5 days, sieving, adding bentonite, mixing, granulating, sieving, drying, cooling and packaging.    USE - Method for biologically fermenting solid organic waste (claimed).    ADVANTAGE - The method is simple.
NOVELTY - The detector has a power source connected with a temperature detection module and a formaldehyde detection module. A humidity module is provided with a carbon dioxide detecting module. An input end of a center processing chip is used for receiving data from the temperature detection module. A terminal is arranged with an indicating lamp and a display screen that is connected to the center processing chip. wireless fidelity is provided with a RG45 wire interface.    USE - Gas detector.    ADVANTAGE - The detector monitors formaldehyde gas and CO2 gas concentration in an effective manner and improves warm air humidity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gas detector. '(Drawing includes non-English language text)'
NOVELTY - The method involves transmitting air (1) to a heat-insulated chamber (E), and cooling the air in a cooler (5) to form cooled flow. Gas mixture is placed inside the chamber to produce two fluids. One of the fluids is heated inside the chamber or vaporized via heat exchange with a heating unit (G) including an element having magnetocaloric properties. The element is alternatingly arranged in thermal contact with a cold source and a hot source, where variation in the magnetic flux via magnetocaloric effect of the element generates electrical and/or mechanical energy.    USE - Method for separating gas mixture at subambient temperature by cryogenic distillation in gas production plant.    ADVANTAGE - The method enables the arrangement of the element having magnetocaloric properties in thermal contact with the cold and hot sources, where variation in the magnetic flux via magnetocaloric effect of the element generates electrical and/or mechanical energy, thus ensuring simple separation of the gas mixture at subambient temperature by cryogenic distillation.    DETAILED DESCRIPTION - The fluid heated in the chamber has component e.g. air, nitrogen, oxygen, argon, carbon dioxide, methane, helium, hydrogen or carbon monoxide. An INDEPENDENT CLAIM is also included for an apparatus for separating gas mixture at subambient temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating structure and operation of a gas production plant.    Heat-insulated chamber (E)    Heating unit (G)    Air (1)    Compressor (3)    Cooler (5)
NOVELTY - The system has a pump for establishing a volumetric flow rate of carbon- poor media from an output port (48) of a reactor and into an input port (40) of an absorber. A first sensor measures a first carbon concentration level in the reactor at the output port of the reactor. A second sensor measures a second carbon concentration level of media discharged from the output port of the absorber. A controller operates the pump with input from the sensors to establish an optimized assimilation of captured carbon from the carbon-enriched growth media into the algae biomass in the reactor.    USE - System for capturing carbon in a carbon-poor media to create a carbon-enriched media in an algae growing system.    ADVANTAGE - The system allows carbon concentration levels of upstream and downstream from the reactor to be measured and compared by the controller with preset carbon concentration levels that are identified for optimal system performance. The system limits the addition of glycerin to the plug flow reactor at night to make algae cells to utilize the glycerin without facilitating the growth of foreign organisms.    DETAILED DESCRIPTION - The reactor is selected from a group consisting of a pond, a plug flow reactor and an expanding plug flow reactor. INDEPENDENT CLAIMS are also included for the following:    (1) a method for capturing carbon in a carbon-poor media to create a carbon-enriched media    (2) a system for establishing elevated carbon dioxide levels in an algae growth medium of a bioreactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an algae growing system.    System for producing biofuel from pollutant-fed algae (10)    Bioreactor (28)    Input port (40)    Output port (48)    Glycerin (100)
NOVELTY - Water oxidation catalyst comprises lithium-cobalt-germanate.    USE - The water oxidation catalyst is useful for splitting water into oxygen and hydrogen ions (claimed).    ADVANTAGE - The water oxidation catalyst can be produced in simple manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) oxygen generating catalyst comprising lithium-cobalt-germanate;    (2) an electrode for electrochemical oxidation of water to split water into oxygen and hydrogen ions, comprising a substrate, and an active material containing lithium-cobalt-germanate, arranged in contact with the substrate;    (3) oxidizing water, comprising providing an electrode containing lithium-cobalt-germanate, providing water and conducting electrolyte, and arranging the water and the supporting electrolyte in contact with the lithium-cobalt-germanate with an applied oxidative overpotential; and    (4) forming the water oxidation catalyst, comprising providing lithium hydroxide and germanium dioxide, mixing lithium hydroxide and germanium dioxide to form a first solution, providing cobalt(II) chloride in a solvent, mixing the obtained first solution and cobalt(II) chloride to form a second solution, and subjecting the second solution to a hydrothermal reaction to lithium-cobalt-germanate.
NOVELTY - A combination energy-saving and environment protection washroom A, relating to a toilet, specifically to a one does not need a water flushing of energy-saving and environment protection washroom. As a feces for use, and reduces the waste of water resource, the utility model is new type adopt the technology scheme is the lower part of the toilet set has storage hopper, feeding a material of a lower end is funnel shape, with discharge wherein. This utility model advantages are: 1. The combination energy-saving and environment protection washroom basic does not need water, saves water resource, 2. The combination a to obtain the energy-saving and environment protection washroom excrement is used for fermentation can generate methane; 3. The waste residue after a marsh gas can to a organic fertilizer or it can directly to field fertilizing, planting organic vigetable, 4. Matched using the new-type pedestal pan for water tank design, a vertical discharging pipe connection, saves using water and space.
NOVELTY - The new type utility claims a methanol recovery device, comprising a reaction kettle and a tank, a reaction kettle and a tank through a pipeline, a pipeline and a reaction tank is connected in series the first condenser, a tank and a condenser through circulation connecting pipe, a condenser by pipeline connected one refrigerator, inner pipe of the first condenser entrance is paved with a layer of molecule sieve. The utility model is new type can at a temperature or reaction temperature is high when, for a rectifying kettle of methanol by two horizontal condenser carrying out two times of condensation, and a refrigerator reinforced condensing effect, thus reducing the methanol consumption, goal of protecting life environment, a water-absorbent is a sieve, a. preparing entrained moisture adsorption in methyl alcohol and a small amount of, which ensures the purity of a methyl alcohol.
NOVELTY - Producing liquid biofuel from bio-based oils and/or fats, comprises: mixing alcohol with a raw material for forming a reaction mixture; pumping the reaction mixture to a reactor (16); mixing catalyst with reaction mixture in a selected process step either before or after the supply of reaction mixture to a high-pressure pump; adjusting temperature and pressure of reactor so that reaction mixture achieves supercritical state; esterifying reaction mixture to produce biofuel; and separating by-products and alcohol from biofuel, where biogas is used as catalyst in the method.    USE - The method is useful for producing liquid biofuel from bio-based oils and/or fats (claimed), where biofuel is biodiesel.    ADVANTAGE - The method utilizes biogas which improves the yield of liquid biofuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system (10) for producing liquid biofuel from bio-based oils and/or fats, including: mixing equipment (46) for mixing alcohol and catalyst with a raw material to form a reaction mixture; heating equipment for heating the reaction mixture; a high-pressure pump (26) for pumping the reaction mixture to a reactor; the reactor for esterifying the reaction mixture to form biofuel; adjustment equipment for adjusting the temperature and pressure of the reactor to achieve the supercritical state of the reaction mixture for esterification; and separation equipment (48) for separating by-products and alcohol from biofuel, where the system includes feed equipment for feeding biogas to the reaction mixture and a biogas reactor for local production of biogas.    DESCRIPTION OF DRAWING(S) - The figure shows a basic process diagram illustrating method and system for producing biofuel.    System (10)    Reactor (16)    High-pressure pump (26)    Mixing equipment (46)    Separation equipment (48)
NOVELTY - Invention describes biofuel containing acetals and vegetable oils; the biofuel represents diethylformal 40-80 vol % and unsaturated fatty glycerides 20-60 vol %.    USE - Chemistry.    ADVANTAGE - Producing the biofuel characterised by a high cetane number, which alongside with improving the low-temperature and start-up properties of the fuel prevents corrosion; it requires no engine rework, possesses the green exhaust with considerable reduction of costs by using the ingredients based on cheap heavy accessible products.
NOVELTY - Bio-fertilizer is prepared by culturing Bacillus, and incubating the culture at 65-80 degrees C for more than 60 minutes or more, where the bio-fertilizer has spore rate of 100%.    USE - The bio-fertilizer is useful for improving crop growth.    ADVANTAGE - The bio-fertilizer has excellent preservability, exhibits excellent crop fixing property, is prepared cost-effectively and rapidly and rich in nutrients, and maintains bacterial count to more than 6 months at 25 degrees C.
NOVELTY - Method for producing and separating at least one fermentation product from mixture of fermentation products in fermentation broth, involves (a) fermenting gaseous substrate in bioreactor comprising culture, (b) passing the fermentation broth to treatment zone operated at conditions to remove substantially all suspended and soluble biomass, (c) passing at least portion of the treated broth stream to simulated moving bed (SMB) module, (d) adsorbing at least one fermentation product onto the adsorbent and yielding raffinate, and (e) desorbing product from the adsorbent.    USE - The method is useful for producing and separating at least one fermentation product, preferably alcohol.    ADVANTAGE - The method is cost-effective and environmentally-friendly, and consumes minimal energy.    DETAILED DESCRIPTION - Method for producing and separating at least one fermentation product from mixture of fermentation products in fermentation broth, involves (a) fermenting gaseous substrate in bioreactor comprising culture of at least one microorganisms to produce fermentation broth comprising mixture of fermentation products, where the mixture comprises at least two products chosen from ethanol, acetic acid, 2,3-butanediol, butanol, isopropanol and acetone, (b) passing the fermentation broth to treatment zone operated at conditions to remove substantially all suspended and soluble biomass and produce treated broth stream, (c) passing at least portion of the treated broth stream to simulated moving bed (SMB) module comprising at least one adsorbent, (d) adsorbing at least one fermentation product onto the adsorbent and yielding raffinate comprising the nonadsorbed components of the treated broth stream, and (e) desorbing at least one product from the adsorbent to yield product stream.
NOVELTY - A system comprises a pyrolizer having an inlet and an outlet, a condenser having an inlet, a non-condensable gas outlet and a liquid outlet, and an anaerobic digester having inlets, where the outlet of the pyrolizer is connected to the inlet of the condenser, and the non-condensable gas outlet or the condenser is connected to an inlet of the anaerobic digester.    USE - The system is used for producing methane.    ADVANTAGE - Provided is a method for converting ligno-cellulosic materials resistant to biotreatment into materials which are highly amenable to biotreatment processes for forming energetic fuels in gaseous and/or liquid states.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a process comprises subjecting biomaterials to pyrolysis to produce pyrolysis products including a pyrogas and char, and mixing the pyrogas into a sludge in an anaerobic digester.
NOVELTY - Producing energy-dense biomass and fermentable sugars from cellulosic biomass comprises providing a feedstock comprising cellulosic biomass; and extracting the feedstock with steam and/or hot water under effective extraction conditions to produce an extract liquor containing hemicellulosic oligomers, dissolved lignin, and cellulose-rich solids, where some of the steam and/or hot water is derived from an internal or external source of fermentation vinasse.    USE - The method is used for producing energy-dense biomass and fermentable sugars from cellulosic biomass.    ADVANTAGE - Processes to prepare biomass, including wood and agricultural residues, into clean, energy-dense biomass for improved combustion, with or without pelletizing the biomass are provided. The energy-dense biomass is capable of being fired alone or in combination with another solid fuel. The processes above have good potential to recover various co-products, such as sugars, sugar fermentation products, furfural, levulinic acid, fertilizers, and lignin.    DETAILED DESCRIPTION - Producing energy-dense biomass and fermentable sugars from cellulosic biomass comprises (a) providing a feedstock comprising cellulosic biomass; (b) extracting the feedstock with steam and/or hot water under effective extraction conditions to produce an extract liquor containing hemicellulosic oligomers, dissolved lignin, and cellulose-rich solids, where some of the steam and/or hot water is derived from an internal or external source of fermentation vinasse; (c) separating a portion of the hemicellulosic oligomers from the cellulose-rich solids, to produce intermediate solids; (d) torrefying the intermediate solids to produce the energy-dense biomass; (e) hydrolyzing the hemicellulosic oligomers into fermentable sugars; and (f) recovering the fermentable sugars.
NOVELTY - The method involves feeding bio-mass pellets prepared from agricultural waste through a reactor (3) and a hopper (1). The air is provided at the rate of l kg per kg of pellets through a blower (2). A gasification process is performed, and the producer gas produced is passed through a cyclone portion (4), when the process of manufacturing producer gas is started. The dust particles are removed. The liquor and tar which are detrimental for burning are removed.    USE - Method of manufacturing producer gas used in thermal application and power generation application.    ADVANTAGE - Since the purified gas is fed through the regulator and the pipeline, the burners are burned with full blue flame without using secondary air with thermal value equivalent to the liquid petroleum gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the process of manufacturing the producer gas.    Hopper (1)    Blower (2)    Reactor (3)    Cyclone portion (4)    Condenser (5)
NOVELTY - A pig manure biogas residue fertilizer production system comprises barn, drainage grill, sewage collection tank, first regulation pool, second regulation pool, continuous flow stirred-tank reactor, secondary fermentation tank, and concentration tank connected to solid-liquid separator.    USE - Pig manure biogas residue fertilizer production system.    ADVANTAGE - The system is easy to operate, effectively solves piggery wastewater and environment pollution problems, reduces incidence of disease and use of fertilizers and pesticides, saves cost and space, alleviates fertilizer and soil pollution caused by pesticides, and promotes recycling of resources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer comprising feeding piggery wastewater into drainage grill to remove suspended solids, discharging into sewage collection pool, and pumping into first regulation pool for 1-3 hours; mixing with pig manure, pumping into continuous flow stirred-tank reactor, fermenting through secondary fermentation tank, pumping ferment into concentration tank, and separating solid and liquid through solid-liquid separator; and mixing, granulating, drying, sieving, cooling, sieving, and subjecting to biological treatment to obtain biogas fertilizer.
NOVELTY - Organic fertilizer comprises 26 pts. wt. pond scum powder, 12 pts. wt. corn meal, 6 pts. wt. chicken bone meal, 8 pts. wt. shrimp shell powder, 10 pts. wt. sweet potato powder, 5 pts. wt. sepiolite powder, 15 pts. wt. silkworm excrement and 12 pts. wt. sugarcane bagasse.    USE - Organic fertilizer.    ADVANTAGE - The method is simple. The fertilizer promotes crop nutrient absorption and improves soil and prevents crop drought and waterlogging.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising taking raw materials, pulverizing, mixing, adding 30 wt.% water, placing mixture in stirred tank fermenter, carrying out fermentation at 40-45 degrees C for 72 hours, cooling, drying, granulating and packaging.
NOVELTY - Biogas pool slag pumping device comprises a solid-liquid separator (9). One end of a liquid pumping pipe (1) of the solid-liquid separator is connected with a water pump (10) and is extended into a biogas pool (5). One end of a liquid return pipe (2) of the solid-liquid separator is extended into a gas storage chamber of the biogas pool. One end of a water return pipe of the solid-liquid separator is connected with a hydraulic pressure chamber of the biogas pool.    USE - Used as biogas pool slag pumping device.    ADVANTAGE - The device reduces cleaning time and energy consumption, and is safe and environmentally friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biogas pool slag pumping device.    Liquid pumping pipe (1)    Liquid return pipe (2)    Biogas pool (5)    Solid-liquid separator (9)    Water pump (10)
NOVELTY - Processing agricultural waste involves crushing agricultural waste lignocellulosic raw materials to obtain crushed material. Sodium hydroxide, urea and water are added into crushed material and then mixed to obtain mixture. Cellulase is added into mixture and then hydrolyzed to obtain hydrolyzed substance containing glucose and lignocellulose.    USE - Method for processing agricultural waste (claimed).    ADVANTAGE - The method enables to recycle agricultural waste in a cost-effective manner.
NOVELTY - Method for preparing fermentation starting sugar liquid, involves saccharifying nonfood-type biomass, obtaining low concentration sugar-containing liquid, mixing obtained low concentration sugar-containing liquid and saccharide or high concentration sugar-containing liquid of food-type derived biomass, and obtaining fermentation starting sugar liquid.    USE - The method is useful for preparing fermentation starting sugar liquid which is useful for manufacturing chemical substance, preferably ethanol or succinic acid, butanol, butanediol, lactic acid, or cellulase (all claimed).    ADVANTAGE - The method is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing chemical substance, which involves preparing and fermenting the fermentation starting sugar liquid.
NOVELTY - Generating monomeric carbohydrates from a biomass feedstock comprises providing a biomass feedstock stream having at least one of cellulose, hemicellulose, amylase and/or maltodextrin, contacting aqueous feed stock with pentacyanocobaltate(II) anion catalyst (a1) to produce a product stream comprising at least one monomeric carbohydrate.    USE - The method is useful for generating monomeric carbohydrate that is glucose, galactose, xylose, mannose, arabinose and/or rhamnose and producing ethanol (all claimed) that is used as transportation fuel and to generate electricity.    ADVANTAGE - The method: in addition to glucose production, concomitantly produces hydrogen that is valuable potential fuel; utilizes inexpensive components; is carried at room temperature in water solution and produces glucose without degradation; is rapid and occurs within minutes; produces products that are separated easily; is performed without expensive separation and purification; does not require complex chemical processes; and occurs under mild conditions and should easily be scaled to large-scale production.    DETAILED DESCRIPTION - Generating monomeric carbohydrates from a biomass feedstock comprises providing a biomass feedstock stream having at least one of cellulose, hemicellulose, amylase and/or maltodextrin, contacting aqueous feed stock with pentacyanocobaltate(II) anion catalyst of formula (a1) to produce a product stream comprising at least one monomeric carbohydrate. An INDEPENDENT CLAIM is also included for a composition, comprising biomass having at least one of cellulose, hemicellulose, amylase and/or maltodextrin and (a1)
NOVELTY - This utility new type claims a a small portable vehicular hydrogen and oxygen generator..., set with a plurality of electrolytic groove, water tank and pump body in a box body, every two electrolytic groove are connected with one of a oxygen pipe, one of a hydrogen pipe and a cable conduit, a oxygen pipe is connected to main oxygen collection pipe, a hydrogen collecting pipe is connected to a hydrogen pipe, water tank and one circulation fluid path is closed, several collecting branch is connected to main water pipe, set with a main water pipe of upper pump body can drive fluid flow. This utility new type to achieve the beneficial effect of: provide a more reasonable is a pneuma way and a water path pipeline design, a hydrogen-oxygen generator whole structure more compact, volume small portable, design a circulation water path make a gas in the electrolytic groove, it can increase efficiency of electrolysis, and to a water vapour electrolytic process and filtering process, oxygen and hydrogen and the design structure of pneuma way in time from electrolytic groove respectively output.
NOVELTY - The method involves obtaining smoldering tarry carbonization gas from a solid organic insert material (A) in a low temperature gasifier (1). The carbonization gas (B) in a high temperature gasifier (2) is partially reduced to a synthesis gas (D) by partial oxidation. The synthesis gas produced in the high-temperature gasifier is dusted off in a de-dusting system (4), and subjected to a wet scrubber (5) of a wet laundry using a wash liquid. The residual coke separated from the synthesis gas is supplied in the wet laundry to support the reduction of the high-temperature gasifier.    USE - Method for partially gasifying solid organic insert material such as biomass and charcoal.    ADVANTAGE - The effective utilization of the residue coke is ensured. The manufacturing cost of the slurry residue coke system is reduced. The essential and reliable mechanical moving components of the coke system are obtained. The reduction of burden of the effluent with coke is enabled. The waste water treatment process is simplified. The efficiency of the gasifier is raised.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a plant for partially gasifying solid organic insert material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the plant for partially gasifying solid organic insert material.    Low temperature gasifier (1)    High temperature gasifier (2)    De-dusting system (4)    Wet scrubber (5)    Solid organic insert material (A)    Carbonization gas (B)    Synthesis gas (D)
NOVELTY - Producing methane, comprises performing methanation by converting methane into carbon source through supplying reaction gas containing hydrogen and carbon source containing carbon dioxide or carbon monoxide into a reactor in the presence of catalyst. The catalyst is methanation catalyst (M(6-x)NixAl2O9) derived by heat treating nickel substituted hydrotalcite-type compound.    USE - The method is useful for producing methane (claimed).    ADVANTAGE - The method promotes methanation reaction, has high conversion rate even at a relatively low temperature, produces methane having excellent durability, is economical, does not utilize expensive metals, and uses catalyst having good activity even at low relatively temperature.    DETAILED DESCRIPTION - Producing methane, comprises performing methanation by converting methane into carbon source through supplying reaction gas containing hydrogen and carbon source containing carbon dioxide or carbon monoxide into a reactor in the presence of catalyst. The catalyst is methanation catalyst of formula (M(6-x)NixAl2O9) derived by heat treating nickel substituted hydrotalcite-type compound.    M = metal element, preferably alkaline earth metal; and    x = 0.2-6.    INDEPENDENT CLAIMS are also included for: (i) methanation catalyst as mentioned above; and (ii) producing methanation catalyst, comprising (a) preparing raw material reagent mixed solution by mixing basic solution and mixed solution containing alkaline earth metal precursor, nickel precursor and aluminum precursor, (b) producing reaction solution using catalyst precursor containing nickel substituted hydrotalcite-type compound by stirring the obtained raw material reagent mixed solution, and (c) producing the methanation catalyst by heat treating the obtained catalyst precursor at 500-900 degrees C.
NOVELTY - Energy-saving type device comprises a separation column (110) for inflowing the 4C liquid petroleum gas, out-flowing a iso-butane stream to an upper side and a normal butane stream to a lower side using waste heat as a heat source, a first heat exchanger (120) for preheating the 4C liquid petroleum gas, and a second heat exchanger (130) for flowing the 4C liquid petroleum gas into the separation column by rising temperature using waste heat as a heat source.    USE - The device is useful for separating normal butane and iso-butane from 4C liquid petroleum gas (claimed).    ADVANTAGE - The device requires low amount of energy during operation, and is economical.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the energy-saving 4C liquid petroleum gas separation device.    Separation column (110)    First heat exchanger (120)    Second heat exchanger (130)    Third heat exchanger (140)    Drum (150)
NOVELTY - Drying machine comprises a machine frame drying interlayer (3) which is connected with former electric machine (5), heater (7), controller (9), later electric machine (11), material turn shaft and walking wheel. A machine frame is mounted on the former electric machine, later electric machine and controller. The later electric machine is connected with the former electric machine. Former wheel is connected with the later wheel, which is intended for belt transmission by a transmission device. A material turn shaft is connected with machine frame installation part.    USE - Drying machine used for fermentation of organic fertilizer (claimed).    ADVANTAGE - The drying machine has high production efficiency, is easy to operate, and ensures short fermentation time and uniform drying.    DETAILED DESCRIPTION - Drying machine comprises a machine frame drying interlayer which is connected with former electric machine, heater, controller, later electric machine, material turn shaft and walking wheel. A machine frame is mounted on the former electric machine, later electric machine and controller. The later electric machine is connected with the former electric machine. Former wheel is connected with the later wheel, which is intended for belt transmission by a transmission device. A material turn shaft is connected with machine frame installation part, which provided with multiple turn material pieces. The machine frame is mounted on a drying interlayer intended for drying, and is connected with stirring shaft and transmission device. The transmission device is connected with the stirring shaft, which is provided with multiple of blades.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a drying machine.    Machine frame drying interlayer (3)    Former electric machine (5)    Heater (7)    Controller (9)    Later electric machine (11)
NOVELTY - The non-polluted cultivation method involves coating seeds before seeding using coating agent that comprises mixture of phoxim, anti-insect triadimefon wettable powder and water, and drying coated seeds, tilling soil of flat farmland by certain tillage depth to loosen soil, planting seeds on fine soil, watering soil after seeding, and fertilizing soil using manure and nitrogen, phosphorus, potassium fertilizer, zinc sulfate, and boron fertilizer.    USE - Non-polluted cultivation method for planting wheat.    ADVANTAGE - The cultivation method is suitable in a soil environment of north China, and improves yield and quality of a marigold rib wheat standard.