NOVELTY - Preparation of liquefied natural gas involves successively passing hydrogen-containing methane gas through the cold box heat exchanger, expansion booster, gas-liquid separator to separate liquid and gas, dehydrogenation tower and denitrification tower, entering dehydrogenated liquid into the denitrification tower, collecting liquefied natural gas from the bottom of denitrification tower, introducing part of liquefied natural gas into dehydrogenation tower, cooling, introducing condensate into denitrification tower and passing non-condensable gas to fuel pipe network.    USE - Method for preparing liquefied natural gas (claimed).    DETAILED DESCRIPTION - Preparation of liquefied natural gas comprises successively passing hydrogen-containing methane gas through the cold box heat exchanger, expansion booster, gas-liquid separator to separate liquid and gas, dehydrogenation tower and denitrification tower, entering dehydrogenated liquid into the denitrification tower, collecting liquefied natural gas from the bottom of denitrification tower, introducing part of liquefied natural gas into dehydrogenation tower, cooling the gas from the overhead through the condenser, introducing condensate into denitrification tower, passing non-condensable gas through the cold tank heat exchanger to fuel pipe network, returning overhead into the dehydrogenation tower, cooling gas by condenser, returning condensate to the top of the tower and delivering non-condensable gas through the cold tank heat exchanger.
NOVELTY - Carbon steel structure anaerobic power generation gas station comprises anaerobic device, purification tower, warming pressure pump and power generator.    USE - Used as carbon steel structure anaerobic power generation gas station.    ADVANTAGE - The device can saves raw materials and protects the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the carbon steel structure anaerobic power generation gas station.
NOVELTY - Recovering acetylisovaleryltylosin tartrate alkali from acetylisovaleryltylosin tartrate crystalline mother liquor comprises adding surfactant to crystalline mother liquor, concentrating into thin film using air foaming method, collecting bubble liquid film, cooling, separating by adding separating agents, filtering, carrying out crystallization process for filtrate and washing to obtain acetylisovaleryltylosin tartrate alkali.    USE - The method is useful for recovering acetylisovaleryltylosin tartrate alkali from acetylisovaleryltylosin tartrate crystalline mother liquor (claimed).    ADVANTAGE - The method is simple, recyclable and economical; solves the problem of recovering by low thermal stability in low concentration of crystalline mother liquor; improves the recovery rate of the finished product by reducing the content of pollutants in discharges; has increased available resources, social and economic benefits; and is environmentally friendly.
NOVELTY - Biogas system comprises feedstock tube (10), discharging tube (20), fermentation pipeline (30), hydraulic pipeline, fermentation annular pipe. The fermentation pipeline is set at top of the annular fermentation pipeline. The feedstock tube and the discharging tube are respectively inserted into the vertical separator feed side wall tube and outlet tube extends to biogas fermentation liquid ring pipeline. Water pressure and feedstock pipe is connected with drain pipe and water discharging pipe. The fermentation pipe is set between adjacent blocking plate forming fermentation area.    USE - Biogas system.    DETAILED DESCRIPTION - Biogas system comprises feedstock tube, discharging tube, fermentation pipeline, hydraulic pipeline, fermentation annular pipe. The fermentation pipeline is set at top of the annular fermentation pipeline. The feedstock tube and the discharging tube are respectively inserted into the vertical separator feed side wall tube and outlet tube extends to biogas fermentation liquid ring pipeline. Water pressure and feedstock pipe is connected with drain pipe and water discharging pipe. The fermentation pipe is set between adjacent blocking plate forming fermentation area. Top of the fermentation area is provided with gasguide tube (36), which is provided with valve. Fermentation system also comprises cloth bacteria device, which includes cloth bacteria pipe, cloth bacteria hole, drainage pipe (46) and water pressure. The cloth bacteria pipe is circular pipe, which fixes cloth bacteria to annular inner side wall pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas system.    Feedstock tube (10)    Discharging tube (20)    Fermentation pipeline (30)    Gasguide tube (36)    Drainage pipe (46)
NOVELTY - Biological microbial inoculum comprises 25 wt.% Rhodococcus, 20 wt.% Bacillus subtilis, 15 wt.% Pseudomonas aeruginosa, 10 wt.% Saccharomyces cerevisiae, 10 wt.% European nitrosomonas Aeromonas, 10 wt.% Bacillus cereus spores, 5 wt.% Aspergillus niger and 5 wt.% Paracoccus denitrificans.    USE - Biological microbial inoculum used for treating municipal sewage (claimed) and industrial wastewater.
NOVELTY - Treatment agent comprises chlorinated trisodium phosphate (15-20 pts. wt.), fenarimol (5-10 pts. wt.), Bacillus subtilis (30-3000 million spores/g formulations, 25-35 pts. wt.), thiamethoxam (20-30 pts. wt.), wetting agent (2-4 pts. wt.), film-forming agent (5-8 pts. wt.), dispersant (3-5 pts. wt.) and surfactant (15-25 pts. wt.).    USE - Treatment agent for corn seed (claimed).    ADVANTAGE - The treatment agent improves seed germination rate, and is disease-resistant and eco-friendly and provides protection to seed.
NOVELTY - Collecting sterile Synechococcus involves transferring Synechococcus from optical bioreactor to sterile collection device. The sterile collection device is sealed, placed in dark and cooled at 1.5 degrees C per minute. The temperature is reduced to 6-8 degrees C. The obtained Synechococcus is mixed with pH modifier at 150-200 revolutions per minute. The pH of the obtained mixture is adjusted to 10-10.5. The bacteria is cooled at 6-8 degrees C for 8-15 minutes. The Synechococcus concentrate is collected from the inlet of the sterile collection device.    USE - Method for collecting sterile Synechococcus (claimed).    ADVANTAGE - The method reduces protein precipitation and improves utilization value of Synechococcus, and enables to produce high yield of Synechococcus in eco-friendly manner.    DETAILED DESCRIPTION - Collecting sterile Synechococcus involves transferring Synechococcus from optical bioreactor to sterile collection device. The sterile collection device is sealed, placed in dark and cooled at 1.5 degrees C per minute. The temperature is reduced to 6-8 degrees C. The obtained Synechococcus is mixed with pH modifier at 150-200 revolutions per minute. The pH of the obtained mixture is adjusted to 10-10.5. The bacteria is cooled at 6-8 degrees C for 8-15 minutes. The Synechococcus concentrate is collected from the inlet of the sterile collection device. The obtained concentrate is centrifuged to obtain bacterial supernatant. The obtained bacterial supernatant is added with hydrochloric acid (10%) and pH is adjusted to 7-7.5. The obtained bacterial mixture (10-20%) is added to the bioreactor and cultured for 10-30 hours to reach cell density 0.8-1.2g/L. The Synechococcus mixture is circulated and sterile Synechococcus is collected.
NOVELTY - A Trichoderma harzianum strain Tr16 (CGMCC NO: 9772), is new.    USE - The T.harzianum strain Tr16 is useful in preparation of drug for preventing sorosis disease in mulberry (all claimed).    ADVANTAGE - The T.harzianum strain Tr16 provides bacteriostatic rate up to 82.25% after 144 hours, and prevention effect of 82.53%, and is environmentally-friendly.
NOVELTY - Microecological composition comprises 60-70 wt.% Bacillus, 10-20 wt.% Actinomycetes and 10-20% lactic acid bacteria.    USE - The microecological composition is useful for repairing aquiculture water environment (claimed).    ADVANTAGE - The composition is environmentally-friendly, has high density, and rapidly forms micro-ecological dominant flora in water to inhibit propagation of pathogenic bacteria, adjust the alga density in water and promote the repair and balance of an aquatic ecosystem.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned composition, which involves (a) inoculating Bacillus and Actinomycetes into culture medium containing soluble starch, autoclaving the medium at 100-140 degrees C for 10-30 minutes (pH 7-7.5), sterilizing lactic acid bacteria, mixing Bacillus, Actinomycetes and lactic acid bacteria, and culturing mixture at 35-40 degrees C for 20-24 hours, (b) adding the 10-20% culture medium into 20 l tank, and expanding medium, (c) adding 10-20% expanded culture medium into 200 l tank, (d) immobilizing the culture medium using wheat bran, and (e) drying medium and crushing dried product.
NOVELTY - Agricultural complex agents comprise microbial cells and adsorption carrier. The microbial cells comprise 20-30 pts. wt. Lactobacillus acidophilus, 15-25 pts. wt. Coccobacillus, 20 -25 pts. wt. Escherichia coli, 15-20 pts. wt. Bacillus, 10-20 pts. wt. Trichoderma and 10-15 pts. wt. Aspergillus. The adsorption carrier comprises 5-10 pts. wt. zeolite, 5-10 pts. wt. bran, 5-10 pts. wt. bone meal, 5-10 pts. wt. fish and 1-5 pts. wt. brown sugar.    USE - Agricultural complex agents.    ADVANTAGE - The agricultural complex agents are eco-friendly, improves efficiency and resistant to bacteria.
NOVELTY - Producing methane, methanol or formic acid involves using single-chamber microbial electrolysis tank (2). The single-chamber microbial electrolysis tank is placed with anode electrode (8) and cathode electrode (3). The anode electrode is connected to higher potential side of power supply (1). The cathode electrode is connected to low potential side of the power supply. Electrically methane oxidizing bacteria (9) is adhered on the surface of the anode electrode. The cathode electrode is platinum-coated titanium (6) mesh electrode. The methane-oxidizing bacteria metabolize methane.    USE - Method for producing methane, methanol or formic acid (claimed).    ADVANTAGE - The method is eco-friendly and, conducted under mild conditions.    DETAILED DESCRIPTION - Producing methane, methanol or formic acid involves using single-chamber microbial electrolysis tank. The single-chamber microbial electrolysis tank is placed with anode electrode and cathode electrode. The anode electrode is connected to higher potential side of power supply. The cathode electrode is connected to low potential side of the power supply. Electrically methane oxidizing bacteria is adhered on the surface of the anode electrode. The cathode electrode is platinum-coated titanium mesh electrode. The methane-oxidizing bacteria metabolize methane and produce methanol, formic acid, hydrogen ions or electrons. The electric auxiliary and cathode catalyst on the surface of cathode electrode produces hydrogen ions.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device.    Power supply (1)    Single-chamber microbial electrolysis tank (2)    Cathode electrode (3)    Titanium (6)    Anode electrode (8)    Methane oxidizing bacteria (9)
NOVELTY - Preparing collagen protein includes using protein (91.37%), acid-soluble protein (75.20%), peptide (67.76%), hydroxyproline (10.47%), free amino acid (7.44%) and total amino acids ( 90.55%,), which are stirred uniformly.    USE - Method for preparing collagen protein (claimed).    ADVANTAGE - The method enables to prepare collagen protein, which improves comprehensive utilization of fish processing, solves problems of environmental pollution and has economic benefits.
NOVELTY - Selective culture medium includes selective solid culture medium or selective liquid culture medium. The selective solid culture medium is an existing medium comprising agar, 2 mu g/ml tobramycin and 20 U/ml polymyxin B. The selective liquid culture medium is obtained by removing agar from the existing medium. The selective liquid culture medium comprises 2 mu g/ml tobramycin and 20 U/ml polymyxin B. The selective culture medium is subjected to sterilization and cooling process.    USE - The selective culture medium is useful for culturing F.columnare (claimed).    ADVANTAGE - The selective culture medium simply and environmentally-friendly enables culturing of F.columnare.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for performing separation and purification of Flavobacterium columnare using selective culture medium, which involves (a) isolating F.columnare from fish lesions, and inoculating the F.columnare into selective culture medium, (b) culturing the F.columnare using selective solid culture medium, (c) culturing the F.columnare using selective liquid culture medium, and (d) purifying the F.columnare culture, and subjecting obtained product to cryopreservation and dry preservation.
NOVELTY - Annular fermentation system comprises raw material feedstock tube (10), multiple fermentation cell (32), and fermentation area. The fermentation area (301) and air pipe (38) are connected to fermentation marsh gas cell. The feedstock tube and discharge tube (20) are connected to water pipe. The fermentation area top part is provided with marsh gas input. The marsh gas flows through high pressure fermentation area to low pressure fermentation cell.    USE - Annular fermentation system used for producing marsh gas (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of marsh producing annular fermentation system.    Feedstock tube (10)    Discharge tube (20)    Fermentation cell (32)    Air pipe (38)    Fermentation area (301)
NOVELTY - Immobilized granule comprises 20-45 wt.% sulfate-reducing bacterial sludge, 2-8 wt.% powder of steel residue, 3-10 wt.% maifanite, 5-9 wt.% polyvinyl alcohol, 0.2-1.5 wt.% sodium alginate, 4-15 wt.% biomass, and 11.5-65.8 wt.% water.    USE - The immobilized granule is useful for acidic wastewater treatment.    ADVANTAGE - The immobilized granule avoids water pollution, reduces concentration of heavy metal, improves ecological quality of mine, preferably coal mine, does not requires floor space for wastewater treatment, and consumes no power.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing immobilized granule, which involves (a) adding polyvinyl alcohol and sodium alginate to distilled water, sealing obtained mixture at room temperature for 20-30 hours, heating the mixture in water bath at 90 plus minus 5 degrees C, and continuously stirring obtained mixture, (b) slowly adding the biomass and maifanite to the mixture obtained in step (a), uniformly stirring obtained mixture, and cooling the mixture to 37 plus minus 1 degrees C, (c) centrifuging raw liquid of sulfate-reducing bacterial sludge at 2000-4000 revolutions/minute (rpm) for 6-15 minutes to obtain product having mixed liquor volatile suspended solids (MLVSS) concentration of 10-15 mg/l, adding product obtained in step (b) to the product, and uniformly stirring obtained mixture, and (d) uniformly adding 2-5% calcium chloride and remaining components to mixture obtained in step (c) in drop-wise manner, controlling pH of the mixture at 5-7 using saturated solution of boric acid, and performing cross-linking reaction for 4-8 hours to obtain product.
NOVELTY - Performing enzymatic synthesis of theaflavins involves mixing tea polyphenol solution as substrate with polyphenol oxidase isoenzymes as an enzyme source in a volume ratio of 1:500-800. Enzymatic reaction is then performed at 20-44 degrees C under 60-150 revolutions per minute in a water bath shaker for 30-60 minutes in order to obtain enzymatic residues containing hydrolyzate. The obtained enzymatic residues containing hydrolyzate is dissolved in an equal volume of analytically pure ethyl acetate, where the prepared mixture is kept for 5-30 minutes to obtain ethyl acetate layer solution.    USE - Method for performing enzymatic synthesis of theaflavins using polyphenol oxidase isoenzymes (claimed).    ADVANTAGE - The method enables to perform enzymatic synthesis of theaflavins using polyphenol oxidase isoenzymes in an efficient manner. The highly purified theaflavins are the result of large scale production.    DETAILED DESCRIPTION - Performing enzymatic synthesis of theaflavins involves mixing tea polyphenol solution as substrate with polyphenol oxidase isoenzymes as an enzyme source in a volume ratio of 1:500-800. Enzymatic reaction is then performed at 20-44 degrees C under 60-150 revolutions per minute in a water bath shaker for 30-60 minutes in order to obtain enzymatic residues containing hydrolyzate. The obtained enzymatic residues containing hydrolyzate is dissolved in an equal volume of analytically pure ethyl acetate, where the prepared mixture is kept for 5-30 minutes to obtain ethyl acetate layer solution. The obtained ethyl acetate layer solution is subjected to extraction to obtain three consecutive ethyl acetate layer fractions. The obtained three consecutive ethyl acetate layer fractions are combined and then concentrated in vacuum to recover ethyl acetate, where the extracted theaflavins are the freeze-dried as the finished product.
NOVELTY - Anaerobic device comprises glass steel cylinder. The top part is provided with a semi-spherical gas storage cabinet (6).    USE - Anaerobic device.    ADVANTAGE - The anaerobic device improves the efficiency of biogas production and enables inner warming.    DESCRIPTION OF DRAWING(S) - The drawing shows a vertical cross-sectional schematic view anaerobic device.    Insulation layer (3)    Gas storage cabinet (6)    Biogas outlet (8)    Automatic alarm (9)    Ladder (13)    Spiral warming device (14)    Sealed doors (15)
NOVELTY - Inducing triploidy in Eriocheir sinensis involves fertilizing female Eriocheir sinensis at 15 degrees C to produce fertilized egg masses during her lifetime from this single mating. Anhydrous calcium chloride is then utilized to induced polyploidy in the fertilized female Eriocheir sinensis at optimized condition. Morphological markers are then used to predict pregnancy outcome in the Eriocheir sinensis, where the zygote to be treated acts as a positive control, where as potassium chloride solution acts as a negative control.    USE - Method for inducing triploidy in Eriocheir sinensis using anhydrous calcium chloride (claimed).    ADVANTAGE - The method enables to induce triploidy in Eriocheir sinensis using anhydrous calcium chloride by significantly improving the stability of triploidy state in the same, in an environment-friendly manner. The method is thus widely applicable in performing large-scale cultivation of Eriocheir sinensis.    DETAILED DESCRIPTION - Inducing triploidy in Eriocheir sinensis involves fertilizing female Eriocheir sinensis at 15 degrees C to produce fertilized egg masses during her lifetime from this single mating. Anhydrous calcium chloride is then utilized to induced polyploidy in the fertilized female Eriocheir sinensis at optimized condition. Morphological markers are then used to predict pregnancy outcome in the Eriocheir sinensis, where the zygote to be treated acts as a positive control, where as potassium chloride solution acts as a negative control. Flow cytometry is then performed to verify the validity of induced triploidy in Eriocheir sinensis using definite concentration of anhydrous calcium chloride under optimized condition based on test results.
NOVELTY - Complex enzyme comprises 8-15 pts. wt. xylanase, 5-10 pts. wt. cellulase, 3-6 pts. wt. beta -glucanase, 3-5 pts. wt. mesophilic alpha -amylase, 1-2 pts. wt. acid protease, 1-2 pts. wt. pectinase, 0.5-1 pts. wt. mannase, 3-6 pts. wt. Lactobacillus plantarum capsule, 2-5 pts. wt. plant preparation, 2-4 pts. wt. ginger extract and 1-2 pts. wt. liquorice.    USE - The complex enzyme is useful for suckling piglets (claimed).    ADVANTAGE - The complex enzyme increases use rate of feed and the growth rate of animal, enhances appetite and disease resistance of animals, prolongs shelf life of the product and is environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the complex enzyme for suckling piglets, comprising ultrafine grinding plant preparation, ginger extract and liquorice, uniformly mixing with xylanase, cellulase, beta -glucanase, mesophilic alpha -amylase, acid protease, pectinase, mannase and Lactobacillus plantarum capsule, sealing and packaging.
NOVELTY - Organic fertilizer comprises 30-69.9 wt.% animal dung, 5-30 wt.% animal urine, 25-40 wt.% various straws used in a single or mixed manner, and 0.05-0.2 wt.% core material, where the animal dung is cow dung or pig manure, the animal urine is cow urine or pig urine and the core material includes Bacillus subtilis and B.licheniformis.    USE - As organic fertilizer.    ADVANTAGE - The organic fertilizer is prepared cost-effectively and environmentally-friendly by utilizing animal dung and urine as raw materials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic fertilizer, which involves crushing the straws and spreading the straws on the ground, mixing the animal dung and the animal urine, and placing the animal dung and the animal urine on the well spread straws, and stirring, stacking, overturning and fermenting to prepare the raw materials into a high-quality product.
NOVELTY - Organic substance comprises 10-20 wt.% animal excreta, 30-45 wt.% animal urine, 40-50 wt.% straw, and 0.05-0.2 wt.% core materials, where the animal excreta is cow dung or pig manure, the animal urine is cow urine or pig urine, and the core materials is Bacillus subtilis, and B.licheniformis.    USE - The organic substance is useful in fertilizer.    ADVANTAGE - The method prepares high quality organic substance without causing pollution to environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic substance which involves (a) pulverizing straw with pulverizer into segments of 1-5 cm long, or filaments of 2-10 cm long, and crushing segments or filaments to 1.5-2.5 m wide, and 0.4-0.7 m height, (b) mixing animal excreta, and animal urine, spraying the mixture on crushed straw, mixing the core material with dried animal manure or rice bran and spreading on the straw, stirring the mixture, and stacking the mixture to a width of 4-6 m, and height of 0.9-1.4 m, (c) fermenting the stacked mixture at 60-75 degrees C for 5-8 days followed by turning, and (d) maintaining surface temperature at 40 degrees C, water content at 35-42%, and carbon and nitrogen ratio at less than 25:1, and pH value at 6-8, where the organic substance is yellow or brown without odor.
NOVELTY - Organic fertilizer is produced by mixing straw and animal manure, fermenting the mixture and adding suitable amount of auxiliary materials.    USE - As organic fertilizer.    ADVANTAGE - The organic fertilizer is produced simply.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing the organic fertilizer, which involves (a) mixing 80% wheat bran and 20% soybean meal, and water in ratio of 1:1, sterilizing the mixture at 121 degrees C for 30 minutes, cooling, inoculating Candida in the mixture, culturing at 28 degrees C for 4-5 hours, storing in refrigerator at 4 degrees C, and mixing with distilled water to obtain spore suspension, and (b) drying the collected straw, pulverizing to particle size of 5-10 mm, mixing 25-35% straw, 50-60% manure, 10-20% plant ash, 0.5% inorganic fertilizer, and 0.1-0.2% spore suspension, forming the mixture into pile to width of 150-200 cm and height of 70-100 cm, turning the mixture when temperature reaches 50-60 degrees C, and maintaining for 2-3 weeks.
NOVELTY - Organic fertilizer comprises 5-6 pts. wt. Acacia, 150-155 pts. wt. fresh sheep manure, 10-15 pts. wt. soybean, 1-2 pts. wt. garlic, 1-2 pts. wt. clove, 10-20 pts. wt. fruits and vegetables skin, 10-20 pts. wt. fish meal, 5-7 pts. wt. radish skin, 1-2 pts. wt. cassava alcohol extract, 4-6 pts. wt. castor cake, 5-7 pts. wt. Poria, 4-6 pts. wt. Astragalus mongholicus, 1-2 pts. wt. pepper leaf, 0.01-0.02 pt. wt. trichlorfon, 1-2 pts. wt. Rhodiola, 2-6 pts. wt. Typhonium giganteum, 1-2 pts. wt. Aconitum and 0.4-0.5 pt. wt. effective microorganism.    USE - Organic fertilizer having anthelmintic effect (claimed).    ADVANTAGE - The organic fertilizer can be prepared in easy manner with high yield and rich nutrition, does not cause harm to soil, is environmentally-friendly and does not leave pesticide residues.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer, which involves mixing Acacia, cassava alcohol extract, fruits and vegetables skin, crushing mixed material to obtain mixed slurry, then adding fresh sheep manure and mixing, fermenting the material at 40-45 degrees C for 24-30 hours to obtain fermented material (I), uniformly mixing Rhodiola, T.giganteum, Aconitum, Astragalus mongholicus, pepper leaf and Poria, decocting the mixed material, filtering decocted material to obtain traditional Chinese medicine dregs, mixing traditional Chinese medicine dregs, castor cake and fermented material (I) and then stacking for 2-4 days to obtain fermented material (II), mixing fermented material (II) and soybean, drying for 3-6 days, grinding the material and sieving through 100-200 mesh sieve, then adding traditional Chinese medicine liquid, granulating, drying and mixing remaining material.
NOVELTY - Bioenergy enhanced liquid comprises 2-2.5 pts. wt. meadow soil, 0.5-1 pt. wt. coastal silt soil, 0.5-1 pt. wt. humus soil, 3-3.5 pts. wt. embryo, 0.1-0.2 pt. wt. humic acid and balance water.    USE - Bioenergy enhanced liquid for waste deodorization and sludge reduction used in sewage reaction pool in nutrient pumice (claimed).    ADVANTAGE - Raw material is easy to get, cost is low and preparation is simple.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of bioenergy enhanced liquid which involves putting raw material in reaction container, keeping pressure of reactor at 0.15-0.2 MPa at 30-36 degrees C, culturing for 120-160 hours, and obtaining high density natural synthesis micoorganisms and its metabolic product with fungus number of 8-10x 108 Cfu/ml and pH value of 2.8-3.5; and    (2) application of bioenergy enhanced liquid in sewage reaction pool in nutrient pumice with sewage treatment capacity of 0.4%.
NOVELTY - Butyloctanol tail gas recycling device consists of compressing unit (a1) which receives tail gas and compresses tail gas to same pressure grade, rectifying unit (b1) which receives stream from unit (a1) and generates recycled butyral stream, compressing unit (a2) which receives tail gas stream from unit (b1) and generates compressed tail gas stream, rectifying unit (b2) which receives tail gas stream from unit (a2) and generates propylene-propane mixed stream, and deep cooling unit which receives tail gas stream from units (a2) and (b2), and recycling propylene-propane mixture.    USE - Device is used for recycling butyloctanol tail gas.    ADVANTAGE - The device efficiently recovers butyral and propylene-propane mixture with high recycling rate with low energy consumption.    DETAILED DESCRIPTION - Butyloctanol tail gas recycling device consists of compressing unit (a1) which receives tail gas and compresses the tail gas to the same pressure grade, rectifying unit (b1) which receives an output stream from the compressing unit (a1), and generates recycled butyral stream and remaining tail gas stream, compressing unit (a2) which receives remaining tail gas stream from the rectifying unit (b1), and generates compressed tail gas stream, rectifying unit (b2) which receives the remaining tail gas stream from the compressing unit (a2) and generates a recycled propylene-propane mixed stream and remaining tail gas stream, and deep cooling unit which receives remaining tail gas stream from the compressing unit (a2) and rectifying unit (b2), and recycling propylene-propane mixture.
NOVELTY - A skin collagen antioxidant peptide comprising a defined sequence of 6 amino acids is new.    USE - The peptide is used as antioxidant.    ADVANTAGE - The skin collagen antioxidant peptide preparation method is simple, easy and efficient. The antioxidant peptide is safe and environment-friendly and has no side effects, high antioxidant activity, and good thermal stability.    DETAILED DESCRIPTION - A skin collagen antioxidant peptide comprises the Asn-Glu-Gly-Ala-Cys-Gly and has a molecular ion peak of (M)+ 531 m/z according to ultra-performance liquid chromatography-mass spectrometry (UPLC-MS). An INDEPENDENT CLAIM is a method for preparing skin collagen antioxidant peptide.
NOVELTY - Method of using ultra-efficient biogas generator involves placing fermentation material into feed tube (10), allowing annular fermentation zones inside the tube to produce different amounts of marsh gas, generating marsh gas in inner pipeline (30), allowing marsh gas to move to extrusion feed pipe, allowing to flow between feed tube and bacteria cloth unit by inflow pressure, using fermentation area at top of airway (36) to discharge marsh gas and reducing pressure in fermentation zone, and refluxing marsh gas slurry stored in feed tube drain (44) into fermentation pipe.    USE - Method of using ultra-efficient biogas generator.    ADVANTAGE - The biogas generator has short routes and enables even distribution of biogas in bacteria.    DETAILED DESCRIPTION - Method of using ultra-efficient biogas generator involves placing fermentation material into feed tube (10), allowing annular fermentation zones inside the tube to produce different amounts of marsh gas in which flow pressure in biogas fermentation zone is smaller than flow pressure in fermentation area and when pressure of methane fermentation zone increases, biogas fermentation continues to flow to unfilled fermentation zone, generating marsh gas in inner pipeline (30), allowing marsh gas to move to extrusion feed pipe, allowing to flow between feed tube and bacteria cloth unit by inflow pressure, using fermentation area at top of airway (36) to discharge marsh gas and reducing pressure in fermentation zone, refluxing marsh gas slurry stored in feed tube drain (44) into fermentation pipe, using remaining stored marsh gas fermentation area, and stopping usage of marsh gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective diagram of the biogas generator.    Feed tube (10)    Discharge pipe (20)    Pipeline (30)    Airway (36)    Feed tube drain (44)
NOVELTY - Method of using U-shaped biogas slurry generating system to produce biogas involves performing process (A) of placing fermentation raw material into U-fermentation pipe (30) by feed tube (10), allowing biogas to accumulate in feed tube side walls and space between side walls of tube, and allowing biogas to flow between feed tube and feed tube drainage (12) by inflow pressure, and performing process (B) of dropping pressure in fermentation pipe, returning biogas slurry from feed tube drainage into fermentation pipe by pressure, and completing biogas slurry circulation.    USE - Method of using U-shaped biogas slurry generating system to produce biogas.    ADVANTAGE - Biogas fermentation route is shorted, gas yield is improved, and fermentation efficiency is improved.    DETAILED DESCRIPTION - Method of using U-shaped biogas slurry generating system to produce biogas involves performing process (A) of placing fermentation raw material into U-fermentation pipe (30) by feed tube (10), allowing biogas to accumulate in feed tube side walls and space between side walls of tube, and allowing biogas to flow between feed tube and feed tube drainage (12) by inflow pressure, performing process (B) of dropping pressure in fermentation pipe, returning biogas slurry from feed tube drainage into fermentation pipe by pressure, and completing biogas slurry circulation, and performing process (C) of continuously producing biogas and promoting biogas circulation.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of the U-shaped biogas slurry generating system.    Feed tube (10)    Feed tube drainage (12)    Discharge pipe (20)    Fermentation pipe (30)    Exhaust pipe (42)
NOVELTY - Anaerobic fermentation method of U-shaped unidirectional convective stirring system to produce biogas involves performing process (A) of placing fermentation raw material into U-shaped fermentation pipe (30) by feed tube (10), allowing biogas to accumulate in collecting or discharging pipe side wall and fermentation zone between feed tube and adjacent blocking plates, allowing fermentation slurry to flow to feed tube drainage (12), discharge pipe (20), and fabric bacteria unit by inflow pressure, and fermenting by inflow pressure.    USE - Anaerobic fermentation method of U-shaped unidirectional convective stirring system to produce biogas.    ADVANTAGE - Biogas fermentation route is shorted, gas yield is improved, and fermentation efficiency is improved.    DETAILED DESCRIPTION - Anaerobic fermentation method of U-shaped unidirectional convective stirring system to produce biogas involves performing process (A) of placing fermentation raw material into U-shaped fermentation pipe (30) by feed tube (10), allowing biogas to accumulate in collecting or discharging pipe side wall and fermentation zone between feed tube and adjacent blocking plates, allowing fermentation slurry to flow to feed tube drainage (12), discharge pipe (20), and fabric bacteria unit by inflow pressure, and fermenting by inflow pressure, performing process (B) of lowering pressure in fermentation area, allowing biogas to flow to adjacent fermentation area, returning biogas slurry from feed tube drainage to fermentation pipe, and completing biogas slurry circulation, and performing process (C) of continuously producing biogas and promoting biogas circulation.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of the U-shaped unidirectional convective stirring system for producing biogas.    Feed tube (10)    Feed tube drainage (12)    Discharge pipe (20)    Fermentation pipe (30)    Exhaust pipe (42)
NOVELTY - Bacillus subtilis strain is preserved in China Center for Type Culture Collection (CCTCC NO: M2014649), is new.    USE - Bacillus subtilis strain used in manure and sewage treatment (claimed).    ADVANTAGE - The Bacillus subtilis strain reduces garbage and sewage stench by reducing generation of ammonia, hydrogen sulfide, and hydrocarbon gas by 95%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biological deodorant, which includes Bacillus subtilis strain.
NOVELTY - Microbial inoculum comprises low efficiency cellulose degrading bacteria, starch degrading bacteria, protein degrading bacteria and sugar degrading bacteria in a volume ratio of 1:1:1:1.    USE - The microbial inoculum is useful for degrading household garbage (all claimed).    ADVANTAGE - The inoculum degrades household garbage efficiently under low temperature condition, reduces household garbage fermentation period, and improves conversion efficiency of garbage.    DETAILED DESCRIPTION - Microbial inoculum comprises low efficiency cellulose degrading bacteria, starch degrading bacteria, protein degrading bacteria and sugar degrading bacteria in a volume ratio of 1:1:1:1, where the low efficiency cellulose degrading bacteria comprises Arthrobacter sp., Flavobacterium sp., and Sphingobacterium sp. in a volume ratio of 1:3:2, the starch degrading bacteria comprises Flavobacterium sp., Aeromonas sp., and Arthrobacter sp. in a volume ratio of 1:2:3, the protein degrading bacteria comprises Kurthia sp., Moraxella sp., and Klebsiella sp. in a volume ratio of 1:1:1, and the sugar degrading bacteria comprises Shigella sp., Pseudomonas sp., Morganella sp., Burkholderia sp. and Pseudomonas sp. in a volume ratio of 1:1:1:1:1. INDEPENDENT CLAIMS are included for the following:    (1) method for preparing the inoculum involves (a) performing dilution coating, marking and isolation of subculture, and screening degrading bacteria from subculture, and (b) adjusting bacterial suspension turbidity of low efficiency cellulose degrading bacteria, starch degrading bacteria, protein degrading bacteria and sugar degrading bacteria until optical density (OD) 600 value reaches 1.9-2.1, and mixing low efficiency cellulose degrading bacteria, starch degrading bacteria, protein degrading bacteria and sugar degrading bacteria in a volume ratio of 1:1:1:1; and    (2) use of microbial inoculum for degrading household garbage.
NOVELTY - Method for controlling Mythimna separata pests, involves contacting the M.separata pests with pesticidal crystal protein (Cry)2Ab protein.    USE - The method is useful for controlling M.separata pests in plant and producing transgenic plant. The plant is corn, soybean, rice, wheat, Sorghum, millet, barley or forage grass (all claimed).    ADVANTAGE - The method provides pest protection for whole growth period, is pollution-free, residual-free and stable, and is performed simply, conveniently and cost-effectively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) use of Cry2Ab protein, for controlling pest; and    (2) method for producing a transgenic plant.
NOVELTY - Constructing engineered bacterial strain comprises: (a) inserting gene encoding desired protein into multiple cloning site of pET-30a(+) vector to give recombinant plasmid pET30-panDB, where desired protein comprises fully defined 127 amino acids (SEQ ID NO. 6) given in the specification; and (b) introducing recombinant plasmid pET30-panDB into Escherichia coli BL21 (DE3) to give the engineered bacterial strain.    USE - The method is useful for constructing engineered bacterial strain. The engineered bacterial strain or recombinant plasmid is useful for producing beta -alanine (all claimed).    ADVANTAGE - The method for producing beta -alanine does not need the used of inducer; does not need high-temperature and high pressure; has mild condition, simple operation; is environment-friendly; and can achieve industrial application level.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a recombinant plasmid pET30-panDB comprising the gene encoding desired protein inserted into multiple cloning site of pET-30a(+)vector; and    (2) a method for producing beta -alanine comprising taking L-aspartic acid as substrate; and using the engineered bacterial strain for biological conversion.
NOVELTY - The utility model claims a... of suction type gasification furnace biomass rubbish guide device, with a platform at top end of solid garbage gasification furnace, wherein a side of a platform in a garbage gasification furnace arranged to contact with a greater than equal to 3 and fuel gas passage, a platform and a surface close to the periphery with a number equal to a gas rising pipe, gas channel and gas rising tube of 3 are connected, with a rib adjacent a gas rising tube in between. Inwards inclined angle alpha with the gas rising tube inclined section b and a terminal connected on a vertical section a, upper end of inclined section b and a bottom fuel gas collector connected the inner cavity, with header with a safety valve, a side wall installed with downward inclined gas output pipe on the top end of gas collector. The device of using combustion of garbage gasification furnace of household garbage in the generation of rough gas can uniformly rising transporting a gas collector for primarily cooling collection purification, the product of biomass tar. relux a garbage gasification furnace for the second time, environmental protection effect is good.
NOVELTY - The utility model claims a new oxygen internal combustion of biomass industrial gasification furnace system, comprising a hypoxia internal combustion of the biomass gasification furnace main body, wherein the bottom of the gasification furnace main body present dispersing shape formed with a combustion port number, a lower part provided with a discharging pipe of the layer set with heat preservation wall in a furnace wall of the gasification furnace main body, a heat insulating wall provided with several lengthways and a fuel gas channel, and also is provided with a plurality of connected a fuel gas channel and fuel gas flow way hole space in the furnace heat preservation of wall, also equipped with is equipped with pusher connector pusher connector with a pusher on a furnace wall of gasification furnace main body, top part of the gasification furnace main body set with barrel, provided with fuel gas outlet on a top part and side, provided with a separate air inclined plate between a gasification furnace main body internal, barrel and fuel gas outlet, also equipped with a pressure monitor on top part of the gasification furnace main body. The utility model is a new gas stable, pure gas degree high, stable, gas pipe is smooth, not easy to be blocked safety coefficient a, using life long.
NOVELTY - The utility model claims a new kind of biomass gasification furnace, comprising furnace body and furnace cover, a furnace body of outside cylinder and inside cylinder one, the inner cylinder upper end is provided with a feeding port, a furnace cover for sealing the feeding port, the inner cylinder inner cavity is a cavity, the inner tube outside wall and outside cylinder inner wall set with air in between, the inner cylinder upper end is a week wall set with connected the first out gas in the air hole, a cylinder and a lower end provided with an igniter, a gas in a set with a gas outlet, the inner cylinder lower part and a week wall equipped with the air cavity and a second air outlet connected. The biomass gasification furnace generation time in use of tar, increase of a combustion gas and conversion rate, reducing a tar to and pollute environment.
NOVELTY - The utility model claims a new low tar produced is a kind of biomass gasification furnace, comprising furnace body and furnace cover, a furnace body of outside cylinder and inside cylinder one, the inner cylinder upper end is provided with a feeding port, a furnace cover for sealing the feeding port, the inner cylinder inner cavity is a cavity, the inner tube outside wall and outside cylinder inner wall set with air in between, the inner cylinder upper end is a week wall set with connected the first gas a gas in and out of the cylinder and a lower end provided with an igniter, a gas in a set with a gas outlet, the inner cylinder between outside wall and outside cylinder inner wall is set with a separating plate 2 more than block, a partition plate for the air cavity is divided into a partition of 2 more than one, said lower cylinder part is within a week wall provided with the connected air cavity and the second air outlet hole and a cavity. The biomass gasification furnace generation time in use of tar, increase of a combustion gas and conversion rate, reducing a tar to and pollute environment.
NOVELTY - The utility model claims a new tar cracking rate a is a kind of biomass gasification furnace, comprising furnace body and furnace cover, a furnace body of outside cylinder and inside cylinder one, the inner cylinder upper end is provided with a feeding port, a furnace cover for sealing the feeding port, the inner cylinder inner cavity is a cavity, the inner tube outside wall and outside cylinder inner wall set with air in between, the inner cylinder upper end is a week wall set with connected the first out gas in the air hole, a cylinder and a lower end provided with an igniter, a gas in the air outlet provided with a, also including outside cylinder is set on outside wall of back , lower end of the back connected back entrance is set with a air outlet structure, and the back end of provided with back outlet. The biomass gasification furnace using a pass back to produce the coke oil for quadratic splitting, a discharge amount of tar reducing at last, thus reducing a tar to and pollute environment.
NOVELTY - The utility model claims a new novel of coal furnace, comprising a furnace body, a water supplement pipe, blast pipe, hot air pipe and water discharging pipe, a water supplement pipe and water discharging pipe are a body of water in a via hole, a wind pipe set with a wind valve, a blast pipe and a furnace body and fire hole connect, the hot air pipe connected body upper end and lower end, a novel coal, coal not directly burning, water seal product gas, a heat reach to the highest, full coal combustion and heat supply in time and make the production need and has a; tar material directly participate combustion, there is no trouble of tar blockage pipeline without machine fault cause a production, to increase of economic value.
NOVELTY - The dry dust remover in spraying dust remover and a pit of a can for purification by heating a biomass in a gas station, a pit in the gasification furnace and the gas dry dust remover in a, in a gasification of a fuel gas transport pipe connection, a high temperature device far from a personnel to prevent scald accident happen, in order to meet in purification heating need, sealing sleeve of a fuel gas transporting pipeline between the spray-type dust remover and dry dust remover, wherein a... has air inlet pipe and air outlet pipe, a air inlet pipe by a axial-flow fan for outdoor cold air in sealing sleeve for heat exchange, heat exchange of hot air form again via a wind pipe leading in purification, to realize the heating in purification, low in heat exchanging effect, gas transporting pipe not sufficient to reach to red heat state, slow down aging speed of the gas transporting pipeline, so as to reduce a gas transport pipe show the damage rate to reduce a safety accident is happen.
NOVELTY - The utility model claims a new plant biomass stove system, between a gasification furnace and combustion stove, the gasification furnace and burning furnace connected with the gas pipeline, the gasification furnace for biomass fuel by a combustion reaction prepared biomass fuel gas, of the prepared biomass fuel gas. transport to carry out burning oven using a combustion gas pipeline. The utility model a biomass stove system as a biomass fuel prepared biomass fuel gas for combustion use, clean, sanitary, a, implement a common application of biomass fuel, a system using a gasification furnace of small size, small matching combustion stove, the can is suitable for family or restaurant use, and is suitable for industrial application of the traditional large gasification furnace, the new utility model solves a technology of gasification furnace miniaturization difficulty, but also a problem of small gasification furnace directly using a pharmaceutical substance in fuel gas and technology blank, a biomass to a more extensive technique is applied, a biomass fuel to obtain more full...
NOVELTY - The utility model claims a.... hydrogen production by reforming methanol fuel cell electric motor car ship, a methyl alcohol water hydrogen production by reforming fuel cell power generation system, a methanol water hydrogen production by reforming power generation, which avoids the danger of carrying high pressure hydrogen, carrying turn safety of methanol water, and the same quality condition below, is carrying more and more hydrogen, which solves the existing technology of high pressure hydrogen storage not only dangerous hydrogen storage then no more a problem, mainly applied in a ship area.
NOVELTY - Preparation of nickel sulfide/nickel hydroxide electrocatalyst involves providing 5 mM nickel chloride hexahydrate and 0.3 M thiourea solution as bath, pre-treated indium-tin oxide as working electrode, 0.3 M silver/silver chloride as reference electrode and platinum mesh as counter electrode, placing working electrode in bath, placing reference and counter electrode in 0.1 M sodium sulfate, and carrying out light-assisted electrodeposition using cyclic voltammetry, with scan rate of 5 mV.second-1 and scanning voltage of -1.2 V to 0.2 V. The light source is Xenon lamp.    USE - Preparation of nickel sulfide/nickel hydroxide electrocatalyst used in water-splitting hydrogen production.    ADVANTAGE - The method enables preparation of nickel sulfide/nickel hydroxide electrocatalyst having excellent activity and stable performance, and Faradaic efficiency of 100% and sustainable response for 22 hours in neutral electrolyte.
NOVELTY - The system has a temperature-type solar energy absorb pyrolysis reactor (1) for processing pyrolysis reaction of solid carbon hydrogen fuel (a) for obtaining tar, coke and hydrocarbon gas mixture product (b). The tar, coke and hydrocarbon gas mixture product is sent into a high temperature rotary solar energy gasification reactor (2). High temperature water vapor (e ') is discharged to the gasification reactor to obtain gasifying agent participate in gasification reaction after cooling high temperature synthesis gas (c ') sent to a gas purification device (5) for depth purification treatment.    USE - Slot-tower combined condensing based solar energy biomass gasification system.    ADVANTAGE - The system has high biomass gasification efficiency, and reduces gasification gas and tar content.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a slot-tower combined condensing based solar energy biomass gasification system.    Solid carbon hydrogen fuel (a)    Hydrocarbon gas mixture product (b)    High temperature synthesis gas (c')    High temperature water vapor (e')    Temperature-type solar energy absorb paralysis reactor (1)    High temperature rotary solar energy gasification reactor (2)    Gas purification device (5)
NOVELTY - The system has a gasification furnace whose outlet is connected with an entrance end of a gas-solid separating device. The gas-solid separating device is connected with a combustion furnace. The gasification furnace is connected with a fluidization wind machine. A lower part of the fluidization wind machine is provided with a main air blowing part. An upper part of the fluidization wind machine is fixed with another fluidization wind machine. The gasification furnace is arranged with a water steam transport mechanism.    USE - Biomass solid waste and dangerous waste pyrolysis gasification system.    ADVANTAGE - The gas-solid separating device separates semi-coke solid material, so that the solid material enters into a return device and wind enters into the gasification furnace so as to complete circulation process at combined furnace temperature and pressure and adjust circulation times. The gas-solid separating device allows high-temperature gas to enter into the gasification furnace so as to increase pyrolysis gasification degree and increase different material gasification efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass solid waste and dangerous waste pyrolysis gasification system.
NOVELTY - The system has a solid feeding system body connected with a feedstock that is connected with a gasification furnace part. A front storage hopper is connected with a feeding machine that is fixed with a flame part. The flame part is fixed with a breaking valve. The feeding machine is a fixed with a temperature measuring device that is connected with a break valve. The feeding machine determines access speed. An inner cavity is fixed with the gasification furnace part. The feeding system body is fixed with a transporting pump.    USE - Biomass solid dangerous waste feeding system.    ADVANTAGE - The system increases urgency discharging efficiency, safety performance and protection efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass solid dangerous waste feeding system. '(Drawing includes non-English language text)'
NOVELTY - Production of liquid fertilizer and co-products involves reducing size of composting excessive organic substance, adding organic substance at fixed ratio into methane fermentation digestive liquid in a tank, composting liquid mixture of the organic substance, stirring methane fermentation digestive liquid, aging the stirred liquid, fractionating byproduct with a final product, and collecting liquid fertilizer and co-products from excessive organic substance.    USE - Production of liquid fertilizer e.g. liquid manure and co-products e.g. earthworm culture medium feed used as raw material for manufacturing earthworm compost, and grub used as aquatic animal feed (all claimed).    ADVANTAGE - The method enables efficient production of liquid fertilizer, by simple and economical process.
NOVELTY - The apparatus has a micro-controller (1) provided with an IIC connector (4), an analog I/O interface (5), a digital I/O interface (12), a Bluetooth module (3) and a series communication interface (6). A detector (11) is connected with the analog I/O interface. The mobile terminal is provided with a GPRS module, a GPS module and a key. The Bluetooth module is connected with a crop canopy information detecting module and a core plate. The GPRS module transmits timing and position information to a remote server.    USE - Crop nitrogen nutrition diagnostic apparatus.    ADVANTAGE - The apparatus realizes quick non-destructive crop plant nitrogen concentration, biological quantity, nitrogen nutrient index, point longitude and latitude, crop nitrogen nutrient deficiency and fertilization detecting process, ensures precise crops fertilizer management performance, increases fertilizer utilization ratio and decreases environment pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of a crop nitrogen nutrition diagnostic apparatus.    Micro-controller (1)    Bluetooth module (3)    IIC connector (4)    Analog I/O interface (5)    Series communication interface (6)    Detector (11)    Digital I/O interface (12)
NOVELTY - Mixing borneol with plant proteins in the presence of solvents, comprises: providing a borneol solution in either acetone or ethyl alcohol; mixing the borneol solution with at least one plant protein, where the mixing step being conducted by kneading; drying the mixture; and milling the mixture in order to obtain a powder. The plant protein comprises at least one of the substances comprising cereal proteins and non-cereal proteins, and the solvents comprise at least one of the substances comprising either acetone or ethyl alcohol.    USE - The process is useful for preparing a powdered mixture of borneol and plant proteins to be used as dietary or food supplements for the improvement of the permeability of the blood-brain barrier (all claimed) which is useful for treatment of CNS illness comprising Alzheimer's disease, stroke cerebral ischemia, cerebritis and cerebral edema, depression and insomnia. No biological data given.    ADVANTAGE - The process: utilizes borneol combined with plant proteins, which tightly binds to the protein moiety and becomes more stable and more bioavailable (claimed); is economical and does not requires costly equipment; and consumes a relatively low amount of energy, does not pollute the environment and uses relatively low temperatures (20-25 degrees C) for the mixing and drying phases.
NOVELTY - This new utility model claims of one of gasification furnace cover furnace, comprising furnace body and cover body, upper part set with the limit switch, one end cover of the furnace body and between through horizontal rotate shaft connected with, the other end is connected with cover hanging body, upper end face of cover body is set with fixing bar, the fixing bar is vertical to the middle position and horizontal rotate shaft, a limiting switch equipped with two of the edge of cover body is equipped with two to three blocking bars, position limiting switch and the baffle corresponding to the cover body to cover furnace body over time, probe pressure limiting switch and lower occulting bar. This new utility model has the advantages and positive effect is: using this utility new type of furnace cover, can prevent the whole single limit switch is damaged, but can not stop in time open action of furnace cover, if one single limit switch is damaged, also can use the other one, and damage the limit switch will maintain or change in time, not influence normal work.
NOVELTY - The utility model claims a... high-efficient fluidization bed biomass gasification device, comprising a cracking chamber and fluidization bed main body, a bottom splitting chamber and extends into the spiral feeding machine is provided with a fluidization bed main body part, a cracking chamber and fluidization bed main body top part and a fuel gas channel connected with, a part of cracking chamber is set with storage bin, top part of fluidization bed main body provided with gasification medium pre-heater and a gasification medium pre-heater connected input gasification medium is fan, bottom of the gasification medium via input fluidization bed main body after gasification medium. The high efficient fluidization bed biomass gasification device for producing a fluidization bed of biomass fuel gas gradually cool to discharging use, and make the heat biomass fuel gas cooling process in a preheat gasification medium heat exchange device and a cracking biomass raw material, a. maximum energy utilization rate of the utility model is a model used for biomass gasification and purification technology area.
NOVELTY - The utility model claims a new biomass gasification furnace of a lighter, comprising a base, a seat and a seat chamber is set with lower end opening, the top end of the base chamber set with heater through hole and the first wind outlet hole, a heater installed in the indoor base, and upper end of heater through outside of the heater through hole exposed base. And the existing technology, this utility new type biomass gasification furnace of a lighter construction is simple, the ignition success rate high.
NOVELTY - The utility model claims a new variable process of desulfurization device, comprising a first tower in parallel at feed gas import and product gas outlet between the, the second, and the third and the fourth tower, through a valve and pipeline directly connected with feed gas and product gas outlet between import, the first, the second, and the third tower and air inlet and air outlet of the fourth tower and equipped with valve, the air outlet of the first desulfurizing tower by a valve with the pipeline a and the second desulfurizing tower, desulfurizing tower and a third desulfurizing tower is connected with air inlet, the air outlet and the third desulfurizing tower by a valve with the pipeline a and the first, the second, and the fourth air inlet connected with desulfurizing tower. The utility model can realize a at least two platform remove sulfur tower series parallel connection switching operation, a single operation, remove sulfur tower data. According to the needed processing quantity corresponding increase, for a gas and biomass raw material gasification generating organic sulfur is effective.
NOVELTY - The utility model claims a a a a tunnel harmful gas detection system, the oxygen between sensor, carbon monoxide sensor, vulcanization hydrogen sensor, methane sensor and a signal connecting device, said detecting device signal a collective monitoring centre and GSM, collective monitoring centre connected with alarm signal interaction input device, storage centre and GSM, the GSM7 connected with signal receiving terminal, a link detecting system signal connected with oxygen sensor, carbon monoxide sensor, vulcanization hydrogen sensor, methane sensor, a device, a collective center, GSM, receiving terminal, alarm interaction input device and storage center. A. connecting relation is simple and effective for the harmful gas in the tunnel by a time monitoring, effect is good, a message, response speed is fast.
NOVELTY - The electrolyzer has case in which electrodes in the form of plates are arranged. The positive and negative electrodes are electrically connected to power supply. The electrolyte is filled in cavities communicated with container. A source of ultrasonic emission into electrolyte is placed in the case. A water seal is communicated with electrolyte cavity of container. The outputs of channels are arranged on opposite housing walls of electrolyzer. The positive and negative electrodes are covered with nickel layers on all sides. A nickel oxide layer is covered on the negative electrodes.    USE - Electrolyzer for obtaining gaseous mixture of hydrogen and oxygen.
NOVELTY - A recombinant host cell comprising a deletion or insertion or other alteration in the beta -glucosidase (bgl7) gene which inactivates the gene and prevents BGL7 polypeptide production is new.    USE - The recombinant host cell is useful for producing a polypeptide or composition. The composition is used for cleaning and for hydrolyzing a lignocellulosic biomass substrate (all claimed). The composition is used in household detergents, stonewashing compositions or laundry detergents, etc.    ADVANTAGE - New and improved cellulase compositions are provided. The cellulases exhibit resistance to surfactants, improved performance under conditions of thermal stress, increased or decreased cellulolytic capacity, and/or high level expression in vitro.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) an antisense oligonucleotide complementary to a messenger RNA that encodes a BGL7 polypeptide having a defined sequence of 740 amino acids (SEQ ID NO. 2), given in the specification, where upon exposure to a beta -glucosidase-producing host cell, the oligonucleotide decreases or inhibits the production of beta -glucosidase by the host cell;    (2) a composition produced by cultivating the recombinant host cell defined above under suitable fermentation conditions to produce proteins;    (3) a method of applying the composition of (2) for cleaning; and    (4) a method of hydrolyzing a lignocellulosic biomass substrate using the composition of (2).
NOVELTY - A carbon material has specific gravimetric methane adsorption of 0.13 g/g or more at room temperature and 50 bar pressure.    USE - Carbon material used in device for storage of gas (all claimed) e.g. low-pressure methane and natural gas.    ADVANTAGE - The carbon material has high packing ratio and improved gas adsorption properties.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) composition, which comprises gas storage particles having packing efficiency of 80% or more;    (2) gas storage device, which has the carbon material;    (3) storage of gas, which involves charging a gas to the gas storage device, and storing the gas at a pressure more than the atmospheric pressure; and    (4) composition, which comprises the carbon material and gas.
NOVELTY - The flow control valve (10A) has the first and second diaphragms (30,35) whose forward and return movement arose by pressure fluctuation of an aperture portion (15) is transmitted to a mutual diaphragm through rotation of a seesaw portion (80) contacted with the first and second rod-shaped movable portions (40,50). A valve portion (38) is moved back and forth with respect to a valve seat (16) through the forward and return movement of the first and second diaphragms, and the flow volume of the to-be-controlled fluid is kept uniformly.    USE - Flow control valve of flow control apparatus (claimed) used for semiconductor manufacturing plant, semiconductor manufacturing apparatus, fuel cell manufacturing field and medical field.    ADVANTAGE - Since the valve portion is moved back and forth with respect to the valve seat through the forward and return movement of the first diaphragm and second diaphragm and the flow volume of the to-be-controlled fluid is kept uniformly, the unexpected contact of the valve seat and valve portion is suppressed, and constant flow is maintained for the purity degree of the fluid in a higher state. The change of the setting of the circulating fluid flow amount area is enabled, and concentration of the apparatus is advanced. Smooth connection state of each movable portion and seesaw portion is maintained. The structure of the flow control valve is simplified at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a flow control apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the flow control valve.    Flow control valve (10A)    Aperture portion (15)    Valve seat (16)    Diaphragms (30,35)    Valve portion (38)    Rod-shaped movable portions (40,50)    Seesaw portion (80)
NOVELTY - An alloy electrode is obtained by coating alloy composition containing 45-65 atomic% (excluding 45 atomic%) iron, 0.6-10 atomic% carbon, 5 atomic% or more nickel and 0.1 atomic% or more cobalt, on metal electrode base material.    USE - Alloy electrode is used in electrolysis of aqueous alkali solution for producing hydrogen.    ADVANTAGE - The alloy electrode has excellent activity, corrosion resistance and durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of alloy electrode.
NOVELTY - The gasification reaction apparatus (10) has a gasification chamber (11) in which a heat transfer material (HT) having catalytic function with water or water vapor is accommodated in an inner side and the gasification raw material (M) is supplied. A stirring unit (30) for stirring heat transfer material is accommodated in the interior of gasification chamber. A circulation path (12) through which heat transfer material circulates, is connected with the gasification chamber.    USE - Gasification reaction apparatus used for gasifying gasification raw material containing carbon compound such as biomass including wood type biomass, cellulose waste material, garbage, organic refuse, industrial foodstuff waste, etc.    ADVANTAGE - A lot of efficient reaction heat can be supplied to the gasification raw material, and the high reaction efficiency is acquired.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the gasification reaction apparatus.    Gasification reaction apparatus (10)    Gasification chamber (11)    Circulation path (12)    Stirring unit (30)    Heat transfer material (HT)    Raw material (M)
NOVELTY - Waste water is treated in a fluidized bed bioreactor which involves: (a) adding electrically conductive particles to the solution present in the bioreactor, where the particles are fluidized in the solution; (b) adding a suspension of bacteria from Geobacter genus in the bioreactor; and (c) oxidizing the organic matter present in waste water in the presence of the particles and the bacteria from Geobacter genus.    USE - The method is useful for treating waste water in fluidized bed bioreactor.    ADVANTAGE - The main advantages of the method comprise: (a) enhancement of biodegradation rates of organic matter by combining the availability of an un-limited electron acceptor (fluidized bed) and the exocellular electron transfer ability of Geobacter; (b) the biodegradation rate is not limited to those cells just forming a biofilm as typically exist in microbial fuel cell applications. Instead, all the cells in solution can participate in the process; (c) minimizing the biomass production due to the lower growth yield of electrogenic bacteria (Geobacter); (d) in situ monitoring of the biodegradation rate on real time through electric current measurement; and (e) no production of greenhouse gas (no or low methane production).
NOVELTY - The apparatus has an intermediate transport medium portion which is provided with intermediate transport medium which conveys a different intermediate from one substance and provided with several intermediate transport medium pillar portions. The one transport medium arrangement portion is made follow substance transportation direction and is arranged while making one transport medium contact the space formed between the intermediate transport medium pillar portions. One cavity is formed as a space (18A,18B) with intermediate transport medium and one transport medium.    USE - Electrochemical reaction apparatus for use as fuel cell, water-electrolysis apparatus, hydrogen production apparatus, secondary battery and gas sensor.    ADVANTAGE - The secondary battery is charged, or water-electrolysis apparatus is optimized. The interface reaction is optimized and efficiency is improved while controlling the interface reaction. The efficiency of the electrochemical reaction apparatus is improved. The substance transport of oxide ion, electron and gas is achieved. The efficiency of the electrochemical reaction of electrochemical reaction apparatus is increased by reducing the transport loss of the substance in electrochemical reaction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of electrochemical reaction apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the fuel electrode of fuel cell.    Fuel electrode (1)    Electrolyte layer portion (3)    Current collection layer (5)    Spaces (18A,18B)    Three-phase interface (19)
NOVELTY - An ethanol producing microbe comprising deleted or inactivated NAD+-dependent deacetylase gene and fructose-1,6-bisphosphatase 1 (FBP1) gene, is new.    USE - As ethanol producing microbe.    ADVANTAGE - The microbe has 10 times or more ethanol producing ability compared to yeast strains.
NOVELTY - Jamun oil biodiesel made from jamun seed, is claimed. The jamun oil biodiesl is an alternative fuel formulated exclusively for diesel engines.    USE - The jamun oil biodiesel is useful: for diesel engines; as fuel in direct or indirect injection diesel engine; and as fuel for homogenous charge compression ignition engine as direct or port injected fuel (all claimed).    ADVANTAGE - The jamun oil biodiesel blend: provides fuel in direct or indirect injection diesel engine with or without modification to the compression ratio or injection pressure (claimed); and increases the efficiency of the diesel engine, and reduces the engine exhaust emission.
NOVELTY - An asymmetrical gas separation membrane is formed using soluble aromatic polyimide comprising polyimide repeating unit (I).    USE - Asymmetrical gas separation membrane is used for selectively separating and recovering specific gas from mixed gas e.g. nitrogen-rich gas from air, carbon dioxide gas from mixed gas of carbon dioxide and methane, hydrogen gas from mixed gas of hydrogen gas, and steam from gas containing steam for humidifying and recovering dehumidified gas (all claimed).    ADVANTAGE - The asymmetrical gas separation membrane has excellent gas-separation performance and mechanical strength, and high gas-separation coefficient.    DETAILED DESCRIPTION - An asymmetrical gas separation membrane is formed using soluble aromatic polyimide comprising polyimide repeating unit of formula (I).    A=10-95 mol% tetravalent unit based on biphenyl structure of formula (i), or 5-50 mol% tetravalent unit based on phenyl structure of formula (ii);    B'=40-90 mol% bivalent unit of formula (iii) and/or bivalent unit of formula (iv), or 10-60 mol% bivalent unit of formula (v);    R,R'=H or organic group;    n=0-2;and    X=-CH2- or -CO-.
NOVELTY - A metal complex is obtained by reacting carboxylic compound which is capable of bidentate coordination(s), zirconium ions and organic ligand capable of bidentate coordination at a nitrogen site with the zirconium ions.    USE - Metal complex is used for material for occluding and adsorbing organic vapor e.g. carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, 1-4C hydrocarbon, noble gas, hydrogen sulfide, ammonia, sulfur oxide, nitrogen oxide, siloxane, water vapor, toluene, alcohol and aldehyde, and separating organic vapor e.g. carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, 1-4C hydrocarbon, noble gas, hydrogen sulfide, ammonia, sulfur oxide, nitrogen oxide, siloxane, water vapor, toluene, alcohol, aldehyde, methane, ethane, ethylene and formaldehyde (all claimed) during deodorizing and purification of air, gas and water.    ADVANTAGE - The metal complex is environmentally-friendly, and has excellent stability even at high temperature and high humidity, and durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of metal complex.
NOVELTY - The method involves plasticizing particulates of biomass by squeezing or crushing. The particulates are mixed with calcium oxide and hydrated lime. Concentration of 20-60 percent of carbon powder is determined. Obtained mixture is compressed in a granulator palette or logs. Granulate fuel is cooled.    USE - Method for preparing granules of biomass.
NOVELTY - Carbonyl compound (I) is reacted with sulfur compound in presence of salt of lanthanoid metal to obtain thiolane/thiane ring-containing compound (II).    USE - Manufacture of thiolane/thiane ring-containing compound used for manufacturing thionucleoside e.g. 1-(2-deoxy-2-fluoro-4-thio- beta -D-arabinofuranosyl) cytosine and 1-(4-thio- beta -D-arabinofuranosyl) cytosine.    ADVANTAGE - The method provides thiolane/thiane ring-containing compound with high yield, by simple, economical and environmentally-friendly process.    DETAILED DESCRIPTION - Carbonyl compound of formula (I) is reacted with sulfur compound in presence of salt of lanthanoid metal to obtain thiolane/thiane ring-containing compound of formula (II).    R1=H, or alkyl or aryl (both optionally substituted);    X=leaving group;    Q1,Q3=optionally substituted methylene, -C(=O)- or -C(=C(Ra1)(Ra2))-;    Q2=single bond, or Q1;and    Ra1,Ra2=H or substituent.
NOVELTY - An amide compound (I), is new.    USE - New amide compound is used as extraction solvent for separating saturated aliphatic hydrocarbon, unsaturated aliphatic hydrocarbon, and aromatic hydrocarbon from hydrocarbon mixture by extractive distillation (all claimed).    ADVANTAGE - The amide compound provides solvent for separating saturated aliphatic hydrocarbon, unsaturated aliphatic hydrocarbon, and aromatic hydrocarbon with high extraction efficiency and high safety.    DETAILED DESCRIPTION - An amide compound of formula (I), is new.    R1=linear, branched or cyclic 1-6C alkyl;    R2=linear or branched 1-6C alkyl;and    n=0-2.    INDEPENDENT CLAIMS are included for the following:    (1) extraction solvent; and    (2) separation of hydrocarbon mixture, which involves separating saturated aliphatic hydrocarbon (a), unsaturated aliphatic hydrocarbon (b), and aromatic hydrocarbon (c) using extraction solvent.
NOVELTY - Laundry wastewater biological treatment formulation comprises freeze-dried sludge which is formed by washing and freeze-drying activated sludge which is acclimatized using laundry wastewater, and adding activated sludge which is processed using laundry wastewater to biological treatment formulation and covering using cloth.    USE - As laundry wastewater biological treatment formulation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) laundry wastewater processing apparatus; and    (2) laundry wastewater processing method.
NOVELTY - Polypeptide with laccase activity comprising an amino acid sequence that is at least 60% identical to the amino acid sequence of SEQ ID NO: 1, where the polypeptide comprises an alanine residue at a position corresponding to amino acid 260 of SEQ ID NO: 1, is new.    USE - The polypeptide is useful in an application comprising pulp delignification, degrading or decreasing the structural integrity of lignocellulosic material, textile dye bleaching, wastewater detoxification, xenobiotic detoxification, production of a sugar from a lignocellulosic material and recovering cellulose from a biomass (claimed) as biocatalysts.    ADVANTAGE - The polypeptide: exhibits improved properties and laccase activity; is eco-friendly; and is produced by a method that results in higher productivity in shorter time and reduces the costs of production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) nucleic acid encoding the polypeptide;    (2) a vector comprising the nucleic acid;    (3) a composition comprising the nucleic acid or the vector;    (4) a recombinant host cell comprising the nucleic acid, the vector or the composition;    (5) a method (M1) for producing the polypeptide; and    (6) a method (M2) for improving the yield of a polypeptide with laccase activity in a heterologous expression system comprising the step of altering the amino acid at a position corresponding to position 260 in SEQ ID NO: 1 to an alanine residue.
NOVELTY - Manufacture of 1,4-cyclohexanedicarboxylic acid dichloride involves mixing and reacting 1,4-cyclohexanedicarboxylic acid with thionyl chloride using reaction liquid of front batch in the absence of solvent, and producing 1,4-cyclohexanedicarboxylic acid dichloride.    USE - Manufacture of 1,4-cyclohexanedicarboxylic acid dichloride used as monomer for synthetic resins, resin additive raw material, and pharmaceutical intermediate material.    ADVANTAGE - The method enables manufacture of 1,4-cyclohexanedicarboxylic acid dichloride with high purity and reduced generation of impurities from reaction solvent or catalyst, without requiring excess chlorinating agent, by environmentally-friendly process.
NOVELTY - Carotenoid is extracted from biomass by one or more solvent (I), washed with an aqueous solution of Bronsted acid and optionally washed with one or more solvent (II) which is not miscible with solvent (I). The obtained solution which comprises the carotenoid is optionally dried, in the isolation of carotenoid from carotenoid-producing bio-organism.    USE - Isolation of carotenoid from carotenoid-producing bio-organism is used in production of feed products, food products, pharmaceutical products and personal care products for e.g. exhibiting antioxidant property.
NOVELTY - Preparation of crude bio-oil involves preparing a biomass slurry, adding catalyst(s) chosen from ionic liquids and surfactants to the biomass slurry to obtain a mixture, heating the mixture at 200-350 degrees C and 70-250 bars pressure for 10-180 minutes to obtain a mass containing crude bio-oil and separating the crude bio-oil from the mass to obtain a separated crude bio-oil and an aqueous phase containing the catalyst.    USE - Preparation of crude bio-oil used as biofuel.    ADVANTAGE - The method is a simple, energy-efficient, time-saving and high-yielding. The method provides bio-oil which is compatible with petroleum crude used in a refinery. The presence of surfactant enables efficient cell wall rupturing which results in the extraction of more oil components. The catalyst in the process is recovered and can be reused.
NOVELTY - Producing xylitol and another fermentation product from lignocellulosic biomass, involves: (a) extracting hemicelluloses from a feedstock comprising lignocellulosic biomass, where the hemicelluloses include xylose oligomers and other sugar oligomers; (b) hydrolyzing the xylose oligomers and the other sugar oligomers, to generate xylose and other sugar monomers, respectively, using an acid catalyst or enzymes; (c) fermenting the other sugar monomers to a first fermentation product, using a suitable first microorganism.    USE - The process is useful for producing xylitol and another fermentation product from lignocellulosic biomass (claimed).    ADVANTAGE - The process is highly improved and can be efficiently used in the field of biorefining, preferably in the production of xylitol and another fermentation product from lignocellulosic biomass.    DETAILED DESCRIPTION - Producing xylitol and another fermentation product from lignocellulosic biomass, involves: (a) extracting hemicelluloses from a feedstock comprising lignocellulosic biomass, where the hemicelluloses include xylose oligomers and other sugar oligomers; (b) hydrolyzing the xylose oligomers and the other sugar oligomers, to generate xylose and other sugar monomers, respectively, using an acid catalyst or enzymes; (c) fermenting the other sugar monomers to a first fermentation product, using a suitable first microorganism; (d) optionally removing at least some of the first fermentation product; (e) fermenting the xylose to a second fermentation product comprising xylitol, using a suitable second microorganism; (f) recovering the first fermentation product, derived from step (c) and/or, if conducted, step (d); and (g) recovering the xylitol derived from step (e).
NOVELTY - Producing pulp product, comprises: (a) converting first biomass feedstock to first pulp stream at biorefinery site, where the first biomass feedstock comprises woody cellulosic material; (b) converting second biomass feedstock to a second pulp stream at the biorefinery site, where the second biomass feedstock comprises non-woody cellulosic material; (c) blending at least a portion of the second pulp stream, or its treated form into the first pulp stream, thus generating a blended pulp stream; and (d) recovering or further processing at least some of the blended pulp stream as pulp product.    USE - The process is useful for producing pulp product.    ADVANTAGE - The process is cost-effective, and improves final pulp product life-cycle profile compared to pulp product derived solely from the first biomass feedstock.
NOVELTY - The device has a ferment shed whose top end is connected with a ventilating pipe. An end of the ventilating pipe is installed with an adjustable fan. A bottom part of the ferment shed is provided with an air inlet sampling point. A tail end of an air tube is connected with an exhaust port sampling point, where the air inlet sampling point and the exhaust port sampling point are mounted with a sample machine. The ferment shed is composed of a frame that is detachably and independently moved to change length of the ferment shed for different stacks.    USE - Excrement compost processing unit releasing gas collecting device.    ADVANTAGE - The device increases result accuracy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an excrement compost processing unit releasing gas sampling method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an excrement compost processing unit releasing gas collecting device.
NOVELTY - A plant with a a gas methane recycling device, the device comprising a gas pipeline industry, chemical industry gas pipeline connected with a pre-cooling heat exchanger, a pre-cooling heat exchanger connected with rectifying tower and one heat exchanger, heat exchanger connected with one cryogenic heat exchanger, cryogenic heat exchanger connected with hydrogen separator and feedstock port, discharge port and separator hydrogen pressure controlling valve in turn by a cryogenic heat exchanger, pre-cooling heat exchanger and a hydrogen pipeline, a hydrogen separator and a cryogenic heat exchanger, the first throttling valve connected with a rectifying tower, wherein the rectifying tower discharge feedstock through a condenser and a condensing separator, one liquid inlet, a discharge port of the condensing separator liquid outlet connected with rectifying tower and a condensing separator by cryogenic heat exchanger connected with expander, an expander in turn connected with condenser, heat exchanger, cooling heat exchanger and nitrogen pipe, the rectifying tower through the second throttle valve in turn a cryogenic heat exchanger, cooling heat exchanger and methane pipeline. The device a high efficiency methane, suitable implement.
NOVELTY - The utility model claims a new plant biomass thermal cracking gas filter device, wherein it comprises a upper end opening and lower end of tank body close, connected with a semi-spherical sealing flange on top of the tank body and a sealing cover, set with a present air inlet pipe is horizontal direction, the air inlet pipe and the axis of the tank body passing a centre of the tank body, fastening the two connected at present, a stainless steel filter screen in interval wall in the upper part of the air inlet pipe and the tank body, filling with filter material in between the two stainless steel filter screen, is set with a exhaust pipe at top part of the sealing cover, provided with a liquid pipe arrange at bottom of the tank body.
NOVELTY - The utility model claims a constant temperature domestic garbage fermentin device, comprising a fermentation chamber, a filter liquor pool, spiral, a detector, a heater, a controller and marsh gas pool, a fermentation cabin upper part set with a feeding port, the bottom in the fermentation chamber installed with a filter screen, a spiral discharging machine installation installed on a top plate of a fermentation chamber at upper part and a filter screen, a temperature detector, a heater mounted on a side wall of a fermentation chamber, a filtered liquid with a fine filter screen, a marsh gas pool via a percolate pipe connected at the lower part of a fermentation chamber, the upper part in said a percolate, the marsh gas pool top part set with marsh gas outlet. The constant temperature domestic garbage fermentin device can realize constant temperature control, can greatly increase efficiency of fermentation.
NOVELTY - Continuous feedstock transport device of biomass carbonizing furnace comprises a furnace body set with an inner cavity. The furnace body inner cavity is provided with a drying chamber, a carbonization chamber, a high temperature chamber and a cooling chamber from top to bottom. The adjacent chambers are respectively separated by a movable grate. The top of the drying chamber is connected with the top of the furnace body inlet. The top of the furnace body is provided with a feed hopper. A discharge opening of the feed hopper is connected with the top of the inlet of the furnace body.    USE - Used as continuous feedstock transport device of biomass carbonizing furnace.    ADVANTAGE - The device realizes continuous production and ensures uniform heating of furnace body.    DETAILED DESCRIPTION - Continuous feedstock transport device of biomass carbonizing furnace comprises a furnace body set with an inner cavity. The furnace body inner cavity is provided with a drying chamber, a carbonization chamber, a high temperature chamber and a cooling chamber from top to bottom. The adjacent chambers are respectively separated by a movable grate. The top of the drying chamber is connected with the top of the furnace body inlet. The top of the furnace body is provided with a feed hopper. A discharge opening of the feed hopper is connected with the top of the inlet of the furnace body. A feed control device is provided between discharge opening of the feed hopper and the top of the inlet of the furnace body. The feed control device prevents outward escape of gas from feed hopper inlet into the furnace body inner cavity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the continuous feedstock transport device of biomass carbonizing furnace.
NOVELTY - M30 methanol gasoline comprises 30 wt.% methanol, 10-30 wt.% waste oil, 20-30 wt.% gasoline, 10-20 wt.% dimethylbenzene, 2-5 wt.% 1,4-butanediol, 1-3 wt.% acetone, 1-4 wt.% dimethyl phosphate, 0.8-1.2 wt.% hexamethylene tetramine, 1-2 wt.% benzotriazole, and 0.00001-0.00023 wt.% 2,6-butylated hydroxytoluene.    USE - Used as M30 methanol gasoline.    ADVANTAGE - The methanol gasoline: has synergistic effect; utilizes waste oil and other raw materials for improving the quality; and has increased water resistance, prolonged shelf life and reduced storage difficulty.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the M30 methanol gasoline, comprising (i) mixing waste oil and xylene, at temperature of 50-80 degrees C environment, mixing and dispersing for 20-30 minutes, and then placing at constant temperature, (ii) mixing 1,4-butanediol, acetone, dimethyl phosphate, hexamethylene tetramine, benzotriazole and butylated hydroxytoluene, stirring under speed of 50-100 rotations/minute (rpm), dispersing for 20-30 minutes, then adding gasoline, adjusting the temperature at 30-40 degrees C, stirring under speed of 90-120 rpm for 10-20 minutes, placing in temperature of 5-10 degrees C environment, and allowing to stand at constant temperature, and (iii) adding the mixture obtained in the steps (i) and (ii) with methanol, adjusting the temperature to 40-60 degrees C, stirring under stirring speed of 130-150 rpm for 1-2 hours, subjecting to ultrasonic treatment for 5-10 hours, allowing to stand, and filtering to obtain M30 methanol gasoline.
NOVELTY - Proposed process consists in electric heating of catalytically active element (5) made of wire mesh or spiral of base metal to be heated at invariable resistance. Exhaust gases are purified with the help of carbon oxide methanation and nitrogen oxides reduction in reducing medium of neutralizer chamber (4). Exhaust gases are cooled after purification with the help of thermoelectric effects, for example, using the thermoelectrical refrigerator (9).    USE - Engines and pumps.    ADVANTAGE - Decreased of toxicity of ICE exhaust gases.2 cl, 6 dwg, 4 tbl
NOVELTY - A genetically modified yeast comprising plasmid expressing LGS1 gene or LGS1 homologous gene of glycoside hydrolases (GH)72 family, where the above-mentioned gene is transduced into the yeast by chromosomal integration, is new.    USE - The genetically modified yeast is useful for producing ethanol from glucose, xylose, mixture of saccharide of glucose and xylose, and saccharified liquid obtained from cellulose biomass (all claimed).    ADVANTAGE - The genetically modified yeast is acid tolerant, salt tolerant or halotolerant, and utilizes biomass resources.
NOVELTY - Reacting and/or removing non-carbohydrate compounds from biomass comprises (a) washing a second biomass with a first acid hydrolysate that is produced by acidic hydrolysis of a first biomass, thus producing acid hydrolysate washed second biomass; and (b) separating the acid hydrolysate washed second biomass from a portion of the first acid hydrolysate that was used for washing the second biomass.    USE - The method is used for reacting and/or removing non-carbohydrate compounds from biomass.    ADVANTAGE - More efficient and cost effective method for producing fermentable sugar molecules from cellulosic feedstock is provided. Biomass is prewashed with acid hydrolysate prior to pretreatment. In so doing, the amount of chemicals that are required to efficiently process biomass for downstream uses is greatly reduced.
NOVELTY - Marine anti-fouling composition, comprises: a base formulation; and at least one abatement agent comprising at least one nuisance marine biota irritating agent, biocide, enzymatic agent that dissolves marine arthropod cements, and/or anti-androgen agent that disrupts marine arthropod settlement cues.    USE - The marine anti-fouling composition is useful as anti-fouling marine paints and enamels. No biological data given.    ADVANTAGE - The marine anti-fouling composition utilizes environmentally-friendly nuisance biota irritating and non-toxic agents.
NOVELTY - This new utility model relates to one kind of biomass rapid pyrolysis steam is condensate fractionating device, includes fractional condensation tower and spherical, grading condensing tower comprises grading condensing tower shell and is set with condensing section in the condensing tower shell inner, grading in condensing tower shell body and condensing section equipped with spiral channel, the condensing segment divided, one grade condensing section, and lower part set with pyrogenation steam entrance, bottom set with one level liquid product outlet, second level condensing section, second grade condensing section comprises is set with an overflow pipe at the bottom, connected to periphery of secondary liquid product outlet, steam entrance and is set with the cap in steam entrance of pyrolysis, the third grade condensing section, the third grade condensing section comprises is set with an overflow pipe at the bottom, connected with the third level liquid product outlet to periphery is, steam entrance and the cap is set with pyrogenation steam entrance of wherein, after using said structure, directly obtaining liquid product and different remote boiling, condensing with full, not easy to block pipe, which avoids second time process, low investment equal.
NOVELTY - The utility model claims power line reconstruction for a methyl alcohol preparation system, comprising a purification section, methanol synthesis, methanol rectification working section, fuel gas pipe network, sulfur recovery, purification workshop fresh air pipeline and a methanol synthesis section a, fresh air control valve provided with a fresh air pipeline of the methanol synthesis section a rough methyl alcohol and methyl alcohol rectifying section connecting pipeline, methanol synthesis section a purge pipeline and fuel gas pipe network connected with the fuel gas pipe through a fuel gas pipeline and a section connected with sulfur. The utility model has the advantages as follows: a fresh air sending fuel gas pipeline root move to a boundary zone valve before, when a back cutting gas, a compound cutting, fresh air is still a sending fuel gas, thus, fuel gas pipe network user sulfur recovery section is a continuous operation, a sulfur can advance turn on 2 to 4 hours, reducing discharge of sulfur containing gas, a environment.
NOVELTY - The utility model is a new supply of a continuous biomass carbonizing device, comprising: automatic feeding device,, gas transporting pipe, a discharging sealing device, a carbonization furnace with open enter port located on top part of the carbonizing furnace, fuel gas outlet, the discharging port and top part of the carbonizing furnace, the biomass material by automatic feeding device, transporting to carbonizing.... open enter port for carbonizing reaction, carbonizing reaction product of gas input to gas transporting pipe and from a fuel gas outlet, the carbonizing product from the discharge port through a discharging sealing device output. The utility model is a model of a supply of continuous biomass carbonizing device, it can realize continuous opening feedstock, continuous carbonizing, a suitable for carbonizing the biomass material is of a shape and size.
NOVELTY - This new utility model claims of a kind of one unite water washing one baking pre-processing biomass microwave pyrolysis more and cogeneration device, comprising biomass water washing, baking-pyrolysis system and water washing liquid circulation system. Biomass raw material after first washing part removing alkali metal and impurities via water for pre drying, and baking later resolve pre-processing of large amount of hemicellulose component, and improving of biomass physical micro-structure, after pre-processing biomass microwave pyrolysis quality of product with increase, to obtain biomass semi coke heat value is high, ash fusion point height, bio-low water content, low acidity, chemistry component stable, synthesis gas heat value high, follow-up using large potential. This utility new type recovery of volatile and baking energy, prevention as drying heat source, at the same time, water washing liquid circulation system of heat recovery de-semi coke and sensible heat and after drying and smoke exhaust and moisture and latent heat, system can effect high, operation process without exhaust gas discharge, operating parameter are can according to the biomass raw material regulation, system operation safety height, low cost.
NOVELTY - This new utility model claims of one of biomass carbonized gasification device, comprising furnace body and is set with set with heat guide plate on the hearth upper part the furnace body middle part, the hearth and the furnace body middle; the furnace body one end equipped with feedstock device and gas leading-out device, the other end set with cooling chamber, in the reducing temperature room out transmission net belt and provided with heat exchanger, the temperature reducing room connected with spray chamber, inside the furnace body set with inner transmission belt, in the transmission screen belt and the transmission belt connected with outside, said inner transmission net belt and the outside transmission belt and transmission device are connected, one layer heat accumulator equipped with close loop intermediate formed in the internal furnace body in the transmission mesh belt, the heat storage body and the heat exchanger connected with, the furnace body of the hearth and are provided with temperature control device. This new utility model can realize continuous work, production efficiency high, and can realize full recovery of heat and to use.
NOVELTY - A. crushing drying auger feeding type biomass pressing forming machine, the front pedestal for drying crushing, a rear pedestal for biomass pressing block forming part, a drying part and a crushing biomass pressing forming part by a connecting mechanism, a drying crushing comprises: crushing machine and dryer, the dryer internal installed with spiral guide plate, a dryer under end is exit, said exit under memory provided with a slot, the biomass pressing forming part includes the electrical machine, the installation has a main shaft, mounted with a rotating disc on the main shaft, and a rotating disc installed with import feeder, installed with a hinge shaft in a spiral feeder, a feeder at the part provided with the transmission mechanism and phase matching of a hopper. Structure is simple, a suitable fast, at the same time a crushing drying material, forming effect is good, uniform size, of a material can effectively increase work efficiency, forming a bag and directly, without a large amount of manpower and material resources to equal;
NOVELTY - The device has circle module (5) whose discharge port is connected to feedstock port of ejector (2). Liquid recoverer (3) is connected to liquid recycling device. Refined desulfurization component (11) is connected to feedstock port. Weak adsorbate product discharging port is connected with combustion net (13). Refined desulfurization component and strong adsorption quality product discharging port are connected with feed gas pipeline (14). Steam device (6) supplies heat to liquid regeneration component (7) and refined desulfurization component.    USE - TSA circulation desulfurization device for refinery plant.    ADVANTAGE - The structure of the TSA circulation desulfurization device is simple. The desulfurization efficiency is effectively increased. Cost of operation is saved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the TSA circulation desulfurization device for refinery plant.    Ejector (2)    Liquid recoverer (3)    Circle module (5)    Steam device (6)    Liquid regeneration component (7)    Refined desulfurization component (11)    Combustion net (13)    Feed gas pipeline (14)
NOVELTY - An alkoxyamine compound comprising homoadamantane skeleton (I), is new.    USE - New alkoxyamine compound is used for catalyst for oxidizing alcohol (all claimed) to carbonyl compound used in pharmaceutical, agrochemical, cosmetics and organic material applications.    ADVANTAGE - The alkoxyamine compound provides alcohol oxidation catalyst with high catalytic activity, by environmentally-friendly process.    DETAILED DESCRIPTION - An alkoxyamine compound comprising homoadamantane skeleton of formula (I), is new.    R1,R2=H or optionally substituted alkyl.    INDEPENDENT CLAIMS are included for the following:    (1) alcohol oxidation catalyst, which consists of alkoxyamine compound or its derivative; and    (2) alcohol oxidation method, which involves oxidizing alcohol in presence of alcohol oxidation catalyst and co-oxidation catalyst.
NOVELTY - The mixer has a rotating shaft (3) that is provided on a left machine frame (1) and a right machine frame (2). The left machine frame is provided with a driving device (4). The right machine frame is provided with a rotating transmission device (5). The left end of the rotating shaft is connected to the driving device, and the right end is connected with the rotating transmission device through a connecting flange (6). The upper portion of the rotating shaft is provided with a mixing device (7), so that the included angle between the mixing device and rotating shaft is 25-35 degrees.    USE - Turnover hopper mixer used in pharmaceutical industry.    ADVANTAGE - The installation maintenance of the turnover hopper mixer is simplified. The operation of the device is stable. The noise in the mixer is reduced. The use of the hopper mixer is very suitable. The stable reliability of the device is improved. The pollution to the working environment is avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the turnover hopper mixer.    Left machine frame (1)    Right machine frame (2)    Rotating shaft (3)    Driving device (4)    Rotating transmission device (5)    Connecting flange (6)    Mixing device (7)
NOVELTY - Producing biogas involves pouring first stage fermentation material into first fermentation system. Second stage fermentation material is poured into second fermentation system. Biogas is produced in fermentation zone, which is formed between side walls of cylinder block and adjacent block. The biogas produced flows into first and second fermentation system from pipeline. Rise of biogas slurry liquid in the first fermentation system eventually flows into the second system. Accumulated biogas slurry liquid drained to inner tube from second fermentation system due to inflow pressure.    USE - Method for producing biogas (claimed).    DETAILED DESCRIPTION - Producing biogas involves pouring first stage fermentation material into first fermentation system. Second stage fermentation material is poured into second fermentation system. Biogas is produced in fermentation zone, which is formed between side walls of cylinder block and adjacent block. The biogas produced flows into first and second fermentation system from pipeline. Rise of biogas slurry liquid in the first fermentation system eventually flows into the second system. Accumulated biogas slurry liquid drained to inner tube from second fermentation system due to inflow pressure. The biogas produced in the first system flows to third and fourth fermentation system from the pipeline due to the inflow pressure. The biogas slurry liquid is stored in the second fermentation system, where the slurry reflux back to the second system due to water pressure. Process is repeated to generate biogas.
NOVELTY - The system has a second stage fermentation system (40) that comprises a second stage fermentation pipeline, second stage feedstock pipeline (42), and a second stage discharging pipeline (44). A first guide pipe (22) is arranged between a first-stage fermentation pipeline and second stage feedstock pipeline. A second guide pipe (24) is arranged between first stage fermentation pipeline and second stage discharging pipeline. A check valve is arranged between the second stage fermentation pipeline and first and second guide pipes.    USE - Multi-level turbulence effect linkage type biogas fermentation system.    ADVANTAGE - The biogas stirring is effectively promoted. The uniform distribution of strain is promoted. The fermentation efficiency is improved.    DETAILED DESCRIPTION - A first-stage fermentation system (10) comprises a first-stage fermentation pipeline, and a material inlet and outlet cylinder (12). The material inlet and outlet cylinder is separated into a first-stage feedstock pipeline and a first-stage discharging cylinder by clapboard. A cloth fungus fermentation device is provided with a drain pipe connected with a cloth bacteria pipeline.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the multi-level turbulence effect linkage type biogas fermentation system.    Fermentation system (10,40)    Material inlet and outlet cylinder (12)    Guide pipes (22,24)    Feedstock pipeline (42)    Discharging pipeline (44)
NOVELTY - The utility model claims a... biogas slurry anti-sediment sleeve AO degradation device, it from a pool (1), a level aerobic degradation pool (2) and multistage Anaerobic degradation. (3) make up of the device a multistage degradation area, a first aerobic.. Anaerobic fermentation after fermentation, aerobic fermentation at front end is set with with aeration device, the aeration device too. According to different design and installation site internal in aerobic ferment finish a suction, aeration device can use microorganism strain and full contact biogas fermentation, back end is set with the relux pump can make a microorganism strain relux circulation cultivation, can get in reducing quantity of microorganism strain, comprising a biogas liquid flow when a relux amount of a relux pump, flow into a part. Anaerobic degradation; Anaerobic. Internal add with upper, lower clapboard, and is alternately mounted up and down, a microorganism and biogas slurry full contact degradation, and a. Anaerobic degradation cylinder two end has dirt, convenient cleaning a degradation product of slag.
NOVELTY - This new utility model claims of cloth fungus device to promote uniform distribution of strain beyond efficient marsh gas generating system, wherein comprising, feedstock tube, discharging tube, U type fermentation pipe, U type pipe horizontal placing for fermentation, feedstock tube and discharging tube vertical U-type fermentation pipeline connected with two end side, U type pipe upper part set hydraulic pressure ferment, and feedstock pipe connecting seat for feedstock pipe drainage hole, and a discharge tube connected with position for discharging pipe drainage hole, a U type pipe and fermentation feedstock pipe connecting seat is set with one feedstock to tube plate, U type fermentation pipe and discharging pipe connected with seat position is set with one discharging tube plate, upper U type pipe is set with fermentation has set air pipe, in also connected with cloth water pressure device fungus, bacteria distributing device of drain pipe, a U type cloth tube fungus, fungus hole composed of cloth, from feedstock tube and discharge tube one end side connected with bacteria distributing device of drain pipe, arrange the other end side connected with fixed water pipe of each suitable for the U-type inner pipe cloth ferment fungus tube, U type cloth tube and shape of fungus ferment pipe and extending to ferment in pipeline. U-type pipe of Brucella with multi-set of vertical direction of the cloth fungus hole, using U-type channel type fermentation device and fermentation line longer, using control of water pressure difference and one-way valve, biogas slurry realize full flow in in system, and uniformly distributing the driving strain, effective prevent the crusting phenomenon, high yield, suitable for large scale production.
NOVELTY - This new utility model claims of promoting air circulation flow of liquid beyond efficient marsh gas generating device, wherein comprising, the feedstock tube, discharging tube, U type fermentation pipe, U type pipe horizontal placing for fermentation, feedstock tube and discharging tube vertical U-type fermentation pipeline connected with two end side, U type pipe upper part set hydraulic pressure ferment, and feedstock pipe connecting seat for feedstock pipe drainage hole, and a discharge tube connected with position for discharging pipe drainage hole, a U type pipe and fermentation feedstock pipe connecting seat is set with one feedstock to tube plate, U type fermentation pipe and discharging pipe connected with seat position is set with one material-blocking pipe board, upper U type pipe is set with fermentation has set air tube, discharge tube drainage hole site of feedstock of pipe drainage hole set with control water pressure in preparing biogas liquid one-way flow into feedstock tube and one-way valve, feedstock pipe drainage hole is lower than the seat, using U-type channel type fermentation device and fermentation line longer, using control of water pressure difference and one-way valve, biogas slurry realize full flow in in system, driving and uniform distribution of strain. Effective prevent the crusting phenomenon, height, suitable for large scale production.
NOVELTY - This new utility model claims of biogas one-way flow promoting uniform strain distribution of marsh gas ferment device, wherein comprising, the feedstock tube, discharging tube, U type fermentation pipe, U type pipe horizontal placing for fermentation, feedstock tube and discharging tube vertical U-type fermentation pipeline connected with two end side, U type pipe upper part set hydraulic pressure ferment, and feedstock pipe connecting seat for feedstock pipe drainage hole, and a discharge tube connected with position for discharging pipe drainage hole, a U type pipe and fermentation feedstock pipe connecting seat is set with one feedstock to tube plate, U type fermentation pipe and discharging pipe connected with seat position is set with one discharging tube plate, upper U type pipe is set with fermentation has set air pipe, in also connected with cloth water pressure device fungus, bacteria distributing device of drain pipe, a U type cloth tube fungus, fungus hole composed of cloth, from feedstock tube and discharge tube one end side connected with drain pipe of Brucella device, arrange the other end side connected with fixing water pipe for the pipe in the U type ferment fungus cloth tube, U type cloth tube and shape of fungus ferment pipeline for each and extending to ferment in pipeline. Upper one-way valve, a discharging pipe drainage hole in U-type pipe of Brucella with multi-set of vertical direction of the cloth fungus hole; feedstock pipe drainage hole set with control of water pressure in the biogas liquid one-way flow into feedstock pipe is set with control discharging pipe and liquid one-way flow into the one-way valve in water pressure, water pipe and arrange device of Brucella has control and is set with one-way in fermented biogas slurry pipe flow into the one-way valve in water pressure, the discharge pipe drainage hole at the lowest level is below the lowest point of water bacteria distributing device and the horizontal plane.
NOVELTY - This new utility model claims of water pressure double pipe channel type marsh gas generating device, comprising the feedstock tube, discharging tube, U type fermentation pipe, U type pipe horizontal placing for fermentation, feedstock tube and discharging tube vertical U-type fermentation pipeline connected with two end side, U type pipe upper part set hydraulic pressure ferment, and feedstock pipe connecting seat for feedstock pipe drainage hole, and a discharge tube connected with position for discharging pipe drainage hole, a U type pipe and fermentation feedstock pipe connecting seat is set with one feedstock to tube plate, U type fermentation pipe and discharging pipe connected with seat position is set with one material-blocking pipe board, upper U type pipe is set with fermentation has set air tube, a discharge tube drainage hole seat set with the one-way inner controlling fermentation biogas pipe flow into the one-way valve in water pressure, feedstock of drainage tube is set with hole with water pressure in control of biogas liquid one-way flow into feedstock tube and one-way valve, using U-type channel type fermentation device and fermentation line longer, using control of water pressure difference and one-way valve, biogas slurry realize full flow in in system, driving and uniform distribution of strain. Effective prevent the crusting phenomenon, height, suitable for large scale production.
NOVELTY - The utility model claims a high efficient marsh gas generating system of marsh gas pressure disturbance promoting several sections marsh liquid disorder flow, which is composed of a feedstock tube, a discharge pipe, a fermentation pipeline, the feedstock material and a detachable tube and U type pipe terminal a fermentation feedstock and a side wall and a side wall extended U-type discharge pipe in fermentation, of between a U-type fermentation pipe on top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, a U-shaped pipe is set with fermentation with gas-guide tube, the fermented line, liquid flow stirring notable effect, and promotes uniform strain distribution.
NOVELTY - The utility model claims a hydraulic turbulent stirring cloth fungus ultra-efficient methane generating system, comprising a feedstock tube, discharging tube, pipe ferment, the ferment pipe is straight pipe, fermentation pipe two end side top part equipped with open mouth and a detachably connected with a biogas liquid face with a feedstock tube and discharging tube, a feedstock side wall and a side wall extending to the discharge pipe in the fermentation, installed on fermentation pipeline between top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharge tube and drain in fermentation pipeline also is set with multi-number between the feedstock has a side wall and a side wall and between the discharging plate, a feedstock/discharging pipe side wall and adjacent blocking plate and forming a space of fermentation area or a space between adjacent blocking plate forming one of fermentation area, a top of a fermentation zone connected with gas-guide tube, the gas-guide pipe is set with a valve with a biogas circulation stirring a strong flow, a biogas liquid flow stirring to promote uniform distribution of strain. and it promots the fermentation raw material into a fermentation system, fermentation system and increase the gas production system.
NOVELTY - The utility model claims a straight hydraulic type super high efficient methane fermentation device, wherein it comprises a feedstock tube, a discharging tube, a pipe ferment, the ferment pipe is straight pipe, fermentation pipe two end side top part equipped with open mouth and a detachably connected with a biogas liquid face with a feedstock tube and discharging tube, a feedstock side wall and a side wall extending to the discharge pipe in the fermentation, installed on fermentation pipeline between top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharge tube and drain in fermentation pipeline also is set with multi-number between the feedstock has a side wall and a side wall and between the discharging plate, a feedstock/discharging pipe side wall and adjacent blocking plate and forming a space of fermentation area or a space between adjacent blocking plate forming one of fermentation area, a top of a fermentation zone is connected with gas-guide tube, the gas-guide pipe is set with a valve with a biogas circulation stirring a strong flow, a biogas liquid flow stirring to promote uniform distribution of strain, and it promots the fermentation raw material into a fermentation system, fermentation system and increase the gas production system.
NOVELTY - This utility model claims a high-efficient marsh gas generating system of Assembled gs shoe type biogas liquid disorder flow Brucella, comprising a feedstock tube, a discharge pipe and a fermentation pipeline, wherein the feedstock material and a detachable tube and a U type pipe. terminal a fermentation feedstock and a side wall and a side wall extended U-type discharge pipe in fermentation, of between a U-type fermentation pipe on top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, a U-shaped pipe is set with fermentation with gas-guide tube, a feedstock arrange water pipe set with a control water pressure in a biogas liquid one-way flow into feedstock tube and one-way valve, a discharging pipe of arrange. with a liquid discharging one-way flow into the one-way valve in water pressure, the fermented line a, liquid flow stirring notable effect, and promotes a uniform strain distribution.
NOVELTY - The utility model claims a Brucella methane fermentation system of hydraulic circulation flow area, wherein it comprises a feedstock tube, a discharging tube and a pipe ferment, wherein the ferment pipe is straight pipe, fermentation pipe two end side top part equipped with open mouth and a detachably connected with a biogas liquid face with a feedstock tube and discharging tube, a feedstock side wall and a side wall extending to the discharge pipe in the fermentation, installed on fermentation pipeline between top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharge tube and drain in fermentation pipeline also is set with multi-number between the feedstock has a side wall and a side wall and between the discharging plate, a feedstock/discharging pipe side wall and adjacent blocking plate and forming a space of fermentation area or a space between adjacent blocking plate forming one of fermentation area, a top of a fermentation zone is connected with gas-guide tube, the gas-guide pipe is set with a valve with a biogas circulation stirring a strong flow, a biogas liquid flow stirring to promote uniform distribution of strain. and it promots the fermentation raw material into a fermentation system, fermentation system and increase the gas production system.
NOVELTY - This new utility model claims of multiple mixed flow area of Brucella double cylinder type methane generating system, comprising the feedstock tube, discharging tube, pipe ferment, the ferment pipe is straight pipe, fermentation pipe two side top part equipped with open end and respectively can detachably connected with the following biogas liquid side with feedstock tube and discharging tube, feedstock pipe side wall and discharge tube side wall extending to ferment in the pipe, installed on fermentation pipeline between top, and feedstock pipe connected with level set between the feedstock tube drain pipe, water discharging pipe and connected with horizontal place of discharge pipe. in fermentation pipeline also set with multi-number between the feedstock tube side wall and discharge pipe side wall and between baffle, feedstock pipe feeding/discharging pipe side wall and the adjacent blocking plate and form one space of fermentation area or the space between the adjacent blocking plate forming one of fermentation area, respectively the top of ferment cell connected with each independent and gas-guide tube, the gas-guide tube is set with upper valve with the liquid circulation flow stirring performance strong. In using biogas liquid flow stirring promoting uniform distribution of strain, and promote the fermentation material into fermentation system, fermentation system and increase the gas production system.
NOVELTY - This new utility model claims of feedstock tube, discharging tube can disassemble type novel methane generating device, comprising the feedstock tube, discharging tube, pipe ferment, the ferment pipe is straight pipe, fermentation pipe two side top part equipped with open end and respectively can detachably connected with the following biogas liquid side with feedstock tube and discharging tube, feedstock pipe side wall and discharge tube side wall extending to ferment in the pipe, installed on fermentation pipeline between top, and feedstock pipe connected with level set between the feedstock tube drain pipe, water discharging pipe and connected with horizontal place of discharge pipe. in fermentation pipeline also set with multi-number between the feedstock tube side wall and discharge pipe side wall and between baffle, feedstock pipe feeding/discharging pipe side wall and the adjacent blocking plate and form one space of fermentation area or the space between the adjacent blocking plate forming one of fermentation area, respectively the top of ferment cell connected with each independent and gas-guide tube, the gas-guide tube is set with upper valve with a biogas circulation stirring performance strong flow, using biogas liquid flow stirring to promote uniform distribution of strain. and it promots the fermentation raw material into a fermentation system, fermentation system and increase the gas production system.
NOVELTY - This new utility model claims a methane fermentation system of one-way circulation flow promoting fermentation raw material flow, wherein a feedstock tube, discharging tube, pipe ferment, the ferment pipe is straight pipe, pipe respectively connected with fermentation feedstock tube and discharge tube with two end side, between installed on fermentation pipe top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, pipeline and fermentation feedstock a position... feedstock with a plate, fermented pipe and discharging pipe connecting seat to set with a discharging blocking plate, a fermentation pipeline also is set with multi-number between the feedstock has a blocking plate and a blocking plate and a discharging plate, the space between the adjacent blocking plate forming one of fermentation area, a top of a fermentation zone... connected with gas-guide tube, the gas-guide pipe is set with a valve with a biogas circulation stirring a strong flow, a biogas liquid flow stirring to promote uniform distribution of strain, and promote the fermentation raw material into a fermentation system, It increases the fermentation system and system.
NOVELTY - The utility model claims a high efficient biogas liquid turbulent flow type methane generating system, wherein a feedstock tube, discharging tube, pipe ferment, the ferment pipe is straight pipe, pipe respectively connected with fermentation feedstock tube and discharge tube with two end side, between installed on fermentation pipe top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, pipeline and fermentation feedstock a position... feedstock with a plate, fermented pipe and discharging pipe connecting seat to set with a discharging blocking plate, a fermentation pipeline also is set with multi-number between the feedstock has a blocking plate and a blocking plate and a discharging plate, the space between the adjacent blocking plate forming one of fermentation area, a top of a fermentation zone... connected with gas-guide tube, the gas-guide pipe is set with a valve with a biogas circulation stirring a strong flow, a biogas liquid flow stirring to promote uniform distribution of strain, and promote the fermentation raw material into a fermentation system, Increase the fermentation system and system.
NOVELTY - The utility model claims a new high efficient mixed flow stirring promoting beyond the methane generating bacteria distributing system, wherein a feedstock tube, discharging tube, pipe ferment, the ferment pipe is straight pipe, pipe respectively connected with fermentation feedstock tube and discharge tube with two end side, between installed on fermentation pipe top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, pipeline and fermentation feedstock a position... feedstock with a plate, fermented pipe and discharging pipe connecting seat to set with a discharging blocking plate, a fermentation pipeline also is set with multi-number between the feedstock has a blocking plate and a blocking plate and a discharging plate, the space between the adjacent blocking plate forming one of fermentation area, a top of a fermentation zone... connected with gas-guide tube, the gas-guide pipe is set with a valve with a biogas circulation stirring a strong flow, a biogas liquid flow stirring to promote uniform distribution of strain, and promote the fermentation raw material into a fermentation system, It increases the fermentation system and system.
NOVELTY - The utility model claims a new type pneumatic bend extrusion biogas liquid flow stirring is beyond efficient methane generating system, wherein comprising: a feedstock, a discharge pipe, a fermentation pipe, a fermentation level pipe set, a feedstock material and a vertical U-type fermentation pipeline connected with a terminal a, a fermentation pipe of a hydraulic part, a feedstock tube connecting seat for feedstock a drainage hole, a discharging pipe and a position for discharging a drainage hole, a pipeline and fermentation feedstock pipe connecting seat is set with a feedstock to a baffle, a fermentation pipe and discharging pipe connecting seat is set with a discharging pipe to plate, discharging tube between blocking board and a feedstock-blocking plate is set with at least a one with a plate, a disc feeding/discharging pipe and between adjacent blocking plate or between the adjacent blocking plate forming one of fermentation area, top part of each fermentation area is set with two independent with the gas collecting pipe, each fermentation area of top part and connecting with the independent gas collecting pipe, a gas collecting tube is set with with a valve, a U-shaped channel type fermentation device. Fermentation line a, a water pressure and a one-way valve and a, biogas slurry realize full flow within a system, and a uniform distribution of strain, a preventing crust, high yield, suitable for large scale production.
NOVELTY - The utility model claims a new type U several ferment cell methane generating system, wherein comprising: a feedstock, a discharge pipe, a fermentation pipe, a fermentation level pipe set, a feedstock material and a vertical U-type fermentation pipeline connected with a terminal a, a fermentation pipe of a hydraulic part, a feedstock tube connecting seat for feedstock a drainage hole, a discharging pipe and a position for discharging a drainage hole, a pipeline and fermentation feedstock pipe connecting seat is set with a feedstock to a baffle, a fermentation pipe and discharging pipe connecting seat is set with a discharging pipe to plate, discharging tube between blocking board and a feedstock-blocking plate is set with at least a one with a plate, a disc feeding/discharging pipe and between adjacent blocking plate or between the adjacent blocking plate forming one of fermentation area, top part of each fermentation area is set with two independent with the gas collecting pipe, each fermentation area of top part and connecting with the independent gas collecting pipe, a gas collecting tube is set with with a valve, a U-shaped channel type fermentation device and fermentation line...... a and a one-way valve. Biogas slurry realize full flow within a system, and a uniform distribution of strain, a preventing crust, high yield, suitable for large scale production.
NOVELTY - The apparatus has a rotary drum unit (500) having a first and a second rotary drum that is respectively connected to a second and a third sprocket, such that the driving force of a driving sprocket wheel is delivered in an oblique direction to an inner holding space (130) of a main portion (100). A rotary shaft is fastened to second and third sprockets of rotary drums. An end portion of tooth-shaped rotary blade is installed at an outer periphery of the rotary shaft. A partitioning plate is installed at outer periphery of the rotary shaft, for partitioning off the rotary blade.    USE - Combustible waste supplying apparatus.    ADVANTAGE - The combustible waste of fixed quantity in the molding machine is supplied stably and smoothly. The phenomenon of garbage containing waste plastic or vinyl during supply of combustible waste is minimized.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the combustible waste supplying apparatus.    Main portion (100)    Inner holding space of main portion (130)    Transfer conveyor (200)    Screw (400)    Rotary drum unit (500)
NOVELTY - The new type utility claims have one plant high-efficient boiling concentrated made paste machine, comprising mounting base, boiler body and boiler cover, boiler body comprises outside cylinder, inside cylinder, and at medium cavity, mounting base of inner tube outside wall and outside cylinder inner wall composed of the matched set with installation cavity and pot body, opening end edge of outside cylinder is lower than mounted in open mouth end edge, end edge opening of inner cylinder and mounted in opening end at least, the inner cylinder opening end edge distance outside cylinder opening end edge set with one section on the extending side wall exposed out of outside cylinder, extending side wall above the discharge hole is set with interval distribution, extending side wall and inner wall mounted in between and discharge hole connected with the discharging cavity, upper mounting base and provided with the exhaust in the exhaust joint connected. The utility model is new type comprises decocting effect is good, it is energy saving and environment-friendly.
NOVELTY - Synthesizing ambroxol hydrochloride comprises taking o-nitrobenzaldehyde as initial raw material, carrying out bromination to obtain 2-nitro-3,5-dibromobenzaldehyde, reacting 2-nitro-3,5-dibromobenzaldehyde and trans-4-aminocyclohexanol to obtain compound (E)-4-(3,5-dibromo-2-nitrobenzylideneamino)cyclohexanol, reducing (E)-4-(3,5-dibromo-2-nitrobenzylideneamino)cyclohexanol, forming hydrochloride salt to obtain ambroxol hydrochloride.    USE - The method is useful for synthesizing ambroxol hydrochloride (claimed).    ADVANTAGE - The method uses economical raw material, has simple operation, is safe and environmentally friendly, increases product yield and product purity, and is suitable for industrial production.
NOVELTY - The stirrer has a vent (120) for ejecting sludge from inlet port (110) of a main portion (100). A shaft (200) is turned upward about the surface and the bottom edge to rotate the main portion. A shaft (300) is horizontally set up about the bottom surface of main portion. The shaft (200) has an agitating blade (210) which is located beneath the main portion and rotated at the driving of the actuator (220) for stirring organic compound. The shaft (300) has an agitating blade (310) which is mounted to the bottom side of the main portion and rotated at the driving of the actuator (320).    USE - Stirrer for disintegration of organic material reaction such as livestock wastewater reaction, food waste reaction and sewage sludge reaction, used for producing biogas such as methane gas, liquefied natural gas and fuel.    ADVANTAGE - The shafts has agitating blades which are mounted to bottom side and beneath of main portion and rotated by actuator for stirring organic compound, so that stirring effect is raised and production efficiency of the biogas is increased. The mixing effect of the methanogenic bacteria and organic compound can be more enhanced. The structure is simple and maintenance and repair of stirrer are easy.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the stirrer.    Main portion (100)    Inlet port (110)    Vent (120)    Shafts (200,300)    Agitating blades (210,310)    Actuators (220,320)
NOVELTY - Producing particle type threonine product comprises (i) preparing threonine fermentation liquid, (ii) preparing powdered threonine, (iii) preparing threonine granules, (iv) obtaining bacterial protein, (v) preparing feed, and (vi) preparing organic fertilizer.    USE - The method is useful for producing particle type threonine product (claimed).    ADVANTAGE - The method avoids moisture absorption agglomeration, can realize process without waste production and environmental pollution.
NOVELTY - The new type utility claims have one plant kitchen garbage, livestock manure, crop straw, sewage, disease livestock and poultry dead equal waste harmless processing device, comprising outside double layer wall structure in the fermentation tank body, the top part of fermentation tank body provided with circulation fan, inner layer tank wall of fermentation tank body provided with concave, fan and circulation fan set on concave to the inner layer tank wall below the horizontal fan blade set with cloth wind plate, cloth wind plate at uniform set with cloth wind mouth, two end and the cloth wind plate and incline downward, in fermentation tank body set with stirring shaft, stirring shaft provided with stirring blade, stirring shaft and equipped with connection in fermentation tank in motor transmission, the inner tank wall and between outside layer tank wall also set with electromagnetic heating coil, magnetic site and stirring shaft of electromagnetic heating coil phase; the utility model is new type of advantage wherein the material for uniform heating, heat preservation effect is good, the heat diffusion uniformity, not produce local overheating phenomenon and temperature dead area, low energy consumption, high efficiency and heating material fermentation efficiency is high.
NOVELTY - The utility model is new type relates to one plant composite liquid fertilizer and production device, said production device comprises fermentation device, stirring dissolution device, a filter device, a filter liquor collecting mixer, mixing device, detection device and split charging and package device, on stirring dissolution device connected with the liquid adding device. The organic fertilizer of production equipment and the production processing process is smooth, simple and environment-friendly, the device through precise adding suspension agent can be equal, and feeding to design the composite layer is more reasonable and use life longer, and will not cause cross pollute equal, the device can effective increase work efficiency, shortens the working time, and production process of dust, clean, the human, poultry and environment safety, non-toxic, the equipment is simple, the design is reasonable and practical.
NOVELTY - The utility model is new type relates to one kind Vc effervescence granule and production device, said production device comprises a mixer, mixing device, granulating device covered and split charging device and package device, at the mixer connected with, upper machine connected with the first electronic steelyard; the upper mixing device connected with the disintegrating agent feeder, on the disintegrating agent feeder connected with the second electronic steelyard, the sieving device and covering the outer device and recovery smashing device connected with, the smashing device and recovery device connected with mixing. The organic fertilizer of production equipment and the production processing process is smooth, simple and environment-friendly, capable of precise adding each raw material and disintegrating agent equal; the device is increase have working efficiency, shortens the working time, reducing have have production cost, and production process for not qualified product recovery and processing, increase quality and in time, and no waste, with the important application value.
NOVELTY - The new type utility claims have one plant in cultivating pig dung dirt site field ecological circulation use system, comprising with solid-liquid separating machine, wherein the pig farm production and waste enter into collecting pool, and through the solid-liquid separating machine for processing pig excrement dry separation as organic fertilizer, then sewage enter into marsh gas pool, outlet of the marsh gas pool connected with straw matrix pool, straw matrix pool connected with the plant purification pool, the plant purification pool through pipeline connected with formed in situ pour pool in the field, at the pipe provided with the lifting tower and lifting pump. The utility model is new type reasonable structure, environmental protection and practical, make sewage waste as treasure, used for domestic production of, realize circulation of sewage ecological cultivating pig manure use site.
NOVELTY - The new type utility claims have can automatically stir and livestock manure pollution processing device, comprising inclined plate, the plate through the inclined lower end set with the joint fixedly stacked outside the edge of the manure pool, the excrement-storing pool set with fixing pedestal, the fixing pedestal is above the uniform distribution with stirring shaft, the upper stirring shaft provided with stirring blade, the excrement-storing pool set with fermentation pool, fermentation pool set with the biological fermentation auxiliary material. The utility model is new type structure is compact, can periodically stir, stirring efficiency is high, save manpower and material resources, can make livestock manure by composting process to be organic fertilizer, can package sold as caused by farmers have economic benefit;
NOVELTY - The utility model is new type relates to one kind solar energy kitchen garbage Anaerobic fermentation bucket, comprising outside bucket, inner bucket, solar energy solar panels cover, the outside bucket upper opening, the inner bucket is in the outside through internal, the solar energy to solar panels can be opened to and in the outside bucket upper part is opening, the outside inner bucket bottom is set with low voltage, constant-temperature controller and radiating fan, the solar energy solar panels to the low pressure electric power supply, the constant temperature controller through the low pressure heating and cooling fan regulate the inner bucket of outside temperature, the inner bucket to the upper opening, the inner bucket and upper part opening can be provided with sealing inner bucket and inner bucket cover internal cavity body, exhaust valve is set with internal gas discharging in the above bucket in the inner bucket cover. A solar energy plant kitchen garbage Anaerobic fermentation bucket the utility new type supply and, using suitable, operation is simple, can realize the kitchen waste into resource, which not only can obtain clean energy, but also reducing have discharge of pollutant.
NOVELTY - Preparing fertilizer involves mixing waste obtained from sugar production with ash and sugarcane pulp in ratio of 100: 15: 10. Bio-fermentation agents are added to obtained mixture to facilitate aerobic fermentation. Obtained brown or gray-brown product is subjected to composting and screening. Screened product is packed.    USE - Method for preparing fertilizer (claimed).
NOVELTY - Preparing organic fertilizer involves mixing crude fiber degrading bacteria and rice bran in a ratio of 1:20-1:25 to obtain a mixture, which is cultured for 5 days to obtain activated bacteria. Mushroom, peat, dry chicken manure, and water are mixed with activated bacteria ( 1kg/2.5-4.0tons) to obtain a mixture. Moisture of obtained mixture is controlled to 45-60%. Obtained material is kept in air in a form of heap (1.5 meter) to carry out fermentation. Fermentation material is mixed after 6-9 days, preferably 6 days in summer, and 9 days in winter.    USE - Method for preparing organic fertilizer (claimed) used for preventing disease caused by bacteria, insect, and nematodes.    DETAILED DESCRIPTION - Preparing organic fertilizer involves mixing crude fiber degrading bacteria and rice bran in a ratio of 1:20-1:25 to obtain a mixture, which is cultured for 5 days to obtain activated bacteria. Mushroom, peat, dry chicken manure, and water are mixed with activated bacteria ( 1kg/2.5-4.0tons) to obtain a mixture. Moisture of obtained mixture is controlled to 45-60%. Obtained material is kept in air in a form of heap (1.5 meter) to carry out fermentation. Fermentation material is mixed after 6-9 days, preferably 6 days in summer, and 9 days in winter. Bacteria (1kg/0.5-0.8 tons), and water is added to obtained product to obtain an another mixture. Obtained mixture is kept for 20-10 days at 35% for another fermentation. Fermented product is dried at relative humidity 18% to obtain final product.
NOVELTY - Preparing cultivation material involves crushing 52-58% sawdust, 16-22% corn, 16-18% bean cake, 4-5% mushroom, 3-4% lime and 1% gypsum into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) at low temperature for 18-24 hours, and then performed piling of product with height of 1.0-1.2m and width 2-3m to obtain ladder-shaped stack (300-500kg), and then carried out natural fermentation at 60 degrees C for 24 hours. Fermented product is wrapped in polyethylene cylindrical bag, and inoculated in dark cultivating bacterium room and cultured at 18-20 degrees C for 36-38 days.    USE - Method for preparing cultivation material used for white fungus (claimed).    ADVANTAGE - The method is eco-friendly and saves labor cost, and enables to prepare cultivation material that produce highly active metabolite product of white fungus, and ensures white fungus growth.
NOVELTY - Preparing cultivation material involves pulverizing cotton seed hull (58-62%), bagasse (18-20%), soybean (12-14%), mushroom (3-4%), lime (3-4%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then cotton seed hull, bagasse, soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours.    USE - Method for preparing cultivation material used for needle mushroom (claimed).    ADVANTAGE - The method is eco-friendly, saves labor, and ensures increased catalytic decomposition and growth of tea tree mushroom.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing cotton seed hull (58-62%), bagasse (18-20%), soybean (12-14%), mushroom (3-4%), lime (3-4%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then cotton seed hull, bagasse, soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Gypsum and lime are added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 20-22 days to obtain the final product.
NOVELTY - Preparing cultivation material involves pulverizing cotton seed hull (52-56%), wood powder (26-30%), soybean (10-12%), mushroom (3-4%), lime (2-3%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then cotton seed hull, wood powder and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and fermented.    USE - Method for preparing cultivation material used for Pleurotus (claimed).    ADVANTAGE - The method is eco-friendly, saves labor, and ensures increased catalytic decomposition and growth of Pleurotus.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing cotton seed hull (52-56%), wood powder (26-30%), soybean (10-12%), mushroom (3-4%), lime (2-3%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then cotton seed hull, wood powder and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Lime and gypsum are added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 23-25 days to obtain the final product.
NOVELTY - Preparing cultivation material involves taking sawdust (52-58%), corn cob (20-24%), tea residue (14-16%), mushroom (3-4%), lime (3-4%), and calcium carbonate (1%), where particle size of sawdust is 3-5mm, and mushroom is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then sawdust, corn cob, tea residue, mushroom, and lime are added to soaked product. Obtained mixture (300-500kg) is piled in heap having diameter 10-15cm. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with calcium carbonate, and obtained mixture is fermented.    USE - Method for preparing cultivation material used for cultivating Agrocybe cylindracea (claimed).    ADVANTAGE - The method is eco-friendly, and enables to prepare cultivation material, which ensures improved Agrocybe cylindracea growth.    DETAILED DESCRIPTION - Preparing cultivation material involves taking sawdust (52-58%), corn cob (20-24%), tea residue (14-16%), mushroom (3-4%), lime (3-4%), and calcium carbonate (1%), where particle size of sawdust is 3-5mm, and mushroom is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then sawdust, corn cob, tea residue, mushroom, and lime are added to soaked product. Obtained mixture (300-500kg) is piled in heap having diameter 10-15cm. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with calcium carbonate, and obtained mixture is fermented for 5-6 days. Moisture content of fermented material is 63-65%. Fermented material is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 24-26 days to obtain the final product.
NOVELTY - Preparing cultivation material involves pulverizing wood powder (58-62%), bagasse (14-18%), tea seed powder (16-18%), mushroom (3-4%), lime (2-3%) and light calcium carbonate (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, bagasse and tea seed powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours.    USE - Method for preparing cultivation material used for tea tree mushroom (claimed).    ADVANTAGE - The method is eco-friendly, saves labor, and ensures increased catalytic decomposition and growth of tea tree mushroom.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing wood powder (58-62%), bagasse (14-18%), tea seed powder (16-18%), mushroom (3-4%), lime (2-3%) and light calcium carbonate (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, bagasse and tea seed powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Lime and light calcium carbonate are added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 22-24 days to obtain the final product.
NOVELTY - Preparing cultivation material involves pulverizing cotton seed hull (38-42%), bagasse (34-36%), soybean (16-18%), mushroom (3-4%), lime (3-4%) and light calcium carbonate (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then cotton seed hull, bagasse and soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours.    USE - Method for preparing cultivation material used for needle mushroom (claimed).    ADVANTAGE - The method is eco-friendly, saves labor, and ensures increased catalytic decomposition and growth of tea tree mushroom.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing cotton seed hull (38-42%), bagasse (34-36%), soybean (16-18%), mushroom (3-4%), lime (3-4%) and light calcium carbonate (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then cotton seed hull, bagasse and soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Lime and light calcium carbonate are added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 21-23 days to obtain the final product.
NOVELTY - Biological fertilizer comprises mushroom residue (80-90 pts. wt.), and inorganic fertilizer (10-20 pts. wt.). Mushroom residue is obtained by fermentation in presence of bacteria (108 spores/g). Inorganic fertilizer comprises nitrogen, phosphorus and potassium (90wt.%).    USE - Biological fertilizer used for controlling infection caused by Sclerotinia sclerotiorum (claimed).
NOVELTY - Compound fertilizer comprises 40-50 pts. wt. ammonium nitrate, 26-28 pts. wt. diammonium phosphate, 22-24 pts. wt. potassium sulfate, 15-18 pts. wt. enzyme residue, 5-7 pts. wt. synergistic amino acid, 32-35 pts. wt. sulfuric acid, 16-18 pts. wt. liquid ammonia, 3-5 pts. wt. humic acid, 6-8 pts. wt. liquid seaweed, 2-4 pts. wt. synergistic concentrated seaweed and 2-4 pts. wt. coating additive.    USE - Compound fertilizer.    ADVANTAGE - The compound fertilizer is eco-friendly, inhibits urease, prevents soil-borne disease, and promotes yield of plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing compound fertilizer, which involves:    (A) mixing water and glutamic acid in ratio of 10:(5-6), and adding 2-3% of biological protease and chelated trace element at 68-78 degrees C for 10-12 hours to obtain synergistic amino acid;    (B) 2-4% mixing polymerization solution in the synergistic amino acid and putting in a concentrating tank at 65-70 degrees C;    (C) drying seaweed and pulverizing through 60-80 meshes, and adding 0.5-0.7% fungus in ratio of 2:1;    (D) stirring the mixture uniformly and fermenting at 68-72 degrees C for 5-7 days to obtain synergistic seaweed;    (E) extracting seaweed with water at 55-62 degrees C for 9-11 hours, and filtering to obtain seaweed extract;    (F) mixing all products and coating the coating additive through nozzle and fluidization bed process; and    (G) heating the coated product at 180-200 degrees C and granulating to obtain fertilizer with particle diameter of 2.5-4.75mm.
NOVELTY - Biological organic fertilizer comprises livestock manure (51-60 wt.%), wine lees powder (15-20wt.%), fermented fungus powder (0.3-0.5 wt.%), calcium-magnesium phosphate fertilizer (8-10 wt.%), oil cake (6-10 wt.%), urea (0.3-0.7 wt.%), and chitosan (5-8 wt.%).    USE - Biological organic fertilizer used for tea plants (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biological organic fertilizer, which involves:    (A) mixing livestock manure and wine lees powder to obtain mixed material;    (B) fermenting obtained mixture with mixing and adding fermented to obtain fermented product having 50-80% water;    (C) adding oil cake to obtained fermented product after 10-20 days;    (D) adding calcium-magnesium phosphate fertilizer, urea and chitosan;    (E) fermenting obtained mixture for 3-5 days; and    (F) pulverizing obtained product.
NOVELTY - Bio-organic fertilizer comprises water ( less than or equal to 30%), organic matter content ( less than or equal to 45%), gamma-polyglutamate ( less than or equal to 21g-1kg) and Bacillus amyloliquefaciens (0.5x 108 colony forming units/) performing starch metabolism, which are prepared after fermentation.    USE - Bio-organic fertilizer used for tobacco (claimed).    ADVANTAGE - The bio-organic fertilizer increases soil moisture and seedling biomass of tobacco plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-organic fertilizer which involves:    (A) inoculating Bacillus amyloliquefaciens in liquid seed culture medium and culturing with rotating speed of 130-160 revolutions per minute at 37 degrees C for 24 hours to obtain fermentation product;    (B) dissolving oxygen and performing fermentation with rotating speed of 120-160 revolutions per minute at 28-35 degrees C for 24 hours to obtain other fermentation product;    (C) mixing both fermentation products, and adding monosodium glutamate residue, bean pulp powder, molasses, magnesium sulfate, humic acid and vinegar residue, and then sterilizing for 30 minutes; and    (D) fermenting the mixture at 55-60 degrees C for 15-20 days, and then packaging.
NOVELTY - p-Hydroxybenzoic acid, ethanol, chitosan sulfate as solid acid catalyst and cyclohexane are added to three-necked flask, heated, refluxed, esterified, filtered and catalyst is recovered. Ethanol and cyclohexane are distilled from the resulting mixture, residue is poured into cold water, precipitated, dried, and recrystallized using ethanol to obtain ethylparaben.    USE - Synthesis of ethylparaben (claimed).    ADVANTAGE - The method provides ethylparaben having high selectivity, and stable catalytic property with high yield, by simple, economical and environmentally-friendly process.
NOVELTY - Preparing torasemide derivative (I) involves reacting toluene derivative (II) with imidazole derivative (III) to obtain the torasemide derivative (I).    USE - Method for preparing torasemide derivative (claimed).    ADVANTAGE - The method enables to prepare torasemide derivative in simple and environment-friendly manner, and with low toxicity and high safety.    DETAILED DESCRIPTION - Preparing torasemide derivative of formula (I) involves reacting toluene derivative of formula (II) with imidazole derivative of formula (III) to obtain the torasemide derivative of formula (I).    R1,R2=H, 1-10C saturated or unsaturated straight chain or branched alkyl group or 3-6C cycloalkyl group; and    NR1R2=five to seven membered heterocyclic unit.
NOVELTY - Synthesizing ethyl-3-(2-(((4-cyanophenyl)amino)methyl)-1-methyl-N-(pyridin-2-yl)-1H-benzo(d)imidazole-5-carboxamido)propanoate involves subjecting 3-(3-(2-(4-cyano-anilinyl) acetylamino)-4-(methylamino)-N-(pyridin-2-yl) benzamido)-propanoate to perform catalyzed condensation with specific chemistry reagent under acid catalytic condensation and then purifying the condensed material to obtain the desired product.    USE - Method for synthesizing ethyl-3-(2-(((4-cyanophenyl)amino)methyl)-1-methyl-N-(pyridin-2-yl)-1H-benzo(d)imidazole-5-carboxamido)propanoate (claimed).    ADVANTAGE - The method enables to synthesize ethyl-3-(2-(((4-cyanophenyl)amino)methyl)-1-methyl-N-(pyridin-2-yl)-1H-benzo(d)imidazole-5-carboxamido)propanoate in cost-effective and energy-saving manner, and with high purity.
NOVELTY - Use of salicylic acid and salicylic acid analogues in improving quality of microalgae biodiesel, is claimed.    USE - The salicylic acid and salicylic acid analogues are useful in improving quality of microalgae biodiesel, and promoting saturated fatty acid, namely myristic acid (C14:0), palmitic acid (C16:0) (preferred) and stearic acid (C18:0) content in microalgae oil, and production of biodiesel with increased cetane number (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use method of salicylic acid and salicylic acid analogues in improving quality of microalgae biodiesel, comprising culturing microalgae by adding salicylic acid analogues includes 5-20 mg/l salicylic acid, 10-20 mg/l sodium salicylate, 5-20 mg/l 2-benzoylbenzoic acid, 5-20 mg/l glycol salicylate and 5-20 mg/l acetylsalicylic acid.
NOVELTY - Wettable powder comprises 15-25 pts. wt. cocklebur extract, 10-30 pts. wt. oligogalacturonic acid, 5-26 pts. wt. wetting agent, 20-30 pts. wt. dispersing agent, 20-35 pts. wt. diatomite and 18-35 pts. wt. water.    USE - The wettable powder is useful for preventing black rot disease of cabbage (claimed).    ADVANTAGE - The wettable powder utilizes cocklebur fruit extract and oligogalacturonic acid by replacing chemical substances, so as to prevent toxic- and side- effects, and production of pesticide residual, and thus it is environmental friendly; and has good microbial controlling effect.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing wettable powder, comprising mixing all the above mentioned raw materials, pulverizing, and filtering through 30-80 mu m mesh, to obtain the final product;    (2) use of wettable powder for preventing black rot disease of cabbage; and    (3) use method of wettable powder, comprising diluting wettable powder by adding water in an amount of 800-1500 times, and then spraying.
NOVELTY - Method for preprocessing lignocellulosic biomass involves injecting exhaust gas of carbon dioxide into ammonium aqueous solution to form ammonium carbonate solution, preprocessing lignocellulosic biomass using the ammonium carbonate solution, and recycling the ammonium aqueous solution and carbon dioxide.    USE - Method for preprocessing lignocellulosic biomass of straw, barley straw, cornstalk, Pinus rigida, Eucalyptus and Eulalia (all claimed).    ADVANTAGE - The method enables efficient and economical preprocessing of lignocellulosic biomass with reduced energy consumption.
NOVELTY - Preparing organic-inorganic fertilizer involves utilizing 4 pts. wt. diatomite, 3 pts. wt. chitosan, 2 pts. wt. potassium humate, 1 pts. wt. active coal, 1 pts. wt. grass and 10 pts. wt. ammonia water. Raw materials are ground (except ammonia water) through 100-200 meshes into powder, and then ammonia water is added and centrifuged at speed of 100-200 revolutions per minute for 20 minutes. 30% Nitrification bacteria, 30% Paracoccus denitrificans, 20% Alcaligenes fecalis and 20% Bacillus cereus are mixed to prepare microbial agent.    USE - Method for preparing organic-inorganic fertilizer (claimed).    ADVANTAGE - The method enables to prepare eco-friendly organic-inorganic fertilizer in a simple manner.    DETAILED DESCRIPTION - Preparing organic-inorganic fertilizer involves utilizing 4 pts. wt. diatomite, 3 pts. wt. chitosan, 2 pts. wt. potassium humate, 1 pts. wt. active coal, 1 pts. wt. grass and 10 pts. wt. ammonia water. Raw materials are ground (except ammonia water) through 100-200 meshes into powder, and then ammonia water is added and centrifuged at speed of 100-200 revolutions per minute for 20 minutes. 30% Nitrification bacteria, 30% Paracoccus denitrificans, 20% Alcaligenes fecalis and 20% Bacillus cereus are mixed to prepare microbial agent. Microbial agent (100-200ml/NM3) is sprayed on centrifuged product to perform desulfurization and denitration at 30 degrees C for 24-36 hours, and then remove flue gas. Monoammonium phosphate, urea, potassium chloride and water are mixed in the obtained product and granulated through twin-screw extruder granulator to obtain granules. Granules are cooled to room temperature, and then sprayed Azotobacter chroococcum, and then dried to obtain organic-inorganic fertilizer.
NOVELTY - Preparing biofertilizer involves utilizing 4 pts. wt. diatomite, 3 pts. wt. chitosan, 2 pts. wt. potassium humate, 1 pts. wt. active coal, 1 pts. wt. grass and 10 pts. wt. ammonia water. Raw materials are ground (except ammonia water) through 100-200 meshes into powder, and then ammonia water is added and centrifuged at speed of 100-200 revolutions per minute for 20 minutes. Nitrification bacteria, Paracoccus denitrificans and Bacillus cereus are mixed in ratio of 1:1:1 to prepare microbial agent.    USE - Method for preparing biofertilizer (claimed).    ADVANTAGE - The method enables to prepare eco-friendly biofertilizer in a simple manner.    DETAILED DESCRIPTION - Preparing biofertilizer involves utilizing 4 pts. wt. diatomite, 3 pts. wt. chitosan, 2 pts. wt. potassium humate, 1 pts. wt. active coal, 1 pts. wt. grass and 10 pts. wt. ammonia water. Raw materials are ground (except ammonia water) through 100-200 meshes into powder, and then ammonia water is added and centrifuged at speed of 100-200 revolutions per minute for 20 minutes. Nitrification bacteria, Paracoccus denitrificans and Bacillus cereus are mixed in ratio of 1:1:1 to prepare microbial agent. Microbial agent (100-200ml/NM3) is sprayed on centrifuged product to perform desulfurization and denitration at 35 degrees C for 24-48 hours, and then remove flue gas. Peanut shell powder, monoammonium phosphate, urea, potassium chloride and water are mixed in the obtained product and granulated through double-screw extruder granulator to obtain granules. Granules are cooled to room temperature, and then sprayed Azotobacter chroococcum, and then dried to obtain organic-inorganic fertilizer. Microbial product, peanut shell powder, monoammonium phosphate, urea, potassium chloride, water and Azotobacter chroococcum are present in ratio of 20:10:10:8:5:20:1.
NOVELTY - Preparing medicinal fertilizer granules involves sieving fosthiazate to obtain particles of 200-300 mesh. Fertilizer granules and fusion agent are dissolved in solvent to obtain obtained a solution. Obtained products are mixed with to with stirring to obtain final product.    USE - Method for preparing medicinal fertilizer used for preventing and treating Meloidogyne disease (all claimed).    ADVANTAGE - The method is simple, and suitable to modern technology.
NOVELTY - Preparation of tilmicosin phosphate comprises taking tylosin, formic acid, 3,5-dimethyl-piperidine and chloroform, reflux heating, ammoniating, hydrolysis acidifying with water and strong acid, separating and cooling chloroform phase, water extracting, dropping liquid caustic soda to combined aqueous phase, centrifuging, washing, dissolving in water and phosphoric acid and spray-drying.    USE - Method for preparing tilmicosin phosphate.    ADVANTAGE - The method is environment-friendly, has high safety and low production cost, and is suitable for industrial production.
NOVELTY - Synthesis of androst-4-ene-6 beta ,19-epoxy-3,17-dione (I) comprises taking androst-5-ene-3 alpha -hydroxy-17-one (II) as raw material, carrying out 3-position protection to obtain androst-5-ene-3 alpha -hydroxy-17-one derivative (III), epoxidizing to get androst-5-ene-3 alpha -hydroxy-17-one derivative (IV), carrying out epoxy ring opening reaction to get androst-5-ene-3 alpha -hydroxy-17-one derivative (V), carrying out 6,19-position cyclization or 3-position hydrolysis to get androst-5-ene-3 alpha -hydroxy-17-one derivative (VI), and carrying out oxidation-dehydration.    USE - Method for synthesizing androst-4-ene-6 beta ,19-epoxy-3,17-dione used for preparing medicine (claimed).    ADVANTAGE - The method has reduced environmental pollution, high yield, and low cost.    DETAILED DESCRIPTION - Synthesis of androst-4-ene-6 beta ,19-epoxy-3,17-dione (I) comprises taking androst-5-ene-3 alpha -hydroxy-17-one (II) as raw material, carrying out 3-position protection to obtain androst-5-ene-3 alpha -hydroxy-17-one derivative of formula (III), epoxidizing to get androst-5-ene-3 alpha -hydroxy-17-one derivative of formula (IV), carrying out epoxy ring opening reaction to get androst-5-ene-3 alpha -hydroxy-17-one derivative of formula (V), carrying out 6,19-position cyclization or 3-position hydrolysis to get androst-5-ene-3 alpha -hydroxy-17-one derivative of formula (VI), and carrying out oxidation-dehydration.
NOVELTY - Biodiesel oil additive comprises 60-70 pts. wt. 9-18C alkane, 8-12 pts. wt. enzyme, 6-7 pts. wt. stabilizer, 2-5 pts. wt. dispersant, 0.1-0.3 pt. wt. N,N-disalicylidene propanediamine and 14-22 pts. wt. solvent.    USE - Biodiesel oil additive used for improving combustion performance and economic performance of diesel engine.    ADVANTAGE - The product is environment-friendly; has energy-saving effect; and reduces diesel emissions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biodiesel oil additive comprising placing raw materials into the reaction kettle, heating at 30-40 degrees and stirring for 20 minutes.
NOVELTY - The device comprises a current collector, a double polar plate, and a membrane electrode component, where the current collector has a porous structure having inner hole for loading catalyst. The double polar plate surface is also loaded with the catalyst. The catalyst comprises catalytic hydrogen or noble metal catalyst for generating water.    USE - Device for manufacturing proton exchange membrane.    ADVANTAGE - The device manufactures the product with high purity and increased safety in a simple and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing proton exchange membrane, which involves:    (A) washing current collector and bipolar plate to remove surface oxides;    (B) preparing catalyst precursor solution;    (C) spraying the prepared catalyst precursor solution on the collector and the bipolar plate surface;    (D) drying the sprayed precursor solution at 200-350 degrees C;    (E) cooling the dried surface to obtain the finished surface; and    (F) loading the prepared surface with a catalyst and membrane electrode assembly to give the proton exchange membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic chromatographic data of the water electrolyzer and the anode product.
NOVELTY - Preparing polysaccharide and/or tobacco balsam by using waste tobacco leaves of flue-cured tobacco, comprises crushing flue-cured tobacco leaves into 40-60 meshes sieve, mixing with water, ultrasonic extracting, centrifuging, taking supernatant, vacuum evaporating and concentrating, taking the concentrate, adding 3-5 times the volume of the concentrated solution of anhydrous ethanol, alcohol precipitating, centrifuging, taking supernatant for making balsam and lower precipitate as refined polysaccharide.    USE - The method is useful for preparing polysaccharide and/or tobacco balsam by using waste tobacco leaves of flue-cured tobacco. The low flue-cured tobacco leaves raffinate is useful for preparing organic fertilizer or tobacco sheet (all claimed).    ADVANTAGE - The method is environmentally friendly and economical.    DETAILED DESCRIPTION - Preparing polysaccharide and/or tobacco balsam by using waste tobacco leaves of flue-cured tobacco, comprises (i) crushing flue-cured tobacco leaves into 40-60 meshes sieve; (ii) mixing sample with water, where the sample to water weight ratio is 1:20-1:30, and ultrasonic extracting with power of 400-600w for 7-10 minutes; (iii) centrifuging at speed of 9000-11000 revolutions/minute for 13-17 minutes at 3-5 degrees C, taking supernatant, vacuum evaporating at 65-75 degrees C and concentrating to a volume of 1/6-1/4; (iv) taking the concentrate, adding 3-5 times the volume of the concentrated solution of anhydrous ethanol, alcohol precipitating at 3-5 degrees C for 43-53 hours, centrifuging under speed of 9000-11000 revolutions/minute, taking supernatant for making balsam and lower precipitate as refined polysaccharide; and (v) adjusting pH of the supernatant to 2.5-3.5 with dilute sulfuric acid, allowing to stand for 3.5-4.5 hours, centrifuging under 9000-11000 revolutions/minute, concentrating and vacuum evaporating the supernatant at 65-75 degrees C to obtain paste as tobacco balsam.
NOVELTY - The new type utility claims have one kind organic fertilizer fermentation turning drying machine, comprising machine frame, drying, the first electric engine, a heater, controller, the second electric engine, shaft and walking wheel, the top machine frame mounted with the first electric machine and the second electric machine and controller, controller and the first electric machine, the second electrical machine connected with, the first electric machine and the first belt wheel connected with, the first belt wheel and the second belt wheel transmission belt, the second belt wheel through transmission device and turning shaft each connected; the machine frame bottom mounted with turn material on shaft, turning shaft provided with several turn material piece, in the machine frame mounted with drying, drying in interlayer mounted with stirring shaft, stirring shaft and transmission device connected with each, on stirring shaft provided with several blades. The utility model is new type can realize fermentation turning machine of organic fertilizer drying material, stirring completely, drying uniformity, the traditional can type fermentation compost process of fermentation, fermentation time is longer, production efficiency high, which saves using space.
NOVELTY - Microalgae culture apparatus comprises anaerobic digestion unit for livestock waste, membrane bioreactor (MBR) tank for separating sludge and effluent treatment by anaerobic digestive juices of anaerobic digester, MBR tank effluent and ozone or organic matter contained in effluent, microalgae culture tank for culturing microalgae with nitrogen and phosphorus, and membrane for separating microalgae cultivation.    USE - Microalgae culture apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for culturing microalgae applied ozone oxidation.
NOVELTY - The bandage comprises a release paper motherboard (1), a disinfection gauze (2), an oval tape (3). The oval tape is provided with sterilized gauze at the center of tape and is made of rubberized fabric.    USE - Bandage for stopping bleeding after blood test or injection.    ADVANTAGE - The bandage comprises a release paper motherboard, a disinfection gauze, an oval tape that is provided with sterilized gauze at the center of tape, and thus enables to provide simple minimally invasive paste structure, compact, efficient, environmentally friendly and replaces cotton swabs to stop bleeding.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of bandage.    Release paper motherboard (1)    Disinfection gauze (2)    Oval tape (3)
NOVELTY - Producing methane by multi-stage biogas fermentation system involves pouring fermentation material into a barrel shaped feed tube of secondary fermentation system (40). The primary fermentation system (10) generates and accumulate biogas in the space between the side wall of the inlet and outlet material cylinder and the adjacent plate or between the adjacent blocking plates. The slurry is extruded in primary fermentation pipeline for flowing to first guide pipe, second guide pipe and then to secondary fermentation pipe to generate and accumulate biogas in secondary fermentation pipe.    USE - Method for producing methane by multistage biogas fermentation system (claimed).    DETAILED DESCRIPTION - Producing methane by multi-stage biogas fermentation system involves pouring fermentation material into a barrel shaped feed tube of secondary fermentation system. The primary fermentation system generates and accumulate biogas in the space between the side wall of the inlet and outlet material cylinder and the adjacent plate or between the adjacent blocking plates. The slurry is extruded in primary fermentation pipeline for flowing to first guide pipe, second guide pipe and then to secondary fermentation pipe to generate and accumulate biogas in secondary fermentation pipe. The secondary fermentation system generates and accumulate biogas between the sidewall of the feedstock pipe (42) and the side wall of the discharging pipe (44). The slurry is stored through third conduit and fourth conduit (34) which flows in primary fermentation pipe. The slurry is stored in feedstock pipe which flows in secondary fermentation pipeline.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fermentation system.    Primary fermentation system (10)    Fourth conduit (34)    Secondary fermentation system (40)    Feedstock pipe (42)    Discharging pipe (44)
NOVELTY - Production of methane involves fermenting raw material in primary fermentation system to produce biogas and collecting biogas in side walls of charging/discharging barrel and adjacent gas baffles or in fermentation area formed between adjacent gas baffles, extruding biogas slurry in primary fermentation pipeline to flow to water guide pipe (a) and water guide pipe (b), and allowing biogas slurry to flow into secondary fermentation pipeline, fermenting to produce biogas in secondary fermentation system and collecting biogas between side walls of secondary feeding/discharging pipe.    USE - Production of methane by using secondary synchronous methane fermentation system (claimed).    DETAILED DESCRIPTION - Production of methane involves fermenting raw material in a primary fermentation system to produce biogas and collecting the biogas in the side walls of a charging/discharging barrel and adjacent gas baffles or in a fermentation area formed between adjacent gas baffles, extruding the biogas slurry in a primary fermentation pipeline to flow to a water guide pipe (a) and a water guide pipe (b), and allowing the biogas slurry to flow into a secondary fermentation pipeline, fermenting to produce biogas in a secondary fermentation system and collecting the biogas between the side walls of a secondary feeding/discharging pipe and adjacent gas baffles or in a fermentation area formed between the adjacent gas baffles, allowing the biogas slurry to flow into a water pressure room in a one-way mode by virtue of a secondary discharging pipe, and allowing the biogas slurry in the secondary fermentation pipeline to flow into the water pressure room by virtue of a drainage pipe of a bacteria distribution device when the liquid level of the biogas slurry in the water pressure room reaches the lowest position of the upper portion of the drainage pipe of the bacteria distribution device.
NOVELTY - Processing of sewage involves adding sewage to fluidized bed reactor, controlling the concentration of dissolved oxygen in the reactor, and adhering anaerobic microorganism and/or microbes to inner surface of filler to form biofilm (a), increasing concentration of dissolved oxygen in reactor, and adhering aerobic microorganisms to the surface of filler to form biofilm (b). The filler is polyurethane foam.    USE - Processing of sewage using biological fluidized bed (claimed).    ADVANTAGE - The method enables efficient processing of sewage by decomposing organic materials.
NOVELTY - Biogas fermentation system includes fermentation region (301) containing raw material is formed between feed tube i.e. inlet tube (10) and outlet tube (20). Air resistance plate (34) is formed adjacent to fermentation zone or fermentation pipeline (30). Methane gas is produced by pushing biogas fermented liquid to flow in the adjacent areas. The fermentation zone is filled with methane. The biogas fermented liquid is continued to flow in adjacent fermentation area. The biogas fermentation annular pipe, where the level reaches to inlet tube and outlet tube sidewalls lowest position.    USE - Biogas fermentation system.    DETAILED DESCRIPTION - Biogas fermentation system includes fermentation region containing raw material is formed between feed tube i.e. inlet tube and outlet tube. Air resistance plate is formed adjacent to fermentation zone or fermentation pipeline. Methane gas is produced by pushing biogas fermented liquid to flow in the adjacent areas. The fermentation zone is filled with methane. The biogas fermented liquid is continued to flow in adjacent fermentation area. The biogas fermentation annular pipe, where the level reaches to inlet tube and outlet tube sidewalls lowest position causes the biogas fermented liquid to overflow from the fermentation system. The biogas fermented liquid rises through feed tube and drains out due to hydraulic pressure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas fermentation system.    Inlet tube (10)    Outlet tube (20)    Fermentation pipeline (30)    Air resistance plate (34)    Fermentation region (301)
NOVELTY - Fermentation system comprises feedstock tube (10), discharging tube (20), fermentation pipeline (30), hydraulic pipeline and fermentation annular pipe. The annular pipe is provided with an opening at the center position extending on two sides from plate to clapboard. The bottom of feedstock pipe, discharging pipe (42) and annular pipe bottom are vertical. The feedstock pipe and side wall of discharging pipe extends to biogas liquid face of annular fermentation pipe below the seat and is connected with feedstock drain pipe between water pressure and feedstock pipe.    USE - Fermentation system used for producing biogas.    ADVANTAGE - The fermentation system is highly efficient.    DETAILED DESCRIPTION - Fermentation system comprises feedstock tube (10), discharging tube (20), fermentation pipeline (30), hydraulic pipeline and fermentation annular pipe. The annular pipe is provided with an opening at the center position extending on two sides from plate to clapboard. The bottom of feedstock pipe, discharging pipe (42) and annular pipe bottom are vertical. The feedstock pipe and side wall of discharging pipe extends to biogas liquid face of annular fermentation pipe below the seat and is connected with feedstock drain pipe between water pressure and feedstock pipe. The water discharging pipe and inner annular fermentation pipe are connected with one of the plate and an adjacent blocking plate (36) is provided in between to form fermentation area. The top part of fermentation area is set with an independent gas guide tube where the gas-guide tube is set with a valve.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the fermentation system.    Feedstock tube (10)    Discharging tube (20)    Fermentation pipeline (30)    Blocking plate (36)    Discharging pipe (42)
NOVELTY - Biogas pressure convection device comprises main body, oil inlet and outlet material cylinder and fermentation pipeline (30,40). The oil inlet and outlet material cylinder is connected with annular vertical pipe (30) to the fermentation pipe. The oil inlet and outlet material cylinder contains feed tube and discharge tube (34,42), where the feed tube is extended between the discharge pipe to bottom of the fermentation pipes and separates both. Pressure mounted on the top of the cylinder between the fermentation pipe is connected to feed tube and discharging pipe.    USE - Biogas pressure convection device.    DETAILED DESCRIPTION - Biogas pressure convection device comprises main body, oil inlet and outlet material cylinder and fermentation pipeline. The oil inlet and outlet material cylinder is connected with annular vertical pipe to the fermentation pipe. The oil inlet and outlet material cylinder contains feed tube and discharge tube, where the feed tube is extended between the discharge pipe to bottom of the fermentation pipes and separates both. Pressure mounted on the top of the cylinder between the fermentation pipe is connected to feed tube and discharging pipe. The fermentation pipe is connected with feedstock stopper plate (10). The discharge pipe is connected with gas feed pipe stopper plate. The gas feed pipe (36) stopper plate and outlet pipe is provided with one stopper plate. Fermentation zone is formed between adjacent air resistance plate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas pressure convection device.    Feedstock stopper plate (10)    Annular vertical pipe (30)    Fermentation pipeline (30,40)    Discharge tube (34,42)    Gas feed pipe (36)
NOVELTY - Methane fermentation system comprises cylinder provided with inlet (36) and outlet (46) and annular fermentation pipe (30). The methane fermentation system contains main body, oil inlet and oil outlet, which are connected vertically to the cylinder, which is connected to annular fermentation pipe. The cylinder is provided with feedstock tube (10) and discharging tube (20). The feedstock tube is connected with water inlet pipe and the discharging tube is connected with water draining pipe. The methane fermentation system also contains cloth bacterial unit which comprises inter-drain cloth.    USE - Methane fermentation system.    ADVANTAGE - The methane fermentation system is highly efficient.    DETAILED DESCRIPTION - Methane fermentation system comprises cylinder provided with inlet and outlet and annular fermentation pipe. The methane fermentation system also contains main body, oil inlet and oil outlet, which are connected vertically to the cylinder, which is connected to annular fermentation pipe. The cylinder is provided with feedstock tube and discharging tube. The feedstock tube is connected with water inlet pipe and the discharging tube is connected with water draining pipe. The methane fermentation system also contains cloth bacterial unit which comprises inter-drain cloth, cloth bacteria pipes, cloth bacteria hole, drain pipe and hydraulic connections. The cloth bacteria pipe is a circular pipe, which is fixed to the cloth bacteria fermentation pipeline wall. Drainage apparatus is placed horizontally.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane fermentation system.    Feedstock tube (10)    Discharging tube (20)    Annular fermentation pipe (30)    Inlet (36)    Outlet (46)
NOVELTY - Biogas pressure convection device comprises main body and oil inlet and outlet material cylinder. The oil inlet and outlet material cylinder is vertically connected to annular fermentation material pipe. The oil inlet and outlet material cylinder is connected with annular vertical pipe to the fermentation pipe. The oil inlet and outlet material cylinder contains feedstock pipe (20) and discharge tube (30), where the feed tube is extended between the discharge pipe to bottom of the fermentation pipes and separates fermentation pipelines.    USE - Biogas pressure convection device.    DETAILED DESCRIPTION - Biogas pressure convection device comprises main body and oil inlet and outlet material cylinder. The oil inlet and outlet material cylinder is vertically connected to annular fermentation material pipe. The oil inlet and outlet material cylinder is connected with annular vertical pipe to the fermentation pipe. The oil inlet and outlet material cylinder contains feedstock pipe and discharge tube, where the feed tube is extended between the discharge pipe to bottom of the fermentation pipes and separates fermentation pipelines. Pressure mounted on the top of the ring between the fermentation pipe, which is present between the feed tube is connected to drainage pipe. The drainage pipe is connected with discharge pipe between the feedstock pipe (46). Annular fermentation pipe and discharging pipe are connected with discharging pipe plate (36), blocking plate and feedstock material blocking plate. Fermentation area (40, 42) is formed between adjacent blocking plate. The fermentation area on the top is connected to air pipe, which is provided with valve.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the biogas pressure convection device.    Feedstock pipe (20)    Discharge tube (30)    Discharging pipe plate (36)    Fermentation areas (40,42)    Feedstock pipe (46)
NOVELTY - Producing biogas involves adding the raw material by feedstock pipe into U-type fermentation pipeline for producing marsh gas in U-type fermentation pipe. A discharging pipe is provided on the side wall for collecting marsh gas with an adjacent blocking plate in between to form a fermentation area. The marsh gas produced in the fermentation cell occupies space and extruded in fermented biogas slurry area. The biogas fermentation feedstock flows through the inner discharged pipe and cloth bacteria device and from the discharge pipe the feedstock flows into the drain pipe with a water pressure.    USE - Method for producing biogas (claimed).    ADVANTAGE - The method enables to produce biogas efficiently.    DETAILED DESCRIPTION - Producing biogas involves adding the raw material by feedstock pipe into U-type fermentation pipeline for producing marsh gas in U-type fermentation pipe. A discharging pipe is provided on the side wall for collecting marsh gas with an adjacent blocking plate in between to form a fermentation area. The marsh gas produced in the fermentation cell occupies space and extruded in fermented biogas slurry area. The biogas fermentation feedstock flows through the inner discharged pipe and cloth bacteria device and from the discharge pipe the feedstock flows into the drain pipe with a water pressure. The fermented marsh gas with water pressure flows to the biogas fermentation area and make the water pressure in the liquid storage pipe flow through one-way relux to the feedstock tube pipe, and cloth bacteria device to the inside fermentation pipeline. The feedstock in the fermentation cell is passed through the discharging tube pipe when the biogas slurry has lower water pressure. The biogas is stored by passing through only one-way relux into the feedstock tube drain pipe and cloth bacteria device to finish the circulation flow of slurry.
NOVELTY - Biogas fermentation system comprises feedstock tube (20), which is poured with fermentation material. The feedstock tube consist of annular pipe, which is present between discharging pipe (30) side wall and blocking plate (34) forming fermentation zone or fermentation zone for generating biogas is formed between adjacent blocking plate. The biogas fermented liquid is pushed to from the adjacent to the feedstock tube (46), discharging pipe (44) and cloth bacteria device through cloth bacteria pipeline. The fermentation zone, which is filled with methane flows to adjacent fermentation zone.    USE - Biogas fermentation system.    DETAILED DESCRIPTION - Biogas fermentation system comprises feedstock tube, which is poured with fermentation material. The feedstock tube consist of annular pipe, which is present between discharging pipe side wall and blocking plate forming fermentation zone or fermentation zone for generating biogas is formed between adjacent blocking plate. The biogas fermented liquid is pushed to from the adjacent to the feedstock tube, discharging pipe and cloth bacteria device through cloth bacteria pipeline. The fermentation zone, which is filled with methane flows to adjacent fermentation zone which is not completely filled. The fermented biogas flows in one direction. The fermented biogas stored in the lowest position of the cloth bacteria reaches drainage device for drainage. The fermented biogas is collected from reduced space to create reflux pressure.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the biogas fermentation system.    Feedstock tubes (20,46)    Discharging pipes (30,44)    Baffle plate (32)    Blocking plate (34)    Air pipe (36)
NOVELTY - Biogas comprises main body. Upper end of the main body is provided with inclined feeding pipe. The main body comprises heating layer, insulating layer and protective layer. The heating layer on its inner wall is provided with heating wire and four temperature sensor. Annular cavity is formed between the heating layer and the insulating layer. The annular cavity is filled with liquid. Outer wall of the protective layer is surrounded by the solar heat-absorbing wall. Bottom of the main body of biogas comprises tilt stepped structure and provided with high level impermeable layer and slag pool.    USE - Biogas.    DETAILED DESCRIPTION - Biogas comprises main body. Upper end of the main body is provided with inclined feeding pipe. The main body comprises heating layer, insulating layer and protective layer. The heating layer on its inner wall is provided with heating wire and four temperature sensor. Annular cavity is formed between the heating layer and the insulating layer. The annular cavity is filled with liquid. Outer wall of the protective layer is surrounded by the solar heat-absorbing wall. Bottom of the main body of biogas comprises tilt stepped structure and provided with high level impermeable layer and low level slag pool. The upper part of the main body is provided with Z type folding lid, which is edged and tanget to inner wall of the heating layer. The lower part of the lid is provided with support column. The outer wall of the protective layer is provided with rock wool, which is connected tightly with nylon straps to inlet end of the biogas and the main body.
NOVELTY - Purifying soil involves mixing microbial broth and gel liquid to obtain immobilized microorganism particle, which is added into soil for degrading high molecular weight polycyclic aromatic hydrocarbons and then plant is grown. The soil is added with crosslinking agent and proliferation culture medium.    USE - Method for purifying soil by degrading high molecular weight polycyclic aromatic hydrocarbons (claimed).    ADVANTAGE - The method enables to purify soil in eco-friendly manner.
NOVELTY - Biogas generating device involves pouring raw materials into feed tube (10). Annular fermentation pipe (32) and fermentation zone produce different amounts of methane. High pressure promotes fermentation zone (30) to release biogas, when fluid flow pressure is smaller then the pressure in fermentation zone. Biogas flows to adjacent fermentation zone. The fermented biogas slurry flows inside the tubes, when the liquid is squeezed into the feed tube. The feed tube and cloth bacteria unit causes fermented slurry to flow into room through the cloth bacteria unit with pressure.    USE - Biogas generating device.    DETAILED DESCRIPTION - Biogas generating device involves pouring raw materials into feed tube. Annular fermentation pipe and fermentation zone produce different amounts of methane. High pressure promotes fermentation zone to release biogas, when fluid flow pressure is smaller then the pressure in fermentation zone. Biogas flows to adjacent fermentation zone. The fermented biogas slurry flows inside the tubes, when the liquid is squeezed into the feed tube. The feed tube and cloth bacteria unit causes fermented slurry to flow into room through the cloth bacteria unit with pressure and remains in the room until the level reaches below lowest position. The fermentation slurry flows through a pipeline in unidirectional way to drain tube (20). Biogas slurry is stored between the feed tube and drain tube.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas generating device.    Feed tube (10)    Drain tube (20)    Fermentation zone (30)    Annular fermentation pipe (32)    Second fermentation area (302)
NOVELTY - The method involves controlling an inflow of general fresh water into a fluidity seasoned food polluted by the rainwater. The material molecules in which a specific gravity combined with a contaminant molecule are separated by a conveyor belt. The contaminant material molecules of a trace amount are cleaned or extracted from a fluidity material molecule. The fluidity material molecule comprising a general fresh water is flowed inside. The garbages combining two stages of an inclination separate board immediately flowed into a material molecule treating plant are removed.    USE - Nature-friendly environment-friendly method of purifying, reusing, mixing contaminant molecules with dissimilar material, and removing all binder molecules and suspended solidses combined with fluidity seasoned food from fresh water.    ADVANTAGE - The all kinds of the suspended solidses contaminants and all kinds of the garbages flowing into to the river with the rainwater are completely removed in a cost-effective manner. The effectiveness which uses the rainwater are displayed if all kinds of the particulate properties contaminants are mixed with the rainwater and flowed to the river. The rainwaters are purified and the domestic water is used in a daily life. The contamination of the lake or the dam is fundamentally prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the river sewage purification apparatus.    Vent (101)    Material molecule storage (1000)    Bottom water preferential exhaust path (1003)    Rear plate (1009)    Front plate (1010)
NOVELTY - Recycling kitchen garbage involves performing pre-treatment of integrated kitchen waste. The garbage having hydraulic material and biodegradable solids are removed. The hydraulic material is heated for melting out fat. The obtain material is floated to obtain defatted material. The defatted material is pulverized to obtain pulp, after sorting. The gravel impurities are treated to form slurry and discharged from bottom sides of container. The pH value of the obtained slurry is 6.5-7.5. The obtained slurry is digested anaerobically to produce biogas.    USE - Method for recycling kitchen garbage (claimed).    ADVANTAGE - The method enables to recycle kitchen garbage by generating less waste material and by efficiently recovering the resources.    DETAILED DESCRIPTION - Recycling kitchen garbage involves performing pre-treatment of integrated kitchen waste. The garbage having hydraulic material and biodegradable solids are removed. The hydraulic material is heated for melting out fat. The obtain material is floated to obtain defatted material. The defatted material is pulverized to obtain pulp, after sorting. The gravel impurities are treated to form slurry and discharged from bottom sides of container. The pH value of the obtained slurry is 6.5-7.5. The obtained slurry is digested anaerobically to produce biogas. The obtained biogas is purified to obtain predetermined concentration of methane.
NOVELTY - Floating-cylinder comprises a groove, floating tank, built-in tank for automatic gas lift, marsh gas and other fermentation tank into the float tank.    USE - Floating-cylinder for biogas production.    ADVANTAGE - The floating-cylinder is good for straw, leaves and weed waste.
NOVELTY - Producing methane from garbage involves mixing materials in a certain ratio and adding anaerobic fungus material in certain quantity. The system is sealed for fermentation at low temperature to obtain methane.    USE - Method for producing methane (claimed).    ADVANTAGE - The method enables to produce methane faster and digest a lot of waste producing organic fertilizer with high quality.
NOVELTY - Preparing ethanol involves crushing sorghum straw as a raw material and adding to the fermentation tank where the quality of raw material is 1-3%. Active dry wine yeast is mixed with the raw material and the mixture is kept for fermentation at natural temperature for 24-72 hours. The fermented product is then distillated to obtain ethanol.    USE - Method for preparing ethanol used as fuel (claimed).    ADVANTAGE - The method enables to prepare ethanol in a simple way and reduces the fermentation cost.
NOVELTY - Anaerobic tank comprises cylindrical brick body, hemispherical top and gas storage cabinet (6).    USE - Anaerobic tank.    ADVANTAGE - The anaerobic tank is economical, has brick structure that reduces the leakage of methane and improves the efficiency of biogas production.    DESCRIPTION OF DRAWING(S) - The drawing shows a vertical cross-sectional schematic view of an anaerobic tank.    Gas storage cabinet (6)    Gas outlet (7)    Automatic alarm (9)    Power stirring device (10)    Ladder (13)    Spiral warming device (14)
NOVELTY - Fermentation system comprises raw material feedstock cylinder (12), first stage fermentation system (10), second grade feedstock pipe (122), second stage fermentation system, and marsh gas fermentation area (13). The fermentation area is provided with blocking plate. The second stage fermentation system is provided with discharging pipe (124), drain pipe and cloth bacteria device. The marsh gas is generated in second stage fermentation system and accumulated at second level for discharging pipe. The marsh gas is stored in drain pipe.    USE - Fermentation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fermentation system.    First stage fermentation system (10)    Material feedstock cylinder (12)    Fermentation area (13)    Second grade feedstock pipe (122)    Discharging pipe (124)
NOVELTY - Methane generating system comprises raw material feedstock cylinder (12), first stage fermentation system (10), second stage feedstock pipe, second stage fermentation system and fermentation area (13). The fermentation area side wall is provided with inlet material cylinder and outlet material cylinder. The material cylinder is provided with blocking plate (15). The second stage fermentation system comprises discharge cylinder (114) and drain pipe and cloth bacteria device. The discharging pipe and drain pipe are connected to cloth bacteria device.    USE - Methane generating system.    ADVANTAGE - The methane generating system provides uniform distribution of fermentation strains.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of methane generating system.    First stage fermentation system (10)    Material feedstock cylinder (12)    Fermentation area (13)    Blocking plate (15)    Discharge cylinder (114)
NOVELTY - Preprocessing lignocellulosic raw material involves using ethylene diamine to treat the raw material.    USE - Method for preprocessing lignocellulosic raw material used for producing cellulosic ethanol (claimed).    ADVANTAGE - The method enables to preprocess lignocellulosic raw material which shows effective degradation of lignin and shows cellulosic enzymatic conversion of glucose with improved efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of enzymatic hydrolysis of lignocellulosic material, which involves mixing the pretreated lignocellulosic feedstock with cellulase, hemicellulase and water.
NOVELTY - Performing hydrolysis acidification includes using straw as raw material. The wheat straw are sliced and sieved, after sealing and kept for future use. The hydrolysis acidification is performed by placing sludge into hydrolysis acidification tank having alkaline medium and pH are regulated. The obtained material, which is hydrolysis acidification sludge (20-30g) is mixed with the obtained wheat straw. The hydrolysis acidification is performed by regulating pH for 18-20days. The sludge hydrolytic acidification is supplemented 0.4-1.0g per day.    USE - Method for performing acidification hydrolysis (claimed).    ADVANTAGE - The method enables to perform hydrolysis acidification of biological nitrogen and phosphorus, removes waste water and has significance in urban sewage treatment plant pollutant emission standard (GB18918-2002).    DETAILED DESCRIPTION - Performing hydrolysis acidification includes using straw as raw material. The wheat straw are sliced and sieved, after sealing and kept for future use. The hydrolysis acidification is performed by placing sludge into hydrolysis acidification tank having alkaline medium and pH are regulated. The obtained material, which is hydrolysis acidification sludge (20-30g), is mixed with the obtained wheat straw. The hydrolysis acidification is performed by regulating pH for 18-20days. The sludge hydrolytic acidification is supplemented 0.4-1.0g per day. The pH is regulated per day to maintain the initial pH. The upper layer clear liquid of the tank is hydrolysis acidification liquid.
NOVELTY - A marsh gas heating device comprises biogas device (1) and boiler (3) in which marsh gas device is embedded in the ground and has marsh gas pools connected in series.    USE - A marsh gas heating device for villages and towns.    ADVANTAGE - The device is environment-friendly, increases production efficiency of marsh gas, and has marsh gas supply stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for heating method of marsh gas heating device which involves properly positioning the marsh gas pool on the bottom digging pit for collective embedding, mounting the boiler, and connecting heating pipe and boiler to household.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a marsh gas heating device.    Biogas device (1)    Feedstock inlet (2)    Boiler (3)    Pipeline (4)    Household energy supply (5)
NOVELTY - Production of biogas involves inoculating and culturing papermaking surplus sludge in a hydrolysis acidification tank and obtaining a hydrolysis acidification solution, adjusting pH of solution to 8-10, pretreating the hydrolysis acidification solution by using fly ash as an adsorbent, inoculating the sludge and generating biogas by controlling the reaction temperature to 25 plus minus 5 degrees C and controlling the reaction pH value to 6-10, starting an anaerobic composite bed reactor and reacting and producing biogas by using hydrolysis acidification solution as external carbon source.    USE - Production of biogas from papermaking surplus sludge (claimed).    ADVANTAGE - The method efficiently and economically removes total nitrogen, total phosphorus and ammoniacal nitrogen, without causing pollution to the environment.    DETAILED DESCRIPTION - Production of biogas involves inoculating and culturing papermaking surplus sludge in a hydrolysis acidification tank and obtaining a hydrolysis acidification solution, adjusting pH of solution to 8-10, pretreating the hydrolysis acidification solution by using 5-25 g fly ash as an adsorbent, inoculating the sludge and generating biogas by controlling the reaction temperature to 25 plus minus 5 degrees C and controlling the reaction pH value to 6-10, starting an anaerobic composite bed reactor and reacting for 10-50 minutes, determining the conditions of the biogas producing process, and producing the biogas by using the hydrolysis acidification solution as an external carbon source.
NOVELTY - Preparation of biodiesel using flower-shaped nickel based catalyst involves placing flower-shaped nickel-based catalyst in a batch reactor, reducing catalyst metal component at 300-500 degrees C for 2-6 hours under hydrogen partial pressure of 2-5 MPa, adding vegetable oil to the reactor in a solid-liquid ratio of 0.01-0.1 and carrying out hydrocracking under hydrogen partial pressure of 2-5 MPa at 300-400 degrees C.    USE - Preparation of biodiesel using flower-shaped nickel based catalyst (claimed).    ADVANTAGE - The method prevents hydrogen sulfide corrosion of the equipment, environmental pollution and health hazards by using non-vulcanized flower-shaped nickel based catalyst. The high nickel content in the catalyst metal and large aperture increases raw material conversion rate and product selectivity. The catalytic efficiency of the catalyst is increased by 10 times than alumina catalyst.
NOVELTY - A Trametes pubescens strain BJFCC1108 having preservation number CGMCC No. 10308 is new.    USE - A Trametes pubescens strain BJFCC1108 having preservation number CGMCC No. 10308 for production of laccase used in degradation of aromatic amines (derivatives) and aromatic carboxylic acid (derivatives), dye, pulp and paper, environmental protection, food manufacturing, cosmetics production, bioremediation, bioassay, biofuels, bioenergy, organic synthesis, and fiber applications (all claimed).    ADVANTAGE - Laccase can be produced in high yield. Laccase exhibits high enzyme activity, stability, and tolerance to metal ions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) use of Trametes pubescens strain BJFCC1108 having preservation number CGMCC No. 10308 in preparation of laccase; and (2) laccase generated by T. pubescens.
NOVELTY - Detecting B-raf gene Val600Glu mutation comprises: (a) extracting DNA using nonionic polyoxyethylene (NP)-40, chelex100, and Tris-HCl; (b) performing DNA polymerase, preferably using TaqDNA polymerase (without exonuclease activity); and (c) preparing PCR reaction solution comprising deoxynucleotide triphosphates (dNTPs), primers, DNA polymerase, PCR buffer, and labeled probe.    USE - The method is useful for detecting B-raf gene Val600Glu mutation (claimed). Preferably, it can be used for detecting whether a particular nucleotide variation exists in the B-raf gene in the DNA sample isolated from the patient body in vivo.    ADVANTAGE - The method is simple, fast, accurate, easy to process, and pollution-free; and has high accuracy and high sensitivity.
NOVELTY - Rapid preparation of biological nitrogen by adding simulated lunar soil filler involves taking biological film anaerobic ammonia oxidation reactor, selecting simulation lunar particle as filler, placing in reaction cell of reactor, mixing nitration sludge and anaerobic sludge, adding in reactor, adding simulation lunar particle, flowing water bath, pumping wastewater using crawling pump, mixing mixed reaction sludge and soil in wastewater in reaction zone, carrying out liquid-gas separation, flowing water from biofilm reactor in overflow weir, discharging gas from top of reactor.    USE - Method for rapid preparation of biological nitrogen by adding simulated lunar soil (claimed).    ADVANTAGE - The method enhances sludge retention.    DETAILED DESCRIPTION - Rapid preparation of biological nitrogen by adding simulated lunar soil filler comprises taking biological film anaerobic ammonia oxidation reactor provided with three phase separator and reaction cell, selecting simulation lunar particle as filler, placing in reaction cell of reactor, placing three phase separator above reaction cell, mixing nitration sludge and anaerobic sludge at mass ratio of 8:1-10:1 for inoculation, adding in reactor, adding simulation lunar particle, flowing constant temperature circulation water bath for heating in reaction area at 30 plus minus 1 degrees C, adopting continuous water feeding mode under close shading condition, pumping wastewater in bottom of reactor using crawling pump, mixing mixed reaction sludge and soil in wastewater in reaction zone, fixing three-phase separator, carrying out liquid-gas separation, flowing water from biofilm reactor in overflow weir, discharging gas from top of reactor.
NOVELTY - The system has a garbage chamber whose one end is provided with a garbage inlet, and other end is connected with a water power sorting device. A sewage purification device is connected to the crushing and dispensing device connected with the pressure hydro-thermal processing device. The end of the pressure hydro-thermal processing device is connected with the methane fermentation device. The methane fermentation device is provided to send the products respectively to the biogas tank and the residue fermentation pool.    USE - Hydraulic high speed sorting fermentation system for municipal domestic organic garbage such as paper and plastic. Can also be used in wood, grass, animal bone, metal, cement, glass, and vegetable.    ADVANTAGE - The sorting operation is performed reliably, and the production cost is reduced. The energy saving environment-friendly sorting fermentation system is realized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the application of hydraulic high speed sorting fermentation system for municipal domestic organic garbage.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the municipal domestic organic garbage hydraulic high speed sorting fermentation system. (Drawing includes non-English language text)
NOVELTY - A Schizochytrium limacinum strain 6961Y01 (CGMCC NO: 9043), is new.    USE - The S.limacinum is useful for producing crude glycerol which is used for producing biodiesel (all claimed).    ADVANTAGE - The S.limacinum enables to produce biodiesel with increased palmitic acid content of 50% and reduced dihydroxyacetone content of 30%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for culturing S.limacinum to produce crude glycerol involves activating S.limacinum in seed culture medium, performing culturing and fermentation process, and centrifuging fermented product.
NOVELTY - Pretreatment of penicillin slag involves dehydrating penicillin slag of pharmaceutical factory for producing antibiotics, adding distilled water, stirring, obtaining fermentation feedstock, placing the fermentation feedstock in a microwave oven, decomposing at 100-105 degrees C for 5-65 seconds, cooling, obtaining decomposed penicillin slag, mixing the decomposed penicillin slag with anaerobic sludge in ratio of 1 g:(1-1.5) mL, obtaining mixed liquid, adjusting pH value to 7 using sodium bicarbonate, adjusting carbon/nitrogen ratio to 20 using starch, and obtaining fermenting liquid.    USE - Pretreatment of penicillin slag in production of anaerobic biogas.    ADVANTAGE - The method improves yield of anaerobic biogas.    DETAILED DESCRIPTION - Pretreatment of penicillin slag involves dehydrating penicillin slag of pharmaceutical factory for producing antibiotics, adding distilled water, stirring, obtaining fermentation feedstock, placing the fermentation feedstock in a microwave oven, decomposing at 100-105 degrees C for 5-65 seconds, cooling to room temperature, obtaining decomposed penicillin slag, mixing the decomposed penicillin slag with anaerobic sludge in ratio of 1 g:(1-1.5) mL, obtaining mixed liquid, adjusting pH value to 7 using sodium bicarbonate, adjusting carbon/nitrogen ratio to 20 using starch, and obtaining fermenting liquid. The mass-volume ratio of penicillin slag and distilled water is 1 g:(0.2-0.5) mL. The dehydrated penicillin slag has moisture content of 72-78% and solid content of 22-28%, and contains 45-49 %mass carbon, 9.5-11.5 %mass nitrogen, 6.7-7.5 %mass hydrogen and 1.6-2.5 mg/g penicillin residue.
NOVELTY - The device has a reaction type flowing chamber whose internal volume is divided into upper and lower cavities by horizontal partition produced in the form of molecular membrane permeated with vapors of methyl alcohol and vapors of methyl fatty acid esters. The lower cavity of reaction chamber is provided with continuous supply of liquid reagents and outlet for continuous unloading of reaction products. The upper cavity of reaction chamber is communicated with a refrigeration chamber through a branch pipe.    USE - Device for preparing base component of biodiesel fuel from vegetable oils.
NOVELTY - The unit comprises an electrolyzer (11) that has a housing containing plate electrodes and is electrically connected to a feed source. The housing is connected to a container (14) filled with water based electrolyte solution. The housing has a pipe (5) for gas and water mixture removal and a pipe (6) for collecting gaseous mixture of hydrogen and oxygen. At least one ultrasonic radiation source in the electrolyte for weakening the molecular bonds of the electrolyte. Dilute solution of water with sodium hydroxide is used as the electrolyte. The electrolyte container is air tight and has an inlet for electrolyte supply forming an unfilled space above the electrolyte surface. The hydrogen and oxygen gaseous mixture collection pipe has a water lock (8) and is connected to the container unfilled space. An ultraviolet radiation source is located in the housing. The electrodes are made as a collection of stainless steel plates with vertical and horizontal notches on their surfaces and openings for electrolyte circulation and gas outlet. The openings in the electrode plates are not coaxial    USE - In the field of electrochemistry.    ADVANTAGE - The output and efficiency are increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the unit for production of gaseous hydrogen and oxygen    Pipe for gas and water mixture removal (5)    Pipe for collection gaseous mixture of hydrogen and oxygen (6)    Water lock (8)    Electrolyzer (11)
NOVELTY - The conveyance machine has a blade portion (32) that is conveyed to agglomerating machine stirring granulated material supplied from kneading machine. A casing (20) is provided to cover blade portion. A drive portion is provided to rotate blade portion at rotational speed from which space factor of granulated material inside the casing becomes predetermined range. A gas exhaust port is provided to discharge gas emitted from granulated material. The casing is equipped with hollow portion (21) formed between gas exhaust port and blade portion.    USE - Conveyance machine such as screw conveyer.    ADVANTAGE - Since the space factor of the granulated material inside the casing rotates the blade portion at the rotational speed used as the predetermined range, the granulated material is deaerated efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a conveying method involves producing a globular form carbon by carrying out globular form of the granulated material. The space factor is of 40%-60% of the predetermined range.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional side view of the screw conveyer.    Screw conveyer (10c)    Casing (20)    Hollow portion (21)    Conveyance portion (30)    Blade portion (32)
NOVELTY - Manufacture of electrode involves electrodepositing alloy composition comprising 2.9-65 atomic% iron, 0.6-10 atomic% carbon, 5 atomic% or more nickel and 0.1 atomic% or more cobalt on electrode base material using plating liquid comprising soluble iron salt, soluble nickel salt, soluble cobalt salt, aminocarboxylic acid and boric acid, and having pH of 2 or less, at 500 A/m2 or less.    USE - Manufacture of electrode used for aqueous electrolysis to generate hydrogen and oxygen.    ADVANTAGE - The method enables manufacture of electrode having excellent durability and uniformity, by simple and economical process, within short period of time. The electrode enables hydrogen generation with reduced energy consumption.
NOVELTY - A photobioreactor for carbon dioxide biosequestration with immobilized biomass of algae or cyanobacteria comprises closed structure divided into segments in which algae or cyanobacteria are immobilized in capsules (3) of 5-40 mm diameter.    USE - A photobioreactor for carbon dioxide biosequestration with immobilized biomass of algae or cyanobacteria.    ADVANTAGE - Monitoring and controlling of light intensity and exposure time, pH value and temperature of culture and purity, and lifetime of culture of selected strain of algae or cyanobacteria are allowed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the photobioreactor.    Capsules (3)    Outer envelope (4)    Light tube (5)    Light source (6)    Conduit inlet (7)
NOVELTY - Preparing sitagliptin (I), comprises either: (a) treating (3R)-3-((tert-butoxycarbonyl)amino)-4-(2,4,5-trifluorophenyl)butanoic acid (II) with 3-(trifluoromethyl)-5,6,7,8-tetrahydro(1,2,4)triazolo(4,3-a)pyrazine (III) or its salts in the presence of a catalyst e.g. trialkyl borate to obtain tert-butyl ((2R)-4-oxo-4-(3-(trifluoromethyl)-5,6-dihydro(1,2,4)triazolo(4,3-a)pyrazin-7(8H)-yl)-1-(2,4,5-trifluorophenyl)butan-2-yl)carbamate (IV), and (b) deprotecting (IV) in the presence of an activated zeolite to obtain (I); or the step (b) as above per se.    USE - The process is useful for preparing sitagliptin (I), which is useful in treatment of type 2 diabetes mellitus. No biological data given.    ADVANTAGE - The process: avoids the use of hazardous and costly reagents e.g. 1-hydroxybenzotriazole and 1,1'-carbonyldiimidazole, hence it is more commercially viable, and cost effective; requires less time; facilitates the recycling of activated zeolite; and eliminates the step of purification step to remove the unwanted side products, as compared to conventional processes.    DETAILED DESCRIPTION - Preparing sitagliptin of formula (I), comprises either: (a) treating (3R)-3-((tert-butoxycarbonyl)amino)-4-(2,4,5-trifluorophenyl)butanoic acid of formula (II) with 3-(trifluoromethyl)-5,6,7,8-tetrahydro(1,2,4)triazolo(4,3-a)pyrazine of formula (III) or its salts in the presence of a catalyst to obtain tert-butyl ((2R)-4-oxo-4-(3-(trifluoromethyl)-5,6-dihydro(1,2,4)triazolo(4,3-a)pyrazin-7(8H)-yl)-1-(2,4,5-trifluorophenyl)butan-2-yl)carbamate of formula (IV), where the catalyst is a trialkyl borate, or a mixture of boric acid and a trifluoromethyl phenylboronic acid, and (b) deprotecting (IV) in the presence of an activated zeolite to obtain (I); or the step (b) as above per se. An INDEPENDENT CLAIM is also included for preparing (IV) comprising the step (a) as above per se.
NOVELTY - The method involves stirring organic waste thrown into the digester main portion (1) by a stirring apparatus (2). The organic waste is heated by a heating apparatus (4). The ratio of the quantity of the digestion gas emitted in the digester main portion with respect to the quantity of the organic waste thrown into the digester main body is lower than predetermined value. The stirring apparatus is operated and the stirring strength of organic waste is raised, if the temperature difference of the organic waste in the digester main portion is set to predetermined value or more.    USE - Method for operating digester for carrying out anaerobic fermentation process of organic waste such as sewage sludge and foodstuff waste material.    ADVANTAGE - The low power operation of the digester is achieved, and the maintenance efficiency of digester is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional side view of the digester. (Drawing includes non-English language text)    Digester main portion (1)    Stirring apparatus (2)    Heating apparatus (4)    Heat exchanger (15)    Digester (100)
NOVELTY - The digester (100) has digester main portion (1) made from a steel plate by which liquid phase portion (11) fermentation-processing the thrown-in sludge, and gaseous-phase portion (12) containing sewage gas produced by sludge fermentation process are formed in inside. A test piece accommodation unit (4) accommodates a test piece (S) of same composition as portion that contacts gaseous-phase portion. A storage chamber (41) accommodates test piece in interior space (42) in a state observable from exterior. A communicating path (46) connects interior space and gaseous-phase portion.    USE - Steel digester for fermentation-processing of sludge e.g. organic waste e.g. sewage sludge and foodstuff waste material.    ADVANTAGE - The corrosion condition of the portion contacting the gaseous-phase portion is acquired easily even if the digester is working.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the steel digester. (Drawing includes non-English language text)    Digester main portion (1)    Test piece accommodation unit (4)    Liquid phase portion (11)    Gaseous-phase portion (12)    Storage chamber (41)    Interior space (42)    Communicating path (46)    Steel digester (100)    Test piece (S)
NOVELTY - Preparation of alkanolamine compound (salt) (I) or (II) involves preparing glycidol in a one-pot reaction of glycerol with dimethyl carbonate at a temperature of 100-160 degrees C in the presence of an ionic liquid catalyst (III), and reacting the glycidol with amine (IV). The molar ratio of glycerol with respect to dimethyl carbonate used during the preparation of glycidol is 1:4-1:10.    USE - Preparation of alkanolamine compound (salt) used for removing carbon dioxide and/or hydrogen sulfide from carbon dioxide and/or hydrogen sulfide-containing gaseous stream e.g. methane-containing gaseous stream, natural gas stream, biogas-derived stream, flue gas stream, and breathing gas stream for life support system (all claimed).    ADVANTAGE - The method enables efficient preparation of alkanolamine compound (salt) with high carbon dioxide absorption capacity, by economical process.    DETAILED DESCRIPTION - Preparation of alkanolamine compound (salt) of formula (I) or (II) involves preparing glycidol in a one-pot reaction of glycerol with dimethyl carbonate at a temperature of 100-160 degrees C in the presence of an ionic liquid catalyst of formula: (Cat+)(X-) (III), and reacting the glycidol with amine of formula (IV). The molar ratio of glycerol with respect to dimethyl carbonate used during the preparation of glycidol is 1:4-1:10.    R1,R2=H, polysaccharide group, polyethylene oxide group, or linear or branched 1-8C alkyl, linear or branched 2-8C alkenyl, 3-8C cycloalkyl, 6-10C aryl, or 3-10-membered heterocyclyl (all optionally substituted by 1-6C alkoxy, 2-8C alkoxyalkoxy, 3-8C cycloalkyl, 6-10C aryl, 3-10 membered heterocyclyl, 7-10C aralkyl, 3-10-membered heterocyclyl-1-4C alkyl, -OH, -CH2CH(OH)CH2(OH), -CH(CH2OH)2, or -NR3R4);    R1+R2+N=heterocyclyl;    R3,R4=H or linear or branched 1-6C alkyl;    (Cat+)=cationic species;and    (X-)=anionic species.
NOVELTY - The device has a reactor provided with a double layer and a contact reaction layer. A purification filler is connected with an air inlet pipe. The reactor generates flue gas in the purification filler and a solution collecting tank. The reactor is equipped with the double layer that is formed under the contact reaction layer of a solution pool in which a circulation pump is connected. An upper outlet of the circulation pump is connected with a circulation water pipe. A weir plate is arranged with a front baffle plate. A water pipe is connected with a waste liquid valve.    USE - Solid organic waste aerobic fermentation deodorizing device for a factory.    ADVANTAGE - The device reduces running cost, saves energy and protects environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a side perspective view of a solid organic waste aerobic fermentation deodorizing device.
NOVELTY - This new utility model claims of a kind of biomass gas in parallel one production system, comprising spiral feeder is in parallel, large angle transmitter, belt transmitter, a biomass gasification furnace, a cyclone separator, spray tower, a gas-liquid separator and electric tar capturing device. Biological gas production system implementation in parallel using multiple gas in furnace in parallel to be collective gas platform, purification system delivery system and in parallel and is matched in parallel, using optimal mutually in production equipment configuration, reducing production equipment idle time, which is good for unified plan management production, saves labour resource integration, when local device when the system happen fault service not influence whole operation.
NOVELTY - Manufacture of ethanol involves carrying out chemical preparation of lignocellulosic raw material by chemical treatment process, performing saccharification of chemically processed raw material suspension using an enzyme, and carrying out saccharification fermentation process using fermentation microorganisms. The weight ratio of solid content after the chemical processing with respect to the solid content before chemical processing in the chemical treatment process is 30-80%.    USE - Manufacture of ethanol used as fuel.    ADVANTAGE - The method enables efficient manufacture of ethanol with high productivity for long period of time and reduced discharge amount of non-decomposed residue after saccharification process.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of ethanol manufacturing apparatus. (Drawing includes non-English language text)    Saccharification fermenter (BR)    Heat treatment equipment (CO)    Vacuum distillation apparatus (EV)    Uniaxial crusher (I)    Grinding apparatus (R)
NOVELTY - Furfurals and ethanol are manufactured from biomass by supplying aqueous suspension of biomass to primary hydrolysis apparatus (R1) through supply port (A), pre-hydrolyzing biomass to produce furfurals, discharging pre-hydrolyzed suspension from discharge port (B) of primary hydrolysis apparatus, separating pre-hydrolyzed liquid from pre-hydrolyzed suspension in solid-liquid separation apparatus (S), taking out from intermediate extraction opening (G), separating furfurals from pre-hydrolyzed liquid, adding fermentation microorganism to liquid phase, and collecting ethanol.    USE - Manufacture of furfurals and ethanol from biomass.    ADVANTAGE - Ethanol production is improved by adding enzyme and yeast to process liquid which remains after performing secondary pre-hydrolysis processing and separating furfural simultaneously.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of an apparatus for manufacturing furfurals and ethanol from biomass.    Raw material suspension supply port (A)    Pre-hydrolyzed suspension discharge port (B)    Intermediate extraction opening (G)    Primary hydrolysis apparatus (R1)    Solid-liquid separation apparatus (S)
NOVELTY - The utility model claims a new garbage transfer station of waste gas treatment system, comprises using garbage compressor surround the negative pressure sealing cover, plasma waste gas treating device, a tail gas processing device, fan, negative pressure sealing cover by blower and plasma waste gas treating device connected with the plasma waste gas treating device and tail gas processing device connected with, a fan setting on leading end, using induced in forming negative pressure and discharging the gas after purification. Wherein, negative pressure sealing cover using transparent endurance board composed of closed form negative pressure area pollution source, negative pressure sealing cover top mounting skirt and pipeline connection. This utility model through set a negative pressure closeness area around a garbage compressor collecting malodorous gas, can effective preventing odour, collection of malodorous gas discharge pipe through a plasma waste gas process and a gas treatment, the whole system structure is simple, can be large wind quantity, high efficiency of complete malodorous gas processing, purification gas discharge accord with state standard.
NOVELTY - A methanol fuel additive contains 30-45 vol.% ethanol, 10-15 vol.% methylethylbenzene, 10-20 vol.% isobutanol, 2-8 vol.% n-butanol, 5-10 vol.% diethyl ether, and 20-50 vol.% solvent oil.    USE - Methanol fuel additive is useful for vehicle methanol gasoline (claimed).    ADVANTAGE - Methanol fuel additive can reduce emission of pollutants, and does not require modification of original vehicle engine.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for vehicle methanol gasoline, which contains 80-84 vol.% gasoline, 15 vol.% industrial methanol and 1-5 vol.% methanol fuel additive.
NOVELTY - The utility model relates to one kind novel composite type biologic diesel esterification reaction device, the structure comprises first-stage reaction tank, first-stage nano colloid mill, three-way valve connected with the second grade reaction tank and second level nano colloid mill, the first-stage reaction tank, first-stage nano colloid mill, three-way valve connected with the second grade reaction tank and second level nano colloid mill connected in sequence. The utility model is novel effective treatment containing longer chain of macromolecule raw material lipid, reducing methanol waste rate and improve raw material and reaction rate of methanol, realize fast single circulation esterification reaction and fast switching between the two time circulation esterification reaction, the biological diesel oil and product quality.
NOVELTY - The new type utility claims one kind have urine collecting device for urology surgery, comprising cone container, a liquid inlet funnel and upper cover plate, upper cone container side through pipe connected with the liquid inlet funnel, a liquid inlet funnel on side provided with upper cover plate, upper side at outside wall set with handle, on upper cone container on side pipe provided with urine detection alarm device, cone container outside wall set with insulating layer, cone container on side outside wall at set with temperature sensor, the utility model is new type urine collecting device for urology surgery, good stability, high reliability, simple and sanitary, convenient for patient and doctor for urine collection and sampling operation, relieving have working burden, to temperature of urine can carry out control to avoid have over-high temperature and cause bacteria, on stability, cover the upper cover board have urine examination result and time can the urine collecting device is sealing state, which avoids have urine smell to hospital environment cause the pollute, and moving device suitable and fast, strong practicability and high convenience.
NOVELTY - The utility model is new type relates to one kind pharmaceutically acceptable colour-changing package film, wherein, comprising aluminium foil layer, upper surface of the aluminium base layer set with OP protective layer, provided with bi-direction stretching polypropylene layer on the aluminium foil layer, the lower part between the OP protective layer and the aluminium foil layer, the aluminium foil between base layer and the bi-direction stretching polypropylene layer respectively connected by aqueous adhesive printed with colour-changing ink layer towards the aluminium foil layer on one side in the OP protective layer. The utility model is new type of beneficial effect wherein the tensile strength, to water vapour, light line with the high barrier property, non-toxic and environment-friendly, light intensity in specific illumination intensity lower surface can be a different color, to the user at that time medicine storage environment and, using suitable and save period longer, with practicability.
NOVELTY - The utility model is new type relates to one kind of medicine package for belt type foam aluminum cover, comprising aluminium foil layer, upper surface of the aluminium base layer set with OP protective layer, provided with heat seal coating part on the aluminium foil layer, the heat seal coating is polyurethane adhesive layer, medicine package for belt type foam cover aluminum thickness is 100 (mu) m to 130 (mu) m. The utility model is new type of beneficial effect wherein, good leak tightness, simple structure, reasonable design, non-toxic and environment-friendly, for separating the water vapour, oxygen and light performance, with practicability.
NOVELTY - A substituted chiral cyclohexane coordinated spiral pyrazolone derivative (I) is new.    USE - Substituted chiral cyclohexane coordinated spiral pyrazolone derivative used in preparing drug for treating inflammation (claimed).    ADVANTAGE - The compound is safe to use and has no toxicity. The preparation method of the compound is simple to carry out and green and environment-friendly.    DETAILED DESCRIPTION - A substituted chiral cyclohexane coordinated spiral pyrazolone derivative of formula (I) is new.    R1=phenyl, 4-MeC6H4, 4-MeOC6H4, or 2-ClC6H4;    R2=phenyl, 3-C1C6H4, 4-BrC6H4, 4-OMeC6H4, 4- tBuC6H4, 2-thienyl, or CH=CH-phenyl;    R3=phenyl, 4-FC6H4, 4-OMeC6H4, 4-tBuC6H4, or 2-furanyl; and    R4=Me, Et or n-propyl.    An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - The utility model claims a new A mice intraperitoneal administration in a device, a base cavity, base cavity is set with the lower part with a tool in the tool set in left right two separately set up with a left supporting column and a right column, base cavity connected with the upper upright post, upright post on left side lower part respectively connected with a cross plate and a transverse plate, the transverse plate and lower transverse plate at left side is set with supply with medicine in the medicine supply in left side connected with tube, left side connected with Drug medicine, medicine in a supply part connected with discharging soft pipe, right side flexible pipe connected with administration tube, supply medicine in a part formed with piston, piston upper part connected with piston connecting rod, piston connecting rod part connected with handle on the base in a part formed with administration in. This new utility model can a destination device aims to mice intraperitoneal administration in, medicine convenient observation, but the following part mice convenient fixing, improving of experiment effect, suitable use, and a suitable administration auxiliary tool, protecting environment.
NOVELTY - The utility model provides a waste gas processing system in organic fertilizer production process. It comprises: a leading-out device, a flue gas leading-out device comprises the exhaust passage, a organic fertilizer raw material storage pool, organic fertilizer fermentation device and second time oxygen ferment device, waste heat recovery device, wherein a leading-out device is set with a gas collecting device between the gas collecting device, connected with a flue gas leading-out device, the other end is set with washing a d a, water washing, alkali washing and a gas collecting discharging device enter into a water washing pool, gas water washing and collecting enter into tower discharge, discharge tower, tower top set up with discharge port, a tower part and a cavity body provided with processing liquid spray device, processing liquid a configuration, a circulation pump for the processing liquid sending pump to discharge tower lower part of cavity body. The utility model is a new supply of organic and a production process of a processing system with zero discharge, comprising a heat recycling, environmental protection, high efficient, reduce production consumption.
NOVELTY - The utility model claims a... automatic biomass microwave heat de-machine, equipped with sealed microwave pyrolysis furnace, pyrolysis in machine frame, power control unit, a liquid separating condenser, cooling device, frame is set with sealed microwave pyrolysis furnace, the gap between the sealed microwave pyrolysis furnace and pyrolyzing machine as a cooling cavity, the cooling cavity connected with a cooling device, a closed microwave pyrolysis furnace equipped with microwave generator, microwave of pyrolysis furnace, a machine frame provided with a discharging device, pyrolysis furnace through air suction pipe connected with the oil liquid separating condenser, electric control unit respectively connected with said sealed microwave pyrolysis furnace, cooling device. This new utility model reducing a weight and a up and down material, increase of working efficiency, reducing a coal preparing cost. Carbonization technique is advanced, short period, high yield.
NOVELTY - The utility model claims a small high efficient multifunction of marsh gas ferment device,wherein it comprises: a fermentation tank, a seal. In the fermentation tank top part of top cover, a set up of a marsh gas output pipe on the header, one in a fermentation tank equipped with a feedstock of a part, one is set with a discharging pipe of the said fermentation tank side wall, one in the fermentation tank is set with centre of marsh gas pipe, a rotation of a joint is set on the marsh gas pipe of sleeve, one located in the fermentation tank and a material a fastening sleeve in the sleeve of the joint, a fastening is inserted into a a a a a a a a cannula, and is set with a heat preservation device A and the fermentation tank outer side, wherein, the marsh gas pipe and upper end connected with a gas compressor and output end, a a a a a a bracket at bottom of the fermentation tank, wherein the fermentation tank is located outside the sleeve is connected with a rotary driving device on. The utility model can be widely used for preparing a small biogas fermentation process.
NOVELTY - Top part of the new utility model claims of a kind of temperature controllable one of Anaerobic reaction experiment device, comprising reactor tank body, a feedstock tube and discharging tube, feedstock pipe and discharging pipe are equipped with bottom in the reactor jar body, jar body and lower part equipped with reactor heating tank, heating inner tank filling with heat guide medium, heating tank and reactor tank body is integrated structure, heating the inner tank bottom equipped with electric heating device, heating the part of inner tank equipped with heat exchange pipe, two end heat exchanging pipe are connected and the bottom the reactor tank body, reactor tank body provided with a flexible membrane and out film, top part tank body and outside membrane reactor is set on the flexible membrane and external, also provided with discharge pipe, discharge pipe and flexible membrane and reactor tank body between the closeness cavity connected with. This new utility model by setting heating device on the bottom, indirectly heating the biogas slurry in tank, can free control of temperature in tank, using Anaerobic reactor not limited by the influence of the outside world temperature, with simple structure and manufacture cost is low.
NOVELTY - The utility model is a model of a dual blade marsh gas fermentation full mixing stirring device, belonging to environment protection and a regeneration energy area, with a speed reducer base, a reversing switch, a speed reducer, a shaft joint, a sealing part, slide key shaft, double blade stirring wing, a slide key set a lead screw, to fix silk, ball bearing, outside sleeve, shaft, marsh gas tank. The utility model using a double spiral propulsion stirring blade, a light and consume low power, a sealing component designed on a filler seal, sealing is simple and reliability, at the same time through a slide key shaft, ball bearing and slide key set a lead screw, to fix silk nut and double blade stirring fin active combination, a double blade stirring wing not only can rotate along circle direction in a marsh gas tank, then a along a translation, from a tank of a the other end back and forth to do spiral movement, can place a material liquid in the marsh gas tank for full mixing stirring, the stirring effect is good, promoting marsh gas tank a volume increase of yield, at the same time of greatly reducing a stirring power consume, saving energy consumption.
NOVELTY - Preparation of zinc indium sulfide nanoparticles, involves: (a) reacting zinc nitrate hexahydrate (Zn(NO3)2.6H2O), indium nitrate pentahydrate (In(NO3)3.5H2O), thiourea and triethylamine for a time period ranging from 0.5-1.0 hour followed by treating hydrothermally at a temperature ranging between 100 degrees C and 200 degrees C for a time period ranging from 12-48 hours to obtain a precipitate; and (b) separating and iteratively washing the precipitate with a solvent to obtain zinc indium sulfide nanoparticles, where the concentration of the triethylamine ranges from 100-1000 ppm.    USE - The processes are useful for preparing zinc indium sulfide nanoparticles, and generating hydrogen (all claimed).    ADVANTAGE - The process provides a simple, inexpensive and efficient process for the preparation of zinc indium sulfide (ZnIn2S4) nanostructured compound, and a process that converts hydrogen sulfide (H2S) into hydrogen (H2).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for generating hydrogen, which involves: (a) reacting Zn(NO3)2.6H2O, In(NO3)3.5H2O, thiourea and triethylamine for a time period ranging between 0.5 hour and 1.0 hours followed by treating hydrothermally at a temperature ranging between 100-200 degrees C for a time period of 12-48 hours to obtain a precipitate; (b) separating and iteratively washing the precipitate with at least one solvent selected from methanol, ethanol, propanol, isopropanol and butanol to obtain zinc indium sulfide nanoparticles; and (c) adding zinc indium sulfide nanoparticles into a reactor containing an aqueous alkaline solution saturated with hydrogen sulfide and irradiating using visible light at a wattage of 200-500 W, where the concentration of the triethylamine ranges between 100-1000 ppm and the process generates hydrogen at the rate of 4000-5500 mu mol/hour/half gram of zinc indium sulfide nanoparticles.
NOVELTY - Method of preparation of poultry droppings for the subsequent use as a part of multicomponent loading raw materials of the single-chamber biogas unit includes microbiological processing of poultry droppings and adding of bioadditives in a liquid form, execution of biological warming up and fermentation of the mix, and the used bioadditive is effluent, amounting 20-25% of the total mass of poultry droppings which comprise mineral fertilizers - N:P:K amounting 0.1:0.16:0.18% respectively and native microflora with the density of microorganisms 260x108 CFU/ml then the obtained substratum is held within 7-9 days in anaerobic conditions, and then is supplied into the biogas unit reactor amounting 15% of loading weight.    USE - Agriculture.    ADVANTAGE - Invention allows to reduce the time of fermentation process, to use a poultry droppings as one of components of the combined raw materials for a single-stage fermentation; to exclude negative impact of harmful components of initial dung on activity of the microorganisms participating in fermentation process.
NOVELTY - The utility model is new type relates to one kind active yeast raw material storing device, belonging to fermentation production equipment field. Above technology scheme is: cold water storage tank (2) in turn through tank outlet water out valve (4), refrigeration for water pump (5), a refrigerating inflow valve (6) and the refrigerator (3) is connected, the refrigerator (3) through cold water out water outlet valve, cold water pump (10) and raw material storage tank cooling jacket (14) is connected, the raw material storage tank cooling jacket (14) setting in raw material storage tank (13) outside internal, the raw material storage tank (13) set with stir device two (12), a raw material storage tank (13) is provided with a thermometer (16), raw material storage tank cooling jacket (14) by cold water outlet water valve and the cold water storage tank (2) is connected. The utility model is new type of beneficial effect is: cold water circulation use, saves energy and at the same time would not to cause environmental pollute. At the same time it can realize large scale storage need, the biologic industrial raw material and quality.
NOVELTY - Fertilizer comprises 9-18 wt.% soil organic matter, 1-2 wt.% plant growth regulator, 6-12 wt.% microbial agent, and chemical elements comprising nitrogen, phosphorus or potassium (remainder) required for plant growth.    USE - The fertilizer is useful for enhancing soil microorganism activity, increasing soil fertility, degrading pesticide residues, and improving crop quality and resistance, and physical and chemical property of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation method of fertilizer, which involves (a) sterilizing the above-mentioned raw materials, (b) grinding sterilized raw materials, (c) mixing ground raw materials, (d) granulating mixture, (e) drying granules at 270-330 degrees C, (f) secondary drying at 120-180 degrees C, (g) cooling dried granules, (h) sieving cooled granules, and (i) weighing and packing sieved granules.
NOVELTY - The new type utility claims have one plant water-saving cultivation for drinking water construction, the reservoir through conduit connected with water, and the water-drinking groove set with heating device, one side the drinking water groove is set with one medicine adding mouth, to the medicine adding mouth connected with one connecting conduit, the connection conduit and medicine adding device connected, on the drinking trough set with several drinking water hole, and the drinking water hole set with seal cover body, the cover body upper surface set with one elastic connection structure, the elastic connection structure through fixing piece fixed at inner side of drinking water hole, outside the elastic connecting structure set with anti-corrosive layer. And the utility model is new type of seal cover can later by pressure when in animal drinking water sinking water groove, when animal after leaving it automatically reset for drinking water hole sealing, can effective reducing loss of water resource, saving and environment-friendly, and can through medicine adding device adding suitable drug, can be widely applied in animal cultivation.
NOVELTY - The utility model is new type relates to one kind of medical appliance waste collecting device, comprising bracket, bracket one end set with handle, bottom end is provided with the guide wheel bracket, bracket is set with three top surface of separating strip, the top face of the strip dividing into three individual holder compartments, three separating strip of left and right two side are provided with slot, inner slot insert flashboard comprises two block connecting plate, its bottom set with holder, upper frame set with containing box, formed by the three compartments of said technology scheme is convenient to place three block, provided with two containing wherein upper at of plugging plate, can by the different receiving mouth connected with the collecting box is convenient to classify, not easy to cause pollute, by supporting frame and the upper place of containing box is convenient to support the whole multi-collecting box, whole through guide wheel pushing, suitable use, classify.
NOVELTY - Preparing biodiesel involves adding additives into sludge and then drying to obtain dried sludge. Catalytic pyrolysis is performed of dried sludge to obtain gas-liquid mixture and sludge coal. Gasification agent is added into sludge coal and then catalytic pyrolysis is performed to obtain another gas-liquid mixture. The obtained gas-liquid mixtures are mixed and then extracted with dichloromethane to obtain organic phase and water phase. The organic phase is distilled to obtain the biodiesel.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method enables to prepare biodiesel in a simple and cost-effective manner.
NOVELTY - The device has a hollow tube whose upper part is connected with a heavy oil inlet. An internal filter is provided with a continuous spiral channel. A lower part of the hollow tube is equipped with a heavy oil outlet. A lower end of a filtering channel is connected with a rectangular-shaped top face, where two side faces of the filtering channel are formed with a filter screen structure. The filtering channel is fixed with a transverse upper support and a filter inner wall that is connected with a vertical centrifugal filtering separator.    USE - Biomass pyrolysis heavy oil filtering and separating device.    ADVANTAGE - The device increases liquid oil production rate and oil temperature, avoids residual impurities and saves energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass pyrolysis heavy oil filtering and separating method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass pyrolysis heavy oil filtering and separating device.
NOVELTY - Pig manure processing device comprises manure liquid pool (2), excrement pool (3), sediment pool (4), and storage tank (5), where excrement pool is temperature resistant and made up of plastic protective layer. Sewage from discharging tank (1) is collected in liquid pool. Solid manure is collected by sediment pool. Pig manure processing device also comprises anaerobic reaction device and solid-liquid separation unit comprising solid-liquid separation machine, organic processer, and excrement storing pool. Former anaerobic reaction tank comprises gas cabinet, and biogas power generator.    USE - Pig manure processing device.    ADVANTAGE - The pig manure processing device enables to process manure in a cost- effective manner.    DETAILED DESCRIPTION - Pig manure processing device comprises manure liquid pool (2), excrement pool (3), sediment pool (4), and storage tank (5), where excrement pool is temperature resistant and made up of plastic protective layer. Sewage from discharging tank (1) is collected in liquid pool. Solid manure is collected by sediment pool. Pig manure processing device also comprises anaerobic reaction device and solid-liquid separation unit comprising solid-liquid separation machine, organic processer, and excrement storing pool. Former anaerobic reaction tank comprises gas cabinet, biogas power generator, and latter anaerobic reaction tank comprises marsh gas collecting pipe connected to gas cabinet. Pig manure processing device also comprises slurry storage pool connected to anaerobic reaction tank and field irrigation device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of pig manure processing device. Drawing includes non-English language text.    Discharging tank (1)    Manure liquid pool (2)    Excrement pool (3)    Sediment pool (4)    Storage tank (5)
NOVELTY - The utility model is new type relates to one kind organic fertilizer and process system, belonging to fertilizer processing technology field. It comprises fermentation device, smashing device, mixing device, pelletizing device, drying device and package device, the smashing device by transport device respectively and the fermentation device and mixing device connected with, the pelletizing device through transport device respectively and the mixing device and drying device connected with the drying device by the transport device and the package device connected with. The utility model is new type and it is can greatly increase production efficiency, fertilizer quality stable.
NOVELTY - The utility model is new type relates to one kind composite paste fertilizer and production device, said production device comprises fermentation device, stirring dissolution device, a filter device, a filter liquor collecting mixer, mixing device, emulsify device, sterilization device, detection device and on split charging and package device; the stirring dissolution device connected with liquid adding device, on said filter liquor collecting mixer connected with inorganic fertilizer feeder. The paste body composite fertilizer and production device and production process of the whole process is smooth, simple and environment-friendly, the device through precise adding emulsifier can be equal, and dust, clean, the human, poultry and environment safety, non-toxic, simple and rational design.
NOVELTY - The utility model is new type relates to one plant can disassemble tower type excrement, comprising frame, on the frame from up to down provided with multiple cloth layer, each layer of material box bottom of the several strip-shaped plate are transversely arranged and composed of a frame rear side provided with leading frame top part of inclined place feeding rack, the upper frame can provided with the feeding frame above, and for sending material to the hopper of the top box. This can detachable tower type excrement fermentation machine not only can realize cultivation site processing dung dirt, manure using rapid fermentation temperature reach to 70 degree, drying, deodorizing, complete rotten cultivation waste residue, no need to add heat, relieving farm to reach to pollute environment and increase effect of pressure, and square meter small floor space, low energy consumption, content high technology, structure is reasonable and simple, suitable operation, easy dismounting and maintenance, fermentation effect is suitable for farm and different production scale, with wide application prospect.
NOVELTY - The utility model is new type relates to one kind trestle air floatation spiral turn mixing fermentation machine, comprising moving trestle and spiral turn mixing, the mobile trestle is set with fermentation slot above, the spiral turn mixing vehicle comprises engine frame, the transverse walking device, turning device, ventilating, hollow spiral stirring shaft, spiral turn mixing vehicle through the transverse walking device mounted on the beam of the moving trestle, wherein the spiral turn mixing the walking direction of the walking direction and the moving trestle mutually vertical, upper end and lower end of the hollow turning shaft are spiral opening, the ventilating oxygen-increasing device comprises oxygen-increasing fan and ventilating pipe, oxygen-increasing fan and ventilating pipe connected with the turning transmission device comprises the upper end closed, hollow transmission shaft and lower end open mouth, the hollow transmission shaft from ventilating pipe and through the shaft wall is opened with the ventilating pipe and the ventilating hole is connected, the lower part connected with the hollow spiral stirring shaft. The utility model is new type can reduce investment cost, reducing energy consumption, shortens fermentation period, and set with ring heat preservation function.
NOVELTY - Use of molasses for remediation of chromium contaminated soil, is claimed.    USE - Molasses for remediation of chromium contaminated soil.    ADVANTAGE - The molasses has high repair efficiency, strengthens the role of bioremediation, improves soil structure to the subsequent development and utilization of large-scale implementation of the project to effectively prevent secondary pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for remediation of chromium contaminated soil by using molasses.
NOVELTY - Sewage hydrolysis treatment device comprises buffer zone (4), blowing device (6), suction pipe (7), gas supply pipe (8), exhaust port (9), guide walls (11,12), anaerobic gas stripping device (13), anaerobic gas mixing zones (20,30), mud separation zone (40) and gas supply pipe branch (81). The sewage hydrolysis treatment involves conveying sewage into anaerobic gas mixing zone (20), refluxing, diluting, stirring, conveying into mud separation zone (40), performing hydrolysis, acidification and bacteria cyclic degradation and concentrating.    USE - Sewage hydrolysis treatment device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of sewage hydrolysis treatment device.    Buffer zone (4)    Blowing device (6)    Suction pipe (7)    Gas supply pipe (8)    Exhaust port (9)    Guide walls (11,12)    Anaerobic gas stripping device (13)    Anaerobic gas mixing zones (20,30)    Mud separation zone (40)    Gas supply pipe branch (81)
NOVELTY - The recovering method of rabeprazole sulfide involves taking 250 ml rabeprazole sulfide-containing methylene chloride solution and then recycling, washing the solution using methanol and water to obtain a methylene chloride phase, distilling the phase and then recycling methylene chloride, dissolving the phase in an alkali solution, uniformly mixing, adding methanol to the mixture and then adjusting pH value to 9-12 using an acid solution, stirring the mixture and then crystallizing, filtering the mixture and then washing using water, and drying under reduced pressure.    USE - The method is useful for recovering rabeprazole sulfide (claimed).    ADVANTAGE - The method is capable of recovering rabeprazole sulfide with high yield of 55-65% and quality and reduced environmental pollution in an economical manner.    DETAILED DESCRIPTION - The recovering method of rabeprazole sulfide involves taking 250 ml rabeprazole sulfide-containing methylene chloride solution and then recycling, washing the solution using methanol and water to obtain a methylene chloride phase, distilling the phase and then recycling methylene chloride, again distilling the phase and then dissolving in an alkali solution, uniformly mixing, adding methanol to the mixture and then adjusting pH value to 9-12 using an acid solution, stirring the mixture and then crystallizing, filtering the mixture and then washing using water, and drying under reduced pressure.
NOVELTY - Synthesizing capecitabine involves reacting 2',3'-di-O-acetyl-5'-deoxy-5-fluorocytidine with halogen acid ester, acid agent and N-amyl acetate in solvent and in the presence of dimethylaminopyridine to obtain N-amyloxycarbonyl-2',3'-di-O-acetyl-5'-deoxy-5-fluorocytidine. The obtained product is hydrolyzed in the presence of inorganic alkali to obtain the capecitabine.    USE - Method for synthesizing capecitabine (claimed).    ADVANTAGE - The method enables to synthesize capecitabine in cost-effective and environment-friendly manner, and with high yield.
NOVELTY - Methanol diesel fuel additive comprises 2.5-14 pts. wt. methanol, 50-70 pts. wt. light diesel oil, 10-15 pts. wt. dimethyl carbonate, 10-15 pts. wt. ether, alcohol, 2-3 pts. wt. preservative, 2-3 pts. wt. co-solvent, 2-3 pts. wt. antioxidant and 2-3 pts. wt. dispersant. The ether and alcohol has carbon number of 2-5 and 5-9, respectively.    USE - Methanol diesel fuel additive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of methanol diesel fuel comprising mixing methanol and co-solvent, denaturing methanol, stirring and adding balance raw materials.
NOVELTY - Energy-saving vehicle fuel reinforcing agent comprises 15-20 pts. wt. ethanol, 1-1.2 pts. wt. catalyst, 3-5 pts. wt. liquid paraffin, 2-4 pts. wt. fatty acid methyl ester, 2-4 pts. wt. isobutyl acetate, 3-5 pts. wt. sorbitan monostearate, 3-5 pts. wt. polyethylene vinyl acetate, 6-8 pts. wt. methyl ethyl ketone, 2-4 pts. wt. tert-butyl ferrocene, 2-4 pts. wt. smoke suppression agent and 5-7 pts. wt. additive.    USE - Energy-saving vehicle fuel reinforcing agent used for improving combustion, increasing octane number, preventing engine knock, reducing combustion chamber deposits, preventing engine corrosion and reduces harmful emissions.    ADVANTAGE - The reinforcing agent can reduce fuel consumption by 25% and extend engine life.
NOVELTY - Biogasoline additive comprises enzyme, methyl tert-butyl ether and alcohol solvent.    USE - Biogasoline additive.    ADVANTAGE - The additive improves octane number, antiknock property and combustion efficiency and reduces pollutant emissions, particulate matter to 2.5 micrometer and cost of gasoline.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of biogasoline additive comprising taking enzyme, methyl tert-butyl ether and alcohol solvent and stirring at 30-40 degrees C for 10 minutes; and    (2) application of biogasoline additive comprising adding 0.09-0.5 wt.% biogasoline additive to gasoline, stirring and standing for 3-5 hours.
NOVELTY - Production of biodiesel oil comprises taking Pyrularia edulis and fruit core, pulping, and placing in extraction cylinder; mixing with oil extraction solvent and two liquid mixed solvent of methanol solution, shaking at 40-60 degrees C, and carrying out transesterification reaction with sodium hydroxide as catalyst to prepare pure biodiesel; and centrifuging to get fatty acids and triglycerides mixture, rotary evaporating, and recovering pure biodiesel.    USE - Method for producing biodiesel oil (claimed).    ADVANTAGE - The method promotes development of biodiesel oil industry system and uses non-food oilseed diesel woody biomass as raw material.    DETAILED DESCRIPTION - Production of biodiesel oil comprises: (A) taking Pyrularia edulis and fruit core, pulping, and placing in extraction cylinder; (B) mixing with oil extraction solvent and two liquid mixed solvent of methanol solution, shaking at 40-60 degrees C, and carrying out transesterification reaction with sodium hydroxide as catalyst to prepare pure biodiesel, preferably taking two liquid mixed solvent and oil extraction solvent and methanol solution at mass ratio of 10-20:1, extracting at 50-65 degrees C, adding certain amount of methanol solution, where mass ratio of oil extraction solvent and methanol solution is 2-5:30, continuously reacting, continuously extracting at 60-70 degrees C, adding a certain amount of oil extraction solvent, where mass ratio of oil extraction solvent to methanol solution is 5-9:30, continuously reacting, and collecting reaction solution to obtain crude product; and (C) centrifuging to get fatty acids and triglycerides mixture, rotary evaporating, and recovering pure biodiesel.
NOVELTY - Production of biodiesel oil comprises heating rice bran oil, adding phosphoric acid, stirring, adding potassium aluminum sulfate, stirring, cooling, and removing supernatant; cooling upper layer and vacuum removing; adding to esterification reactor, adding methanol, adding potassium hydroxide, stirring, and reacting; standing, adding crude biodiesel to second esterification reactor, adding methanol and potassium hydroxide, stirring, and reacting; standing for stratification, washing upper layer, centrifuging, distilling, cooling, and filtering; and adding sulfuric acid and centrifuging.    USE - Method for producing biodiesel oil (claimed).    ADVANTAGE - The biodiesel oil has high quality. The method has low production cost and high yield.    DETAILED DESCRIPTION - Production of biodiesel oil comprises:    (A) heating rice bran oil to 80 degrees C, adding 0.35 wt.% rice bran oil to 80% phosphoric acid, stirring for 30 minutes, adding 8 wt.% rice bran oil to 5 wt.% potassium aluminum sulfate, mixing, stirring for 15 minutes, cooling to room temperature for 2 hours, and removing supernatant;    (B) cooling upper layer to 8 degrees C and vacuum removing to obtain refined rice bran oil;    (C) adding to esterification reactor, adding methanol, where mass ratio of methanol to rice bran oil is 5-6.5:1, adding 0.7-0.8 wt.% potassium hydroxide as catalyst, stirring, and reacting at 68 degrees C for 1.5 hours;    (D) standing for stratification, adding crude biodiesel to second esterification reactor, adding methanol and potassium hydroxide, where mass ratio of methanol to rice bran oil is 0.6-1.95:1, stirring, and reacting at 70 degrees C for 1.5 hours;    (E) standing for stratification, washing upper layer with aqueous solution at 85 degrees C, centrifuging, distilling off methanol, cooling, and filtering; and    (F) adding 98% sulfuric acid and centrifuging to give acid oil, crude glycerol and solid sodium sulfate.
NOVELTY - Obtaining iridoid glycoside from Tabebuia involves utilizing polar solvents, such as methanol, ethanol, water or acetone.    USE - Method for obtaining iridoid glycoside from Tabebuia used as antiinflammatory, food deterrent and antiophidic agent (claimed).    ADVANTAGE - The method enables to obtain iridoid glycoside from Tabebuia in low cost without affecting environment.
NOVELTY - Processing pharmaceutical beetle larva using straw and mushroom residue comprises selecting agricultural straw and mushroom residue as raw materials, crushing, adding water, stirring, fermenting in fermentation pool and feeding to beetle larva.    USE - Processing pharmaceutical beetle larva (claimed).    ADVANTAGE - The method solves rural straw burning pollution problem and feed source problem, reduces cultivation cost and risk, and increases beetle yield, thus, meeting market demand.
NOVELTY - Method for cultivating Grifola frondosa involves (a) using cottonseed hull, bean cake, mushroom, lime and gypsum, and drying and crushing raw materials, (b) adding crushed mushroom obtained in step (a) to clean water, and soaking for 18-24 hours, adding cottonseed hull to mixture, stacking mixture, fermenting stacked mixture at 60 degrees C for 24 hours, turning fermented product, and adding lime and gypsum, again performing fermentation, planting G.frondosa in fermented product, and (c) performing fruiting management process by spraying mushroom leachate.    USE - The method is useful for Method for cultivating G.frondosa (claimed).    ADVANTAGE - The method enables to cultivate product in an environmentally-friendly manner.    DETAILED DESCRIPTION - Method for cultivating Grifola frondosa involves (a) using 82-90% cottonseed hull, 6-8% bean cake, 3-4% mushroom, 2-3% lime and 1% gypsum, and drying and crushing raw materials, (b) adding crushed mushroom obtained in step (a) to the 20-30 times clean water, and soaking for 18-24 hours, adding cottonseed hull to mixture, stacking mixture to height of 1 m, and width of 2-3 m, fermenting stacked mixture at 60 degrees C for 24 hours, turning fermented product, and adding lime and gypsum hermetically, again performing fermentation for 5-6 days, planting G.frondosa in fermented product, and (c) performing fruiting management process by spraying 0.005-0.01 g/ml mushroom leachate, where the mushroom leachate is prepared by soaking mushroom particles in 20 times or more water, filtering mixture, and concentrating filtrate to 0.05 g/ml.
NOVELTY - Processing amino acid exhaust gas involves defogging exhaust gas by spray cooling gas, where exhaust gas temperature is reduced to less than 35 degrees C. The processed exhaust gas is demisted by electrostatic precipitator. The demisted gas is desulfurized with chemical agent for 20 minutes. The desulfurized gas is treated with micro-organism, spray composite agent for 24 hours. The obtained gas is stirred with chemicals, straw, wheat flour, monoammonium phosphate, urea, potassium chloride and water in twin-screw extruder granulator. The granule is cooled and then stirred with Azotobacter.    USE - Method for processing amino acid exhaust gas used for preparing fertilizer (claimed).    ADVANTAGE - The method enables to process amino acid exhaust gas in simple manner and low cost.
NOVELTY - Preparing composite fertilizer involves mixing 40-50 parts dairy manure, 10-22 parts waste fungus bran, 8-15 parts straw and 10-15 parts soybean meal uniformly with 20-30 parts water. Effective microorganism strain is added in the mixture to carry out fermentation by using a fermentation device at 40-50 degrees C. 30-50 parts Urea and potassium sulfate are mixed in the fermented product and dried in a drying device to reduce water content to 10%. The product is cooled and crushed, and then placed in granulator to obtain granules. Adhesive is mixed in granules, and then cooled and packaged.    USE - Method for preparing composite fertilizer (claimed) used for vegetables and crops.    ADVANTAGE - The method enables to prepare composite fertilizer, which improves soil quality.
NOVELTY - Preparing cultivation material involves pulverizing corn cob (70-76%), tea seed powder (16-20%), mushroom (3-4%), lime (4-5%), light calcium carbonate powder (1%), and then drying pulverized materials. Mushroom particles are soaked in clean water (20-30 times the quantity of granules) for 18-24 hours at low temperature. Soaked product is mixed with corn powder and tea seed powder. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Heaps are covered with grass, and fermented at 60 degrees C for 24 hours. Obtained material is turned once in a day.    USE - Method for preparing cultivation material used for tea mushroom (claimed).    ADVANTAGE - The method is eco-friendly, and ensures accelerated catalytic decomposition, and saves labor.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing corn cob (70-76%), tea seed powder (16-20%), mushroom (3-4%), lime (4-5%), light calcium carbonate powder (1%), and then drying pulverized materials. Mushroom particles are soaked in clean water (20-30 times the quantity of granules) for 18-24 hours at low temperature. Soaked product is mixed with corn powder and tea seed powder. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps. Heaps are covered with grass, and fermented at 60 degrees C for 24 hours. Obtained material is turned once in a day. Calcium carbonate is added to obtained material, and fermentation is continued to obtain fermented product having moisture content of 63-65%. Fermented product is cooled, and packed in polypropylene bags. Bacteria is inoculated in bags, and then kept in dark room at 20-22 degrees C and 60-75% humidity for 23-25 days to obtain the final product.
NOVELTY - Preparing cultivation material involves pulverizing bagasse (68-72%), tea seed powder (20-24%), mushroom (3-4%), lime (4-5%), light calcium carbonate powder (1%), and then drying pulverized materials. Mushroom particles are soaked in clean water (20-30 times the quantity of granules) for 18-24 hours at low temperature. Soaked product is mixed with bagasse and tea seed powder. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Heaps are covered with tarpaulin, and fermented at 60 degrees C for 24 hours. Obtained material is turned once in a day.    USE - Method for preparing cultivation material used for tea mushroom (claimed).    ADVANTAGE - The method is eco-friendly, and ensures accelerated catalytic decomposition, and saves labor.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing bagasse (68-72%), tea seed powder (20-24%), mushroom (3-4%), lime (4-5%), light calcium carbonate powder (1%), and then drying pulverized materials. Mushroom particles are soaked in clean water (20-30 times the quantity of granules) for 18-24 hours at low temperature. Soaked product is mixed with bagasse and tea seed powder. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps with stick. Heaps are covered with tarpaulin, and fermented at 60 degrees C for 24 hours. Obtained material is turned once in a day. Calcium carbonate is added to obtained material, and fermentation is continued to obtain fermented product having moisture content of 63-65%. Fermented product is cooled, and packed in polypropylene bags. Bacteria is inoculated in bags, and then kept in dark room at 20-22 degrees C and 60-75% humidity for 20-22 days to obtain the final product.
NOVELTY - Preparing tea involves weighing broadleaf hardwood (70-76%), tea seed cake (18-22%), mushroom (3-4%), lime (2-3%), and calcium carbonate (1%), and pulverizing the weighed product. Mushroom is fermented in water (20-30 times) for 18-24 hours at room temperature. Fermented product is mixed with broadleaf hardwood, tea seed cake, mushroom, and lime to obtain a heap of width 2-3 meter and height 1-2 meter. Obtained product is heated at 60 degrees C for 24 hours. Calcium carbonate is added to heated product, and obtained product is kept for 5-6 days.    USE - Method for preparing tea (claimed).    ADVANTAGE - The method is eco-friendly , and enables to prepare tea with reduced carbon content.    DETAILED DESCRIPTION - Preparing tea involves weighing broadleaf hardwood (70-76%), tea seed cake (18-22%), mushroom (3-4%), lime (2-3%), and calcium carbonate (1%), and pulverizing the weighed product. Mushroom is fermented in water (20-30 times) for 18-24 hours at room temperature. Fermented product is mixed with broadleaf hardwood, tea seed cake, mushroom, and lime to obtain a heap of width 2-3 meter and height 1-2 meter. Obtained product is heated at 60 degrees C for 24 hours. Calcium carbonate is added to heated product, and obtained product is kept for 5-6 days. Moisture content of obtained product is adjusted to 63-65%. Obtained product is packed in bags and inoculated at 20-22 degrees C, and humidity 60-75% for 24-26 days to obtain final product.
NOVELTY - Preparing cultivation material involves pulverizing corn cob (56-62%), wood (12-14%) bean cake (18-22%), mushroom (3-4%), lime (3-4%), light calcium carbonate (1%), and then drying obtained pulverized materials. Mushroom powder is soaked in clean water (20-30 times the quantity of raw materials) for 18-24 hours at low temperature. Soaked product is mixed with corn cob, wood powder and bean cake. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps with stick. Heaps are covered with tarpaulin.    USE - Method for preparing cultivation material used for needle mushroom (claimed).    ADVANTAGE - The method is eco-friendly, and ensures accelerated catalytic decomposition, and saves labor.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing corn cob (56-62%), wood (12-14%) bean cake (18-22%), mushroom (3-4%), lime (3-4%), light calcium carbonate (1%), and then drying obtained pulverized materials. Mushroom powder is soaked in clean water (20-30 times the quantity of raw materials) for 18-24 hours at low temperature. Soaked product is mixed with corn cob, wood powder and bean cake. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps with stick. Heaps are covered with tarpaulin, and fermented at 60 degrees C for 24 hours. Obtained material is turned once in a day. Obtained material is mixed with lime and light calcium carbonate, and fermentation is continued for 5-6 days to obtain fermented product having moisture content of 63-65%. Fermented product is packed in polypropylene bag, and fungus is inoculated in bag. Obtained material is kept at 18-20 degrees C and 60-75% humidity for 23-25 days to obtain the final product.
NOVELTY - Preparing mushroom cultivation matrix involves weighing cotton seed hull (60-64%), broad leaf wood (12-14%), soybean (16-20%), mushroom (3-4%), lime (2-3%), calcium carbonate (1%). Weighed product is dried and crushed to obtain granules. Mushroom is soaked in water (20-30 times) to carry out fermentation for 18-24 hours. Fermented product is mixed with cotton seed hull, broad leaf wood, soybean, and lime to obtain a pile of height 1-2 meter, and width 2-3 meter. Obtained product is heated at 60 degrees C for 24 hours. Calcium carbonate (3-4 times) is added to heated product.    USE - Method for preparing mushroom cultivation matrix (claimed).    ADVANTAGE - The method is eco-friendly, and enables to prepare mushroom cultivation matrix with low carbon content.    DETAILED DESCRIPTION - Preparing mushroom cultivation matrix involves weighing cotton seed hull (60-64%), broad leaf wood (12-14%), soybean (16-20%), mushroom (3-4%), lime (2-3%), calcium carbonate (1%). Weighed product is dried and crushed to obtain granules. Mushroom is soaked in water (20-30 times) to carry out fermentation for 18-24 hours. Fermented product is mixed with cotton seed hull, broad leaf wood, soybean, and lime to obtain a pile of height 1-2 meter, and width 2-3 meter. Obtained product is heated at 60 degrees C for 24 hours. Calcium carbonate (3-4 times) is added to heated product, and obtained product is kept for 5-6 days. Moisture content of obtained product is adjusted to 60-75%. Obtained product is packed in bags and inoculated at 20 degrees C, and relative humidity 60-75% for 22-24 days to obtain final product.
NOVELTY - Preparing cultivation material involves pulverizing bagasse (54-60%), wood (12-14%), bean cake (18-22%), mushroom (3-4%), lime (3-4%), light calcium carbonate (1%), and then drying obtained pulverized materials. Mushroom powder is soaked in clean water (20-30 times the quantity of raw materials) for 18-24 hours at low temperature. Soaked product is mixed with corn cob, wood powder and bean cake. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps with stick. Heaps are covered with tarpaulin.    USE - Method for preparing cultivation material used for needle mushroom (claimed).    ADVANTAGE - The method is eco-friendly, and ensures accelerated catalytic decomposition, and saves labor.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing bagasse (54-60%), wood (12-14%), bean cake (18-22%), mushroom (3-4%), lime (3-4%), light calcium carbonate (1%), and then drying obtained pulverized materials. Mushroom powder is soaked in clean water (20-30 times the quantity of raw materials) for 18-24 hours at low temperature. Soaked product is mixed with corn cob, wood powder and bean cake. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps with stick. Heaps are covered with tarpaulin, and fermented at 60 degrees C for 24 hours. Obtained material is turned once in a day. Obtained material is mixed with lime and light calcium carbonate, and fermentation is continued for 5-6 days to obtain fermented product having moisture content of 63-65%. Fermented product is packed in polypropylene bag, and fungus is inoculated in bag. Obtained material is kept at 18-20 degrees C and 60-75% humidity for 20-22 days to obtain the final product.
NOVELTY - Preparing cultivation material involves pulverizing cotton seed hull (50-60%), corn cob (26-32%), bean cake (8-10%), mushroom (3-4%), lime (2.5%) and gypsum (1%), and the drying pulverized materials. Mushroom powder is are soaked in clean water (20-30 times the quantity of granules) for 18-24 hours at low temperature. Soaked product is mixed with cotton seed hull, corn cob and bean cake powder. Obtained mixture (300-500kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heap with stick. Heap is covered with tarpaulin, and then fermented.    USE - Method for preparing cultivation material used for Grifola frondosa (claimed).    ADVANTAGE - The method is eco-friendly, and ensures accelerated catalytic decomposition, and saves labor.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing cotton seed hull (50-60%), corn cob (26-32%), bean cake (8-10%), mushroom (3-4%), lime (2.5%) and gypsum (1%), and the drying pulverized materials. Mushroom powder is are soaked in clean water (20-30 times the quantity of granules) for 18-24 hours at low temperature. Soaked product is mixed with cotton seed hull, corn cob and bean cake powder. Obtained mixture (300-500kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heap with stick. Heap is covered with tarpaulin, and then fermented at 60 degrees C for 24 hours. Obtained material is turned 3-4 times, and then gypsum is added to it. Fermentation is continued for 5-6 days to obtain fermented material having water content of 63-65%. Obtained material is put in polypropylene bag. Hairy fungus is inoculated in bag through hole, and then kept at 18-20 degrees C at 60-75% humidity for 20-22 days to obtain the final product.
NOVELTY - Preparing cultivation material involves pulverizing corn cob (54-60%), wood (22-28%), bean cake (12-14%), mushroom (3-4%), monopotassium phosphate (0.1%), calcium superphosphate (0.4%), and gypsum (1%), and then drying obtained pulverized materials. Mushroom powder is soaked in clean water (20-30 times the quantity of raw materials) for 18-24 hours at low temperature. Soaked product is mixed with corn cob and wood powder. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps with stick.    USE - Method for preparing cultivation material used for Hericium erinaceum (claimed).    ADVANTAGE - The method is eco-friendly, and ensures accelerated catalytic decomposition, and saves labor.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing corn cob (54-60%), wood (22-28%), bean cake (12-14%), mushroom (3-4%), monopotassium phosphate (0.1%), calcium superphosphate (0.4%), and gypsum (1%), and then drying obtained pulverized materials. Mushroom powder is soaked in clean water (20-30 times the quantity of raw materials) for 18-24 hours at low temperature. Soaked product is mixed with corn cob and wood powder. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps with stick. Heaps are covered with tarpaulin, and fermented at 60 degrees C for 24 hours. Obtained material is turned once in a day. Obtained material is mixed with gypsum, calcium superphosphate, monopotassium phosphate, and fermentation is continued for 5-6 days to obtain fermented product having moisture content of 63-65%. Fermented product is packed in polypropylene bags, and fungus is inoculated in bag through hole. Obtained material is kept at 18-20 degrees C and 60-75% humidity for 26-28 days to obtain the final product.
NOVELTY - Preparing cultivation matrix involves weighing bagasse (46-52%), broad leaf wood (28-32%), bean cake (14-18%), mushroom (3-4%), monopotassium phosphate (0.1%), calcium superphosphate (0.4%), and gypsum (1%). Weighed product is crushed to obtain powder. Mushroom is soaked in water (20-30 times) for 18-24 hours at low temperature to carry out fermentation. Fermented product is mixed with bagasse, broad leaf wood, and bean cake to obtain a pile of height 1-2 meter and width 2-3 meter. Obtained material is kept at 60 degrees C and adding calcium superphosphate and monopotassium phosphate to it.    USE - Preparing cultivation material used for Hericium (claimed).    ADVANTAGE - The method is eco-friendly, and enables to prepare cultivation matrix with reduced carbon content.    DETAILED DESCRIPTION - Preparing cultivation matrix involves weighing bagasse (46-52%), broad leaf wood (28-32%), bean cake (14-18%), mushroom (3-4%), monopotassium phosphate (0.1%), calcium superphosphate (0.4%), and gypsum (1%). Weighed product is crushed to obtain powder. Mushroom is soaked in water (20-30 times) for 18-24 hours at low temperature to carry out fermentation. Fermented product is mixed with bagasse, broad leaf wood, and bean cake to obtain a pile of height 1-2 meter and width 2-3 meter. Obtained material is kept at 60 degrees C for 24 hours. Calcium superphosphate and monopotassium phosphate is mixed with obtained material and obtained mixture is kept for 5-6 days. Moisture content of obtained product is adjusted to 63-65%. Obtained product is packed in polypropylene plastic and inoculated at 18-20 degrees C, and relative humidity 60-75% for 24-26 days to obtain final product.
NOVELTY - Preparing cultivation material involves crushing 58-64% cotton seed hull, 18-22% wood powder, 12-16% bean cake, 3-4% mushroom, 0.1% monopotassium phosphate, 0.4% calcium superphosphate and 1% gypsum into granules. Granules are dried, and then: mushroom is soaked with clean water (20-30 times) for 18-24 hours. Cotton seed hull, wood powder, bean cake and gypsum are mixed in trapezoidal container to carry out natural fermentation at 60 degrees C for 24 hours. Calcium superphosphate and monopotassium phosphate are added in the fermented product.    USE - Method for preparing cultivation material for Hericium erinaceus (claimed).    ADVANTAGE - The method is eco-friendly, and enables to prepare cultivation material for Hericium erinaceus in low-carbon environment.    DETAILED DESCRIPTION - Preparing cultivation material involves crushing 58-64% cotton seed hull, 18-22% wood powder, 12-16% bean cake, 3-4% mushroom, 0.1% monopotassium phosphate, 0.4% calcium superphosphate and 1% gypsum into granules. Granules are dried, and then: mushroom is soaked with clean water (20-30 times) for 18-24 hours. Cotton seed hull, wood powder, bean cake and gypsum are mixed in trapezoidal container to carry out natural fermentation at 60 degrees C for 24 hours. Calcium superphosphate and monopotassium phosphate are added in the fermented product. Fermented product is packaged in polypropylene plastic bag and Hericium erinaceus is kept in bag. Hericium erinaceus is cultivated in dark room at 18-20 degrees C at humidity of 60-75%, where Hericium erinaceus is grown in 24-26 days.
NOVELTY - Preparing cultivation material involves pulverizing cotton seed hull (54-60%), bagasse (18-22%), bean cake (12-14%), mushroom (3-4%), (0.1%), lime (2-3%), and gypsum (1%), and then drying obtained pulverized materials. Mushroom powder is soaked in clean water (20-30 times the quantity of raw materials) for 18-24 hours at low temperature. Soaked product is mixed with cotton seed hull, bagasse and bean cake. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps with stick. Heaps are covered with tarpaulin.    USE - Method for preparing cultivation material used for Pholiota nameko (claimed).    ADVANTAGE - The method is eco-friendly, and ensures accelerated catalytic decomposition, and saves labor.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing cotton seed hull (54-60%), bagasse (18-22%), bean cake (12-14%), mushroom (3-4%), (0.1%), lime (2-3%), and gypsum (1%), and then drying obtained pulverized materials. Mushroom powder is soaked in clean water (20-30 times the quantity of raw materials) for 18-24 hours at low temperature. Soaked product is mixed with cotton seed hull, bagasse and bean cake. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps with stick. Heaps are covered with tarpaulin, and fermented at 60 degrees C for 24 hours. Obtained material is turned once in a day. Obtained material is mixed with lime and gypsum, and fermentation is continued for 5-6 days to obtain fermented product having moisture content of 63-65%. Fermented product is packed in polypropylene bags, and hairy fungus is inoculated in bag through hole. Obtained material is kept at 18-20 degrees C and 60-75% humidity for 22-24 days to obtain the final product.
NOVELTY - Preparing cultivation matrix involves weighing bagasse (34-40%), broad leaf wood (38-42%), bean cake (14-16%), mushroom (3-4%), lime (3-4%), and gypsum (1%). Weighed product is dried and crushed to obtain granules. Mushroom is soaked in water (20-30 times) for 18-24 hours at low temperature to carry out fermentation. Fermented product is mixed with bagasse, broad leaf wood, and bean cake to obtain a pile of height 1-2 meter and width 2-3 meter. Obtained material is kept at 60 degrees C for 24 hours. Gypsum is added to obtained product (3-4 times) for 5-6 days.    USE - Preparing cultivation material used for Pleurotus nebrodensis (claimed).    ADVANTAGE - The method is eco-friendly, and enables to prepare cultivation matrix with reduced carbon content.    DETAILED DESCRIPTION - Preparing cultivation matrix involves weighing bagasse (34-40%), broad leaf wood (38-42%), bean cake (14-16%), mushroom (3-4%), lime (3-4%), and gypsum (1%). Weighed product is dried and crushed to obtain granules. Mushroom is soaked in water (20-30 times) for 18-24 hours at low temperature to carry out fermentation. Fermented product is mixed with bagasse, broad leaf wood, and bean cake to obtain a pile of height 1-2 meter and width 2-3 meter. Obtained material is kept at 60 degrees C for 24 hours. Gypsum is added to obtained product (3-4 times) for 5-6 days. Moisture content of obtained product is adjusted to 63-65%. Obtained product is packed in polypropylene plastic and inoculated at 18-20 degrees C, and relative humidity 60-75% for 26-28 days to obtain final product.
NOVELTY - Preparing biological fertilizer involves inoculating enteromorpha polysaccharide in Bacillus medium at 30-35 degrees C, and pH value 6.8-7.4 for 18-24 hours to obtain culture broth of concentration 3-10%. Culture broth is fermented at 24-32 degrees C for 18-24 hours. Fermented product is centrifuged to prepare extracellular fermentation broth. Obtained product is mixed with 95% ethanol and calcium chloride in a ratio of 1:1.5:2.5. Obtained mixture is dried under vacuum to obtain a powder. Obtained powder is dissolved in water at 60 degrees C at 200 Watt. Obtained product is mixed with cellulase.    USE - Method for preparing biological fertilizer used for tobacco (all claimed).    ADVANTAGE - The fertilizer is eco-friendly, and shows good market application.    DETAILED DESCRIPTION - Preparing biological fertilizer involves inoculating enteromorpha polysaccharide in Bacillus medium at 30-35 degrees C, and pH value 6.8-7.4 for 18-24 hours to obtain culture broth of concentration 3-10%. Culture broth is fermented at 24-32 degrees C for 18-24 hours. Fermented product is centrifuged to prepare extracellular fermentation broth. Obtained product is mixed with 95% ethanol and calcium chloride in a ratio of 1:1.5:2.5. Obtained mixture is dried under vacuum to obtain a powder. Obtained powder is dissolved in water at 60 degrees C at 200 Watt. Obtained product is mixed with cellulase (20 plaque-forming unit/g), and protease (30 plaque-forming unit/g), and obtained product is centrifuged. Centrifuged product is lyophillized to obtain powder. Obtained powder is dissolved in water to obtain a concentration of 0.05-2%, and then heated to obtain final product.
NOVELTY - Preparing natural taurine comprises collecting raw materials comprising waste generated in aquatic product processing, including cooking soup of edible part and waste internal organs of aquatic products, adding 2-5 times weight by volume of water, cooking at 80-120 degrees C for 60-120 minutes, filtering, primary concentrating, adding ethanol to obtain precipitate and supernatant, extracting the supernatant, secondary concentrating, placing concentrate in -15 to -30 degrees C environment, adding little taurine seed crystal, stirring, precipitating taurine crystals, filtering, dissolving, cooling and drying.    USE - The method is useful for preparing natural taurine (claimed).    ADVANTAGE - The method is simple, environmentally friendly and economical; does not require large scale equipments and suitable for industrial production.    DETAILED DESCRIPTION - Preparing natural taurine comprises (i) collecting raw materials comprising waste generated in aquatic product processing, including cooking soup of edible part and waste internal organs of aquatic products, (ii) adding 2-5 times weight by volume of water, cooking at 80-120 degrees C for 60-120 minutes and filtering to obtain extract, (iii) primary concentrating to the original volume of 1/5-10, (iv) adding ethanol to a final concentration of 50 to 80% by volume to obtain precipitate and supernatant, extracting the supernatant, (v) secondary concentrating the supernatant under reduced pressure to remove ethanol, where in the solid content is 30-60 wt.%. (vi) placing concentrate in -15 to -30 degrees C environment, adding little taurine seed crystal, stirring slowly for 12 hours or more, precipitating taurine crystals, filtering to obtain crude taurine, and (vi) dissolving crude taurine in 80 degrees C hot water, cooling to room temperature to obtain wet taurine and drying.
NOVELTY - Preparing organic fertilizer involves fermenting raw material in anaerobic conditions. Fermented product is filtered in aerobic conditions to obtain final product and to remove residue.    USE - Method for preparing organic fertilizer (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for a device used for anaerobic fermentation, which comprises tank provided with two channel wall, gasification unit, settling zone, and reflux tube.
NOVELTY - Cement grinding agent comprises waste acid, ammonium salt, triethanolamine, and ethylene oxide at mass ratio 0.5-3.0:1:5-0.5:1.0-5. The waste acid comprises 1-35 wt.% hydrochloric acid or 1-45 wt.% sulfuric acid. The concentration of triethanolamine is 50 wt.%.    USE - Cement grinding agent used for preparing cement, concrete and pharmaceutical intermediates.    ADVANTAGE - The grinding agent uses industrial waste and by product salt which reduces cost of production, improves economic efficiency of enterprises, and prevents environmental pollution. It has high purity, excellent performance and good using effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cement grinding agent comprising mixing waste acid and ammonium salt in reactor, stirring uniformly, purging with nitrogen to replace air inside the reactor; adding triethanolamine slowly for 1-2 hours, adjusting temperature to 40-80 degrees C; adding ethylene oxide continuously for 1-4 hours, adjusting temperature to 40-100 degrees C and pressure to 0.1-0.6 MPa, reacting at constant pressure for 0.5 hour; and vacuum dehydrating or crystallizing at room temperature to obtain dry powdery solid product.
NOVELTY - Preparing hydrogen by decomposing water through light anode photovoltaic cells coupled dual illumination optical drive. The photoelectrocatalysis technology and photovoltaic cell technology are coupled to form a two-electrode system. The water oxidized catalyst semiconductor material and modified silicon battery pole are provided as light anode to achieve sunlight driven water splitting without utlilizing any extra energy.    USE - Method for preparing hydrogen (claimed).
NOVELTY - Monopolar electrolytic groove comprises outer cylinder (1), inner cylinder (2), oxygen outlet pipe (5), hydrogen gas outlet tube (6), alkali liquid inlet pipe (8), ceramic sealing component, ceramic insulation module and control unit. The one end of inner cylinder is open and its other end is provided with a flange cover (4). The flange cover is provided on the hydrogen gas outlet and oxygen outlet. The inner cylinder near the flange cover cylinder is attached to an insulating sleeve section. The one end of the outer cylinder is open and the other end is closed end.    USE - Monopolar electrolytic groove used for treating heavy water containing tritium.    ADVANTAGE - The monopolar electrolytic groove is durable, radiation resistant, alkali resistant, corrosion resistant, and has simple structure and suitable assembly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a monopolar electrolytic groove.    Outer cylinder (1)    Inner cylinder (2)    Flange cover (4)    Oxygen outlet pipe (5)    Hydrogen gas outlet tube (6)    Alkali liquid inlet pipe (8)
NOVELTY - Regenerating chemical oxygen iodine laser chemical raw material involves separating an aqueous solution of potassium chloride or sodium chloride from chemical oxygen iodine laser product through alkali electrolysis. The potassium hydroxide or sodium hydroxide solution is separated from chemical oxygen iodine laser product. The sodium hydroxide or potassium hydroxide is entered into the fuel cell reactor to separate hydrogen. The alkaline hydrogen peroxide solution is oxidized. The alkaline hydrogen peroxide solution is collected from alkaline hydrogen peroxide solution tank.    USE - Method for regenerating chemical oxygen iodine laser chemical raw material (claimed).
NOVELTY - Microbial consortium for degradation of lignocelluloses comprises a bacterial strain selected from Bacillus subtilis deposited under MTCC accession number MTCC5843, and Streptomyces sp. deposited under MTCC accession number MTCC5844, and a fungi selected from Aspergillus brasiliensis deposited under MTCC accession number MTCC5845.    USE - The microbial consortium is useful for degradation of lignocelluloses; and for preparing compost from waste containing lignocelluloses (all claimed).    ADVANTAGE - The microbial consortium is capable of effectively degrading lignocelluloses. Additionally, the microbial consortium comprising microorganisms for bio-degradation of lignocelluloses can be revived easily. The microorganisms are compatible with each other. The use of consortium helps in eliminating/reducing toxicity of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method of preparing compost from waste containing lignocelluloses by any conventional method, comprising adding the microbial consortium for degradation of lignocelluloses contained in the waste.
NOVELTY - Fertilizer comprises wood (28-48 pts. wt.), rapeseed cake (18-30 pts. wt.), crab shell powder (10-20 pts. wt.), Hyponex (RTM: Potting soil) (10-20 pts. wt.), and honeysuckle (6-10 pts. wt.).    USE - Fertilizer used for Anoectochilus roxburghii (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) mixing raw materials;    (B) adding activated effective microorganisms to obtained mixture in weight ratio of 1:30-50 to obtain solution having moisture content of 40-50%;    (C) fermenting obtained mixture at 30-35 degrees C for 20-30 days;    (D) adding 2-5% bentonite to fermented material; and    (E) granulating obtained mixture by extrusion granulator to obtain the final product.
NOVELTY - Carbon steel reinforced filter device comprises a cylindrical body (23) that is placed on the top of a hemispherical tank. Bottom portion of the carbon steel reinforced filter device is connected to a discharge pipe (21) that is guided by a valve (2). The valve is opened during the operation. A gas storage cabinet (6) placed in contact with the circular cover plate, is provided with a biogas outlet (8). The circular cover plate is utilized for supporting the gas membrane from getting collapsed due to the absence of gas. A side cover is linked to methane gas flow passages.    USE - Carbon steel reinforced filter device.    ADVANTAGE - The designed carbon steel reinforced filter device is highly efficient to yield pure biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional schematic view of carbon steel reinforced filter device.    Valve (2)    Gas storage cabinet (6)    Biogas outlet (8)    Discharge pipe (21)    Cylindrical body (23)
NOVELTY - Biogas fermentation system system comprises raw material feedstock cylinder (12), first stage fermentation system (10), second grade feedstock pipe (122), second stage fermentation system, and marsh gas fermentation area (13). The fermentation area is provided with blocking plate. The second stage fermentation system is provided with discharging pipe (124), drain pipe and cloth bacteria device. The marsh gas is generated in second stage fermentation system and accumulated at second level for discharging pipe. The marsh gas is stored in drain pipe.    USE - Fermentation system.    ADVANTAGE - The fermentation system is highly efficient.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fermentation system.    First stage fermentation system (10)    Material feedstock cylinder (12)    Fermentation area (13)    Second grade feedstock pipe (122)    Discharging pipe (124)
NOVELTY - Substituted quinolinyl epoxy ketone compounds (l) are new.    USE - (l) are useful: for treating bacterial and fungal infection (claimed); and as intermediates for the production of pharmaceutical products.    ADVANTAGE - (I) can be prepared at higher chemical purity and greater yield using mild conditions in shorter reaction time and simple and eco friendly manner.    DETAILED DESCRIPTION - Substituted quinolinyl epoxy ketone compounds of formula (l) are new.    R, R1, R2 = hydrogen, alkyl, alkoxy or halo.    An INDEPENDENT CLAIM is also included for the preparation of (I).
NOVELTY - Method for cultivating black sesame, involves (a) choosing land which does not grow sesame for more than 3 years and have loose soil texture, (b) plowing and fertilizing the land, (c) performing seed treatment, (d) sowing the treated seeds in early June, (e) obtaining seedlings having 3-4 pairs of true leaves and planting the seedlings, (f) fertilizing the seedling using urea and superphosphate before flowering stage, and potassium dihydrogen phosphate after flowering stage and spraying water, (g) controlling pest, and (h) cutting stem and harvesting black sesame.    USE - The method is useful for cultivating black sesame (claimed).    ADVANTAGE - The method is environmentally-friendly, and improves permeability of nutrients in soil.    DETAILED DESCRIPTION - Method for cultivating black sesame, involves (a) choosing land which does not grow sesame for more than 3 years and have loose soil texture, (b) plowing the land to a width of 180-200 cm and height of 25-30 cm and applying 2000-2500 kg/acre organic fertilizer and 15-20 kg/acre compound fertilizer, (c) performing seed treatment by exposing the seeds to sun for 1-2 days, mixing 8 g 50% carbendazim wettable powder and water, and mixing 0.5 kg obtained mixture and 0.5 kg seed, (d) sowing the treated seeds in early June at a spacing of 30-35 cm and depth of 2-3 cm in trench and adding soil to the trench, where the seeds are sown in an amount of 0.4-0.5 kg/acre seeds, (e) obtaining seedlings having 3-4 pairs of true leaves and planting the seedlings at a spacing of 12-15 cm, (f) fertilizing the seedling using 8-10 kg/acre urea and 8-10 kg/acre superphosphate before flowering stage, and 0.2 kg/acre potassium dihydrogen phosphate after flowering stage and spraying 60 kg water by foliar spray at an interval of 5-7 days for 2 times, (g) controlling pest by spraying 800-1000 times 50% carbendazim wettable powder (WP) for every 10-12 days, and (h) cutting stem and harvesting black sesame.
NOVELTY - Preparing biological fertilizer involves culturing Bacillus subtilis (CICC 10339) to obtain high density bacterial suspension. The density of bacterial suspension is 109-1010 colony forming units/ml. The Nitraria branches are cut into small pieces. The small pieces of branches i.e. compost is sprayed with high density bacterial suspension i.e. biological fertilizer for fermentation.    USE - Method for preparing biological fertilizer for preventing and treating stem rot disease, promoting growth of Nitraria plant, and inhibiting or killing pathogenic fungi (all claimed).    ADVANTAGE - The method is simple, cost-effective, energy conservative, easy to operate and suitable for large scale industrial production.
NOVELTY - Microbial inoculum comprises mixed culture of bacteria and carrier. The mixed culture of bacteria (10-20%) contains Bacillus amyloliquefaciens, Bacillus cereus, Cellulomonas, Alcaligenes, Bacillus megaterium, Bacillus thuringiensis, Bacillus subtilis in ratio of 2-4:1:1:1:1:1:1.    USE - Microbial inoculum for degrading domestic garbage wastes (claimed).    ADVANTAGE - The microbial inoculum is cost-effective and easy to use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing microbial inoculum, which involves:    (A) culturing Bacillus amyloliquefaciens, Bacillus cereus, Cellulomonas, Alcaligenes, Bacillus thuringiensis and Bacillus subtilis, respectively in Luria Bertani medium and incubating at 30 degrees C for 24-36 hours;    (B) mixing obtained cultures of Bacillus amyloliquefaciens, Bacillus cereus, Cellulomonas, Alcaligenes, Bacillus thuringiensis and Bacillus subtilis in ratio of 2-4:1:1:1:1:1:1 to obtain mixed culture of bacteria;    (C) centrifugating the mixed culture of bacteria to collect cells:    (D) freeze-drying the obtained cells under vacuum and then sterilizing; and    (E) mixing the obtained sterilized cells with carrier in ratio of 1-2:9-8 to obtain microbial inoculum.
NOVELTY - An organophosphorus pesticide in textile extracting method involves mixing acetone and water in volume ratio of 1:9-19 as extracting solvent, extracting textile with solvent, collecting extracting liquid, soaking carbon nanotube in extracting liquid, eluting carbon nanotube with organic solvent ultrasonically, collecting eluate, and filtering the eluate with filter film to obtain filtrate.    USE - Method for extracting organophosphorus pesticide in textile, where the organophosphorus pesticide is methamidophos, dichlorvos, mevinphos, omethoate, demeton-S-methyl, ethoprophos, dicrotophos, monocrotophos, disulfoton, dimethoate, propetamphos, diazinon, methylparathion, fenitrothion, malathion, fenthion, parathion, chlorfenvinphos, quinalphos, tetrachlorvinphos, profenofos, triazophos, edifenphos, azinphos-methyl, azinphos-ethyl or coumaphos (claimed).    ADVANTAGE - The method enables extracting organophosphorus pesticide in textile with high recovery rate, high sensitivity, better reproducibility, little time consumption and high efficiency, overcoming problems due to usage of extensive organic solvents, avoiding elution influence of carbon nanotube, satisfying requirements, and improving perfect evaluation system of ecological textile to provide scientific basis.
NOVELTY - A rubiasin D (I), is new.    USE - New rubiasin D is useful for preparing agent for providing nematicide effect (all claimed).    ADVANTAGE - The rubiasin D is environmentally-friendly and cost-effective.    DETAILED DESCRIPTION - A rubiasin D of formula (I), is new. INDEPENDENT CLAIMS are included for the following:    (1) nematicide comprising rubiasin D (I), 2-methoxy-1,4-naphthoquinone and/or 1,4-naphthoquinone as an active ingredient; and    (2) preparation of rubiasin D (I), 2-methoxy-1,4-naphthoquinone and 1,4-naphthoquinone, which involves drying madder root and rhizome, splintering, extracting with methanol, concentrating the extract under reduced pressure, and subjecting obtained product to silica gel column chromatography. The rubiasin D is prepared using petroleum ether/acetone in a ratio of 30:1, 10:1, 5:1, or 1:1 as eluent in silica gel column chromatography. The 2-methoxy-1,4-naphthoquinone is prepared using petroleum ether/chloroform in a ratio of 10:1, 5:1, or 1:1 as eluent in silica gel column chromatography. The 1,4-naphthoquinone is prepared using petroleum ether/chloroform in a ratio of 30:1, 10:1, 5:1, or 1:1 as eluent in silica gel column chromatography.
NOVELTY - Method for preparing base composition of biological preparation for plant growth, involves obtaining biomass of Mortierella alpina strain F-1134 by removing culture liquid, removing complex of fatty acids with predominance of arachidonic acid from mycelium, and culturing fungus on surface of thin layer of liquid nutrient medium, where the inoculation is performed before bottling and the culturing process is performed to achieve maximum biomass destruction of mycelium by performing cryodestruction and alkaline hydrolysis.    USE - The method is useful for preparing base composition of biological preparation for plant growth (claimed).    DETAILED DESCRIPTION - Method for preparing base composition of biological preparation for plant growth, involves obtaining biomass of Mortierella alpina strain F-1134 by removing culture liquid, removing complex of fatty acids with a predominance of arachidonic acid from mycelium using alcohol solution with additional components, and culturing fungus on surface of thin layer of liquid nutrient medium, where the inoculation is performed before bottling, and the culturing process is performed to achieve maximum biomass destruction of mycelium by performing cryodestruction and alkaline hydrolysis to obtain biodegradable detergent as end product.
NOVELTY - The device has first and second first-stage anaerobic fermentation tanks (1-1,2-1). First first-stage anaerobic fermentation tank is connected with one end of first heat exchanger (1-2) whose other end is connected with first first-stage anaerobic fermentation tank and second-stage anaerobic fermentation tank. Second first-stage anaerobic fermentation tank is connected with one end of second heat exchanger (2-2) whose other end is connected with second first-stage anaerobic fermentation tank and second stage fermentation tank sets with marsh gas transport interface.    USE - Device for efficiently preparing biogas.    ADVANTAGE - The gas production rate is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the method for efficiently preparing biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for efficiently preparing biogas. (Drawing includes non-English language text)    First-stage anaerobic fermentation tanks (1-1,2-1)    Heat exchangers (1-2,2-2)    Material crushers (1-4,2-4)    Hot water boiler (4)    Stirrer (6)
NOVELTY - A high pressure oxyhydrogen machine comprises: at least one set of electrolytic tanks and a storage tank for storing electrolyte. The electrolytic tanks are laterally connected as one unit. The storage tank is disposed above each of the electrolytic tanks and may deliver electrolyte via pipelines into each electrolytic tank. The electrolytic tank is disposed with a cathode plate, an anode plate and an insulated net layer between each cathode plate and anode plate. The cathode plate and anode plate are respectively distributed with multiple pores. The mesh of the insulated net layer allows passage of electrolyte, hydrogen and oxygen. The insulated net layer, the cathode plate and the anode plate are tightly bonded to reduce impedance and increase the hydrogen and oxygen production efficiency. The two side walls of the electrolytic tank are provided with at least two inclined ribs which cut the internal space of the into a Z shape so as to guide the electrolyte, hydrogen, and oxygen in the recesses to flow upwardly in a Z-shaped path.
NOVELTY - The furnace has a furnace body (1) whose side is provided with a feeding port (2). A lower part of the furnace body is fixed with a conveying belt (3) that is formed with a combustion cavity. The combustion cavity is matched with a heat storage cavity through a way hole. A combustion gun (7) is installed in the heat storage cavity that is connected with a vertical tube (8). The vertical tube is connected with an inclined pipe (9) that is fixed with a lower part of a burner (10). A hopper (11) is connected with a feeding auger (12) that is connected with the feeding port.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace utilizes heat energy so as to reduce loss. The furnace has high heating efficiency. The furnace cleans discharge hot air so as to ensure better environmental protection.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a biomass gasification furnace.    Furnace body (1)    Feeding port (2)    Conveying belt (3)    Combustion gun (7)    Vertical tube (8)    Inclined pipe (9)    Burner (10)    Hopper (11)    Feeding auger (12)
NOVELTY - Box/container/bag made from bagasse, is claimed. The box/container/bag is dipped in paraffin and filled with wood pieces, biomass or renewable resources.    USE - Used as box/container/bag.    ADVANTAGE - The box is lightweight, and are combustible.
NOVELTY - Preparing a catalyst, comprises: mixing a suspension of a solid support and a solution of a transition metal precursor to form a surface modified solid support; drying the surface modified solid support; and adding a solution of a noble metal salt to the dry surface modified solid support to form the catalyst.    USE - The method is useful for preparing a catalyst, which is useful in hydrodeoxygenation reactions of oxygen containing chemicals, preferably biomass-derived pyrolysis oils (claimed).    ADVANTAGE - The method provides the catalyst that exhibits improved stability, high activity for hydrodeoxygenation of pyrolysis oil under low severity conditions and improves economic feasibility of bio-oil upgrading technology significantly, with high selectivity towards aromatic products, while decreasing hydrogen consumption and operation cost, and providing high value products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the catalyst obtained by the method.
NOVELTY - The system (100) has a hydrogen-producing unit that generates hydrogen using the heat from a fuel cell (102), or water steam and the electric power from the electric power generating apparatus. A hydrogen storage apparatus (112) stores the generated hydrogen. The fuel cell is electric-power-generated using the stored hydrogen as a fuel. A water steam electrolyzer (110) which electrolyzes the water steam from the steam generation unit using the electric power from the electric power generating apparatus, and generates the hydrogen is provided.    USE - Distributed power supply system.    ADVANTAGE - Since the fuel cell produces electric power and load is supplied as stable electric power after converting into hydrogen and being stored, the system is highly efficient and provides the distributed power supply system for enabling the stable electric power generation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an operation method of distributed power supply system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram which shows the distributed power supply system. (Drawing includes non-English language text)    Distributed power supply system (100)    Fuel cell (102)    Solar power generation device (104)    Water steam electrolyzer (110)    Hydrogen storage apparatus (112)
NOVELTY - The system (10) has a control unit that controls the water level in the gas liquid separation apparatus normally in the range of a normal time upper limit water level to a normal time minimum water level at the time of electrolysis. First drain piping (32) is provided between upper limit water levels at the time of the depressurization. Second drain piping (34) is provided below minimum water level at the time of the depressurization. A pressure-loss element (36) that is provided to reduce the pressure of high-pressure water is arranged at two drain pipings.    USE - High-pressure water electrolysis system.    ADVANTAGE - Since the first drain piping is sunk in the stagnant water in a gas liquid separation apparatus and can always be normally drained during electrolysis, the wastewater treatment and depressurization process are performed effectively and economically.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a control method of the high-pressure water electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the high-pressure water electrolysis system. (Drawing includes non-English language text)    High-pressure water electrolysis system (10)    Tank (30)    First drain piping (32)    Second drain piping (34)    Pressure loss element (36)
NOVELTY - Producing exothermic gas and electricity by utilizing biomass, comprises drying biomass; and performing dry distillation of the dried biomass at 400-1200 degrees C for 40-240 minutes.    USE - The method is useful for producing exothermic gas and electricity by utilizing biomass (claimed).    ADVANTAGE - The method can generate large amount of exothermic gas which can be used as heat source by optimizing biomass dry distillation temperature and linearly increases the total amount of exothermic gas of biomass with increase in temperature to exhibit high calorific value compared to the coke oven gas; easily recovers char and heat generating syngas using the biomass which is introduced in the batch-type process; and generates electricity by combusting the biomass (cow manure) in the combustion furnace containing oxygen using a heat exchanger.
NOVELTY - A lotus shell-bamboo charcoal bar comprises 50 wt.% lotus shell and 50 wt.% bamboo powder.    USE - Lotus shell-bamboo charcoal bar used in air purification and tea processing, and as fuel.    ADVANTAGE - The lotus shell-bamboo charcoal bar is non-toxic and environmentally-friendly. The lotus shell-bamboo charcoal burns for long time with less combustion ash and high heat value (above 7500 kcal).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of lotus shell-bamboo charcoal bar which involves crushing the raw materials, drying, cooling, pushing 30-50 tons of cooled materials through a molded sleeve at 190-260 degrees C and high pressure using a screw propeller, and burning the charcoal bar obtained in a kiln for 10 days to 2 weeks.
NOVELTY - The system (10) has a source for generating high-purity oxygen to be delivered to a fuel cell stack (20). An endothermic reformer (24) is coupled to the stack for processing input hydrocarbon fuel to cool the stack comprising a closed-cell cathode (28). The source comprises a cryogenic air separation unit (12) that simultaneously generates liquid nitrogen and the high-purity oxygen that comprises high-pressure oxygen to be delivered to the cathode. The stack comprises a molten carbonate fuel cell. The separation unit recovers hydrogen and carbon dioxide from an output stream of the stack.    USE - Integrated high temperature fuel cell system for industrial applications such as enhanced oil recovery.    ADVANTAGE - The system achieves high FTE efficiency at large scales in range of 65 to 75%, thus simultaneously recovering high purity hydrogen and liquid carbon dioxide with minimal parasitic load. The system provides synergistic benefit to the fuel cell in form of higher Nernst potential and reduced diffusion losses and minimizes thermal gradients in the fuel cell stack, thus reducing mechanical stress and entropy generation across the cell. The system realizes current results indicating 50% increase in power without significantly affecting efficiency, thus ensuring better manufacturing benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for operating a high temperature fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an integrated fuel cell system including an air separation unit, a fuel cell and carbon dioxide liquefaction/hydrogen separation unit.    Integrated high temperature fuel cell system (10)    Cryogenic air separation unit (12)    Fuel cell stack (20)    Endothermic reformer (24)    Closed-cell cathode (28)
NOVELTY - The method involves performing microaerobic treatment process for carrying out the biological waste treatment of the water containing para-toluylic acid in microaerobic state. The biological waste treatment of the water is carried out in an anaerobic condition. The biological waste treatment is carried out at the latter stage anaerobic processing process to microaerobic treatment process. The water by which the biological waste treatment carried out by microaerobic treatment process is returned to front stage anaerobic processing process.    USE - Water treatment method for treating biological waste water containing para-toluylic acid on anaerobic conditions.    ADVANTAGE - The biological waste treatment can be carried out on anaerobic conditions without completely degrading the organic compound in water and carbon dioxide. The para-toluylic acid can be decomposed into organic compound, without requiring large amount of aeration like an aerobic state.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a water treatment apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of water treatment apparatus.    Microaerobic processing tank (10)    Methane fermentation unit (20)    Acid generation tank (22)    Reaction tank (24)    Water treatment apparatus (100)
NOVELTY - The method involves sending an electric current and electrolyzing water among both surfaces of an electrolytic film (102) containing a solid polymer membrane which provided a catalyst layer in the surface. The water temperature-controlled only by the cathode side of the electrolytic film is supplied, when the pressure difference of both surfaces of the electrolytic film set to 50 kPa or less is controlled. The solid polymer membrane is reinforced by fluororesin porous membrane or polytetrafluoroethylene porous membrane.    USE - Water-electrolysis method for regeneration type fuel cell.    ADVANTAGE - The water electrolysis efficiency is improved, the purity of hydrogen and oxygen which are generated is ensured. The process is suitable for generation of hydrogen and oxygen in a weight, space, and a satellite with many installation restrictions and a space station. The gas separation of electrolysis efficiency at the time of water-electrolysis is made easy. Mixing of hydrogen to the inside of oxygen and mixing of oxygen to the inside of hydrogen are suppressed. Damage resulting from the pressure difference is prevented. The structure of water-electrolysis apparatus is simplified.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a water-electrolysis apparatus; and    (2) an electrolytic membrane used for water-electrolysis method.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the water-electrolysis apparatus.    Water-electrolysis apparatus (100)    Electrolytic film (102)    Water supply unit (120)    Oxygen side pressure control unit (130)    Hydrogen side pressure control unit (140)
NOVELTY - The air cell has a positive electrode which has carbonized paper. The negative electrode has a metal, and an electrolyte layer. The diameter of the hole which the first surface of the positive electrode has is smaller than the diameter of the hole which the second surface of the positive electrode. The electrolyte layer has water absorbing resin in which electrolyte solution is included. The negative electrode, the electrolyte layer, and the positive electrode are laminated.    USE - Air cell or a fuel cell for manufacturing carbonized paper.    ADVANTAGE - Provides low cost with the carbonized paper by using an electrode of an air cell or a fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a positive electrode containing the carbonized paper.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the air cell. (Drawing includes non-English language text).
NOVELTY - An interconnect has stainless steel substrate including surfaces (S1,S2), a chromium-oxide layer formed on surface (S1) of the substrate, and a metal-oxide coating formed on the chromium oxide layer. The chromium oxide layer has a thickness of 350-600 nm.    USE - Interconnect is used for low-temperature solid-oxide fuel cell for fuel stack for generating electrical energy (all claimed).    ADVANTAGE - The interconnect has excellent electroconductivity, chemical stability with respect to fuel and oxidant, and mechanical stability, and low contact resistance at the interconnect/electrode interface.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of an interconnect;    (2) fuel cell stack; and    (3) use of a fuel cell stack in generation of electrical energy.
NOVELTY - The device has a gasification furnace body (12) fixed with a combustion cavity body. An outer side wall of the gasification furnace body is provided with a supporting part and a limiting piece. The gasification furnace body is fixed with a top supporting lug and a gasification furnace cover. A box (21) is formed with an internal cavity. An air inlet is fixed with an air inlet cavity that is connected to an air inlet pipe (33). An air outlet box and the gasification furnace body are connected with the air inlet. An air box and a fuel gas furnace body are connected with the air inlet pipe.    USE - Biomass fuel gas carbonizing device.    ADVANTAGE - The device is simple in structure and environment-friendly, has high energy conversion rate and high combustible gas purity rate, and ensures high isolation effect and high safety performance and avoids backfire phenomenon and forestry waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a biomass fuel gas carbonizing device.    Gasification furnace body (12)    Box (21)    Air inlet pipe (33)
NOVELTY - The device has a high temperature fuel gas fan whose air outlet is connected with a first pipeline. An end of the first pipeline is connected with a fluidization bed pyrolysis gasification furnace. A side wall of the fluidization bed pyrolysis gasification furnace is connected with a biomass feeding device. Another side wall of the fluidization bed pyrolysis gasification furnace is provided with a reactant outlet that is connected with a second pipeline. A third pipeline is connected with a fourth pipeline and a low heat value fuel gas combustion chamber.    USE - Biomass pyrolysis gasification combustion section conversion biological coal/steam co-generation device.    ADVANTAGE - The device is simple in structure. The device has better reliability and low production cost. The device effectively increases production benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass pyrolysis gasification combustion section conversion biological coal/steam co-generating method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass pyrolysis gasification combustion section conversion biological coal/steam co-generation device.
NOVELTY - Specific gravity separator for carbon dioxide and methane of marsh gas, setting the barrel of the chamber (1), in the gas chamber (1) side height, setting 30-40% methane gas inlet (2) in the air room (1) top setting methane gas outlet (3), the chamber (1) Setting carbon dioxide outlet (4) at the bottom, set the methane compressor or fan (5) on the methane gas outlet (3), the carbon dioxide outlet (setting carbon dioxide compressor or fan (6) 4), methane compressor or fan (5) and carbon dioxide compressor or fan (6) while electrically connected with automatic switch (7). The utility model has beneficial effects as: a specific gravity type method, a simple device, a ground and a marsh gas methane and carbon dioxide and a separating and compare the low cost, make discharged harmful gas. atomphere of waste as treasure, environmental protection energy saving;
NOVELTY - The utility model claims a new automatic supply heat of biomass gasification device and oil gas cogeneration system, comprising a furnace and a combustion furnace, a furnace from upper to lower in turn divided pyrogenation, oxidation and reduction zone, zone equipped with way to a furnace outside the pyrolysis gas outlet, reduction area set with way to a furnace outside the gasification air outlet, matched set with pyrogenation element supply heat, burning furnace entrance reducing area is connected with a collection of solid product, the combustion furnace smoke gas outlet connected with a way to smoke channel and a supply heat. The utility model is a model for pyrolysis technique and gasification technology coupled on a set device of biomass from supply heat by forced rapid pyrolysis for production a tar pyrogenation in pyrogenation gas, residue and a falling response to cell oxidation reduction and gasification, generating a tar gasification gas, and a combustion zone producing carbon residue reduction and heat for the biomass supply heat, realize biological gas, coal better separation, a saving of energy and production cost. This new utility model can applied to preparing the biomass fuel gas.
NOVELTY - Traditional Chinese medicine comprises drug liquid for soaking food materials made of rice, where each food material comprises 0.5 g drug after soaking step.    USE - The traditional Chinese medicine is useful as rat poison (claimed).    ADVANTAGE - The traditional Chinese medicine is environmentally-friendly, causes no danger to other animals, and leads to diarrhea and thus kills rat.
NOVELTY - The station has a spray-type dust remover fixed in a gasification furnace. A dry dust remover is connected with a first gas transporting pipe. The spray-type dust remover is connected with a second gas transporting pipe. The spray-type dust remover is connected with a water-bath dust remover through a third gas transporting pipe. An end of a transporting pipe coat is connected with a sealing sleeve tube. The sealing sleeve tube is connected with an air inlet pipe. The sealing sleeve tube is connected with a wind pipe. An air outlet pipe is fixed in a purification wall through a firewall.    USE - Purification type heating biomass gas station.    ADVANTAGE - The station reduces heat exchanging effect, damage rate, chance of accidents happening and aging speed of the gas transporting pipe. The gas transporting pipe reaches red heat state. The station achieves heating during purification process.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a purification type heating biomass gas station.
NOVELTY - The utility model claims a a a a a hydrogen purifying device of reforming hydrogen fuel cell power generation module, a methyl alcohol water hydrogen production by reforming device (1), a high temperature proton exchange membrane fuel cell (2), a methanol water hydrogen production by reforming device (1) and high temperature proton exchange membrane fuel cell (2) is connected with the methanol water hydrogen production by reforming device (1) and high temperature proton exchange membrane fuel cell (2) is not formed between hydrogen purifying device. This utility model through a cancel hydrogen purifying device, reducing a palladium gold use cost, at the same time by a high temperature proton exchange membrane fuel cell, which avoids a platinum gold catalyst carbon monoxide poisoning, this utility new type main application sending power area in reforming hydrogen fuel cell.
NOVELTY - The utility model is a new supply of a biomass double fluidization bed gasification. methane device, belonging to biomass gasification technology area, wherein the incinerator feeder installed on the side wall of furnace, burning furnace cyclone separator installed on side wall of upper part of incinerator, incinerator cyclone separator through a return furnace material, furnace and gasification furnace returning part., gasification furnace feeder installed on gasification furnace and side wall of the gasification furnace cyclone separator installed on side wall of part of gasification furnace of the gasification furnace cyclone separator by... returning a,... returning device and a gasification furnace lower part communicated, gasification furnace cyclone separator part... waste heat boiler, a bag-type dust remover, cyclone dust collector cooling device, purifier, a methane tower. The utility model is a new type of a biomass double fluidization bed gasification. methane device, has high efficiency, stable operation, without a equal, biomass gasification technology is hard to solve the technology problem of methane is applied to a system.
NOVELTY - The utility model claims a new ultrasonic wave auxiliary shell of a kind a lime and mico-algae biological diesel oil preparing system. The device comprises shell powder grinding machine, turn calcining kiln, the first conveyor belt, the second conveyor belt, biologic diesel oil ultrasonic reacting tank, biological diesel oil ultrasonic reaction tank material chamber, the first organic solution storage tank, organic solution storage tank outlet, the first pump, the second pump, a valve, a first separating machine, the second centrifugal separating machine, the first channel, the second channel, distillation device, the oil storage tank, the oil storage tank entrance, organic solution recycling tank and organic solution recovery tank entrance, the biology diesel oil a tank using ultrasonic cavitation effect and emulsify effect of ultrasonic wave, matching chloroform/methyl alcohol organic solution and catalyst shell a series a lime, a mico-algae generating lipid transesterification, produce the solid liquid mixture through a separation machine centrifugal separating a crude biological diesel oil, distillation device by purifying a biological diesel oil.
NOVELTY - The new type utility claims have one anti-plant junction shell sum biogas pool, relating to marsh gas fermentation device technology field, comprising pool body and water in pressure with the lumen, upper part of pool body lumen as part of the following sum storage room, pool body lumen is fermentation room pool body on set with fermentation room and connected the feedstock tube and gas-guide tube, the lower part in water pressure provided with discharging mouth, internal pool body provided with a shell protecting device, the device comprises rotating shaft, and rotating shaft and the sum room connected to set with sealing tube, lower rotating shaft part connected with cutting device, cutting device is upper and lower at least 2 layer connected with the propeller blade, thickness of upper layer blades than thickness of lower layer small blades. The utility model is new type of beneficial effect: through upper layer blades stir, effective cutting structure shell, taking floating on the liquid side, break shell reach the goal. The lower propeller rotating, using plant substance under each level of mixing is more uniform, full fermentation, add reach to goal of gas quantity.
NOVELTY - A two phase A Anaerobic type film biologic reactor, flow composite type producing acid and complete mixed reactor producing methane reactor, complete mixing type producing methane reactor through circulation pump and tube-type film component, the out water end of tube-type film component divided producing port and wherein circulation, wherein circulation mouth and complete mixing type producing methane reactor, complete mixing type producing methane reactor gas outlet connected with the gas metering system, the metering system divided sum gas water separator and gas flow meter, a complete mixing type producing methane reactor is connected with gas outlet of gas separator to sum water separator, water is connected to gas flow meter, a sum sum water separator and liquid outlet through pipeline connected to complete mixing type producing methane reactor, comprising, composite type producing acid-flow reactor internal dividing into multiple of reaction room, the water inlet of each reaction room of the bottom, the water outlet is located at the top, each using one reaction room are as above to flow, the water inlet and water outlet of each reaction room is gradually connected in series.
NOVELTY - The utility model claims a novel biogas pool, comprising biogas pool main body, a marsh gas pool main body set with a gas-guide tube, the gas-guide the other end set with a condenser, the condenser is set with a condensing water pipe with the condenser by the condensed water pipe and biogas purification regulator connected with the bottom the marsh gas purification regulate and control device set with marsh gas and marsh gas purification a modulator tube, this utility model new structure design reasonable, suitable construction, low cost, not only fireproof performance, also can realize a a a a a a a gas and waste gas from storage, and has high yield, high safety performance and it can meet a requirement of the user.
NOVELTY - The new type utility claims one kind have high efficiency and low cost and environment-friendly pig died harmless processing compost fermentation shed, characteristic is, including fermentation fence is rectangular, the top support pole, top, middle and fermented fence composed of fermentation pool, formed with a plurality of partition of fermentation pool in the partition wall for fermentation pool is divided into multi-fermentation in different pools of, in between left wall of fermentation, rear wall, right wall and ceiling, partition wall and between the shed top are mounted with roller shutter, fermented fence is mounted with the front fence door, top, and fence door selecting light material composed of, fermentation pool is front high low floor, the floor inclination is 3-10 degree, lower part floor and wall surfaces of the fermentation pool are coated with waterproof layer. The utility model is new type with ring-friendly, efficient and simple structure and it can furthest reduce the died pig harmless treatment cost, reducing site disease dead pig to pig and pollute environment, preventing pig epidemic disease site is transmitting, and cause disease dead pig after composting fermentation so resource again use.
NOVELTY - The new type utility claims have one plant biomass forming fuel particle and preparation system, the utility model is new type of preparation system comprises raw material processing system, molding system, system and boiler system, a boiler system through high temperature steam pipe and warm air supply pipe in the raw material processing system to supply high temperature steam and middle temperature smoke sum, boiler system through high temperature air supply pipe to bake system providing high temperature smoke sum. The utility model is new type of system operation cost low, molding condition is mild, molding equipment loss small, heat can use rate high, the obtained molding fuel property is good.
NOVELTY - The method involves using wooden stick for raw earth rolling process. The soil is crushed and sieved finely. The de-ionized water is added little by little to ensure ratio between soil and water. The fine soil is mixed with de-ionized water evenly. The soil sample is manufactured uniformly in order to ensure same set of uniform density of soil samples. The large air bubbles and large voids are formed at the bottom of dish. The soil is taken out after finishing the experiment soil sample manufacture process. The charcoal is added in the soil to manufacture the impurity soil sample.    USE - Standardized experiment soil sample manufacturing method.    ADVANTAGE - The de-ionized water is added to the certain amount of fine soil, so that rigidity and density of the soil samples are improved. The standard process provides reference basis for rapid production of different types of soil texture.
NOVELTY - The hair color renovating agent comprises 0.5-2 pts. wt. metal complex dye, 0.4-1 pts. wt. softener, 45-60 pts. wt. ethyl alcohol, 0.2-1 pts. wt. mildew preventive agent, 0.5-2 pts. wt. brightening agent, 0.1-2 pts. wt. fungicide, 10-25 pts. wt. propane or butane, and 0.5-1 pts. wt. essence. The hair color renovating agent is prepared by mixing raw materials with stirring at room temperature.    USE - Hair color renovating agent.    ADVANTAGE - The hair color renovating agent has simple prescription, easy preparation, good coloring effect, and wide application range, gives bright surface color, and effectively prevents surface hardening.
NOVELTY - The biomass pyrolysis system has a heating furnace (1), a reaction kettle (2), a condensing tower (3) and a filtering device (4). A main portion of reaction kettle is located in a hearth of heating furnace. An air outlet end of reaction kettle is connected with an air inlet end of condensing tower through pipeline. An air outlet end of the condensing tower is connected with an air inlet end of a filter device through pipeline. An air outlet end of fuel gas power generation unit is connected with fuel gas furnace through pipeline.    USE - Biomass pyrolysis system for carbon gas cogeneration.    ADVANTAGE - The utilization rate of biomass pyrolysis system is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass pyrolysis system. (Drawing includes non-English language text)    Heating furnace (1)    Reaction kettle (2)    Condensing tower (3)    Filtering device (4)
NOVELTY - Hydrocarbon fuel comprises 40-60 pts. wt. biodiesel, 30-50 pts. wt. low carbon alcohol, 10-20 pts. wt. ether, 2-4 pts. wt. co-solvent, 2-4 pts. wt. stabilizer, 3-5 pts. wt. dispersant and 2-4 pts. wt. preservative.    USE - Hydrocarbon fuel.    ADVANTAGE - The hydrocarbon fuel is inexpensive, highly combustible, environmental-friendly and has high heat value. It has wide raw material source.
NOVELTY - Preparing multi-microbial strain liquid brewed wine comprises inoculating multi-microbial strain liquid into food grains, subjecting to compost stacking fermentation stage, where the multi-microbial strain liquid comprises bacterial liquid and yeast liquid in a mass ratio of 2:1-4:1.    USE - The method is useful for preparing multi-microbial strain liquid brewed wine (claimed).    ADVANTAGE - The method: is simple; improves the flavor of the wine and its quality; and has low production cost and high production efficiency.
NOVELTY - A liquid organic biofertilizer comprises fruits including pineapple, banana, papaya and mango; cow, goat, or sheep manure; cow, goat, or sheep urine; water; and molasses or sugar. The liquid organic biofertilizer is produced by fermenting peeled and softened fruit (pineapple); simultaneously fermenting cow, goat, or sheep manure and urine; mixing fermented fruit with fermented urine and manure, uniformly stirring, and continuously fermenting; adding water and fermenting; and filtering.    USE - Liquid organic biofertilizer used as substitute for chemical fertilizers.    ADVANTAGE - The liquid organic biofertilizer has low cost, high organic material content and high nutrient content; is rich in microbial decomposer and soil fertilizer; increases crop yield and quality; and saves production cost. Raw materials are easy to obtain. Production method is easy and short and optimizes utilization of livestock waste.    DETAILED DESCRIPTION - A liquid organic biofertilizer comprises fruits including pineapple, banana, papaya and mango; cow, goat, or sheep manure; cow, goat, or sheep urine; water; and molasses or sugar. The liquid organic biofertilizer is produced by introducing peeled and softened fruit (pineapple) into a tank, adding 2 kg molasses or 250 g sugar and 10 L water, uniformly stirring, fermenting for 1 week while stirring for 2-3 minutes everyday, and closing tank after stirring; simultaneously charging 10-12 kg cow, goat, or sheep manure into a 100-L tank, adding 80 L cow, goat, or sheep urine and closing the tank, and fermenting for 1 week while uniformly stirring for 2-3 minutes everyday; mixing fermented fruit with fermented urine and manure, uniformly stirring, and continuously fermenting for 1 week while uniformly stirring for 2-3 minutes everyday; adding 70 L water and fermenting for another 1 week while uniformly stirring for 2-3 minutes everyday; and filtering. (Abstract based on disclosure).
NOVELTY - Producing lignocellulosic material with cellulase and hemicellulose involves reacting lignocellulosic material with the hydrogen peroxide supplemented with ash from the lignocellulosic material.    USE - Method for producing lignocellulosic material used for obtaining monomeric sugars that are glucose, mannose, galactose, xylose, rhamnose and arabinose (claimed).    ADVANTAGE - The method enables to obtain monomeric sugars by producing lignocellulosic material in a simple, economical and eco-friendly manner.
NOVELTY - Preparation of organic fertilizer comprises formulating, preparing, and fermentation.    USE - Method for preparing organic fertilizer used for radix isatidis (claimed).    ADVANTAGE - The fertilizer has good ventilation system performance and strong water absorbent property, contains trace elements and nutrients, improves resource utilization, increases disease resistance, balances soil moisture, and promotes root development.
NOVELTY - Artificial wetland movable sewage purification treatment device comprises collection box (1), treating tank (2), water hopper (3), inlet holes (4), floating foam (5), base plate (6) and card slot. Collection box is located below the treatment tank. The treatment tank is connected to the base plate. The treatment tank is provided with card slots and connected to floating foam.    USE - Artificial wetland movable sewage purification treatment device.    ADVANTAGE - The device is simple, reasonable and easy to clean, has reduced blockage, and can control the flow of water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of artificial wetland movable sewage purification treatment device.    Collection box (1)    Treating tank (2)    Water hopper (3)    Water hopper (3)    Inlet holes (4)    Floating foam (5)    Base plate (6)    Matrix plate (6)
NOVELTY - Organic composite fertilizer comprises 50-70 pts. wt. earthworm manure, 30-50 pts. wt. pig manure, 20-30 pts. wt. dairy manure and 20-30 pts. wt. fly ash.    USE - Organic composite fertilizer.    ADVANTAGE - The organic fertilizer is nutritious and environment-friendly, and ensures no soil pollution with chemicals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic composite fertilizer, which involves fermenting mixture of earthworm manure, pig manure and cow dung for 30-50 days, where fermented material is mixed with fly ash uniformly.
NOVELTY - The method involves starting culture of phototrophic micro-organisms i.e. microalgae, on a growth medium at selective pressure. Non-sedimenting cultures are removed from the growth medium. Settling of biomass is selectively retained on non-settling biomass to form granules. Biomass with higher sedimentation rate on biomass with lower sedimentation rate is selectively retained. The phototrophic micro-organisms and other micro-organisms are present in the granules. Pellets are used to promote production of storage compounds during waste water treatment process.    USE - Method for obtaining granules of phototrophic micro-organisms i.e. microalgae, in a freshwater system and a marine system.    ADVANTAGE - The method enables using selective mechanisms to maintain functionality of the granules without requiring a sterilization equipment and incoming and outgoing flows and adding bacteria to provide mechanical stability of the granules.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a pellet.    DESCRIPTION OF DRAWING(S) - The drawing shows a photograph of micro-organisms.
NOVELTY - Method for utilizing soil using fruit tree branches involves crushing pruning fruit tree branches having particle size of 0.5-1 cm, mixing crushed branches with dry chicken manure, weathered coal, urea, calcium superphosphate and effective microorganism, grinding mixture, digging hole in soil to a height of 15-20 cm and depth of 40-60 cm, adding ground mixture into digged hole to a depth of 7-10 cm, irrigating and fertilizing soil, and covering fertilized soil using plastic thin film.    USE - The method is useful for utilizing soil using fruit tree branches (claimed).    ADVANTAGE - The method improves growth of crops.
NOVELTY - Purification of blue-green algae water body comprises cultivating Chinese medicinal herbs by conventional method, transplanting into the foam board, placing into the wetland area, letting the roots absorb the water and nutrients of wetland where seedlings for each foam board is single species, taking the cultured herbs seedlings, allowing to grow to 30-50 cm high, transferring to foam board, letting fibrous roots absorb nutrients in the water and pruning stems and leaves without application of fertilizer and pesticides.    USE - Method for purifying blue-green algae water body (claimed).    ADVANTAGE - The method is environment-friendly, non-toxic and has no side effect.    DETAILED DESCRIPTION - Purification of blue-green algae water body comprises cultivating Chinese medicinal herbs by conventional method, transplanting into the foam board, placing into the wetland area, letting the roots absorb the water and nutrients of wetland where seedlings for each foam board is single species, taking the cultured herbs seedlings, allowing to grow to 30-50 cm high, transferring to foam board, letting fibrous roots absorb nutrients in the water and pruning stems and leaves without application of fertilizer and pesticides. The Chinese medicinal herbs are made of 20-30 pts. wt. honeysuckle, 10-20 pts. wt. Fagopyrum cymosum, 10-20 pts. wt. radix isatidis, 5-10 pts. wt. Houttuynia cordata, 5-10 pts. wt. ciliate desert-grass, 5-10 pts. wt. garlic, 5-10 pts. wt. Acorus calamus, 40-50 pts. wt. clover and 50-60 pts. wt. Eupatorium.
NOVELTY - Flower fertilizer comprises 10-20 wt.% rapeseed cake residue, 10-20 wt.% peanut rice residue, 25-35 wt.% soybean, 10-20 wt.% sauce slag, 8.5-12.5 wt.% plant ash water, 6.5-14.5 wt.% taomi and 2-6 wt.% yeast powder.    USE - Flower fertilizer.    ADVANTAGE - The flower fertilizer is eco-friendly, and enriched in nutrient, and manufacture is simple, and ensures no side effect on flowers.
NOVELTY - The system has a fermentation pool that is provided with a fermentation chamber. A gas storage plate is fixed inside fermentation chamber by a supporting device. A fermentation area is provided between a material blocking plate and a baffle plate. The top portion of fermentation area is formed with an independent gas-guide tube. A pull rod is fixed with feedstock baffle plate and discharge opening blocking plate. The pull rod is fixed in the fermentation chamber. Two vertical rods are located at the clearance between gas storage plate and pool.    USE - Self-circulating and anti-blocking biogas fermentation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the self-circulating and anti-blocking biogas fermentation system.
NOVELTY - Treatment of microcystin-LR polluted water involves inoculating microcystin-LR (MC-LR) degrading bacteria to an inorganic salt medium with MC-LR initial concentration of 0.1-5 mg/L based on inoculation amount of 1 g/L, reacting for 2-6 days, and then adding a Fenton reagent and degrading obtained mixture with pH of 4 for 30-60 minutes at 25 degrees C and speed of 130 rpm. The MC-LR degrading bacteria are obtained by culturing Pseudomonas putida or Microcystis aeruginosa (FACHB905) in BG-11 culture medium.    USE - Treatment of microcystin-LR polluted water (claimed).    ADVANTAGE - The method efficiently and economically removes microcystin-LR from sewage water with high efficiency.    DETAILED DESCRIPTION - Treatment of microcystin-LR polluted water involves inoculating microcystin-LR (MC-LR) degrading bacteria to an inorganic salt medium with MC-LR initial concentration of 0.1-5 mg/L based on inoculation amount of 1 g/L, reacting for 2-6 days, and then adding a Fenton reagent and degrading obtained mixture with pH of 4 for 30-60 minutes at 25 degrees C and speed of 130 rpm. The MC-LR degrading bacteria are obtained by culturing Pseudomonas putida or Microcystis aeruginosa (FACHB905) in BG-11 culture medium, centrifuging and removing supernatant, adding the supernatant and activated carbon simultaneously to MC-LR sewage, cultivating at 25 degrees C for 3 days and performing slab cultivation, streak cultivation and slant cultivation.
NOVELTY - Fertilizer comprises pig bone (10-20 pts. wt.), fish bone (10-20 pts. wt.), tea root (20-30 pts. wt.), soybean residue (10-15 pts. wt.), pericarp (5-0 pts. wt.), urea (0.5-1.5 pts. wt.), monopotassium phosphate (0.1-0.2 pts. wt.), calcium superphosphate (0.3-0.5 pts. wt.), magnesium sulfate (0.05-0.1), ferrous sulfate (0.05-0.1), boric acid (0.1-0.2) and rice vinegar (0.3-0.6).    USE - Fertilizer used for camellia plant (claimed).    ADVANTAGE - The fertilizer has improved nutrients, and shows improved absorption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing, which involves:    (A) weighing pig bone, fish bone, tea root, soybean residue, and pericarp;    (B) adding water to weighed material to carry out fermentation the for 10-20 days; and    (C) adding urea, monopotassium phosphate, calcium superphosphate, magnesium sulfate, ferrous sulfate, boric acid, and rice vinegar to fermented product with stirring to obtain final product.
NOVELTY - Organic fertilizer comprises 250-300 pts. wt. dairy manure, 50-70 pts. wt. edible fungus residue, 20-25 pts. wt. sawn wood ash and 5-15 pts. wt. Bacillus subtilis leavening agent.    USE - Organic fertilizer used for improving soil (claimed).    ADVANTAGE - The organic fertilizer controls pH value, reduces soil acidity and increases soil organic matter and nitrogen, potassium phosphorus content, and ensures easy storage and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves;    (A) fermenting wet cow dung anaerobically in sealed state at 50-65 degrees C;    (B) drying fermented dairy manure;    (C) decomposing edible fungus residue at 50 degrees C for 45-55 days;    (D) drying sawn wood ash;    (E) mixing Bacillus subtilis liquid with edible fungus residue uniformly;    (F) fermenting obtained mixture at 25-30 degrees C for 7-9 days to obtain Bacillus subtilis leavening agent;    (G) mixing obtained raw materials uniformly; and    (H) drying obtained mixture to obtain product.
NOVELTY - Preparing soil conditioner comprises: (i) respectively crushing 21% silicon fertilizer, 25% humic acid-containing natural peat and 49% clay mineral into powder; (ii) uniformly mixing all the raw materials; (iii) drying 5% bioremediation agent at room temperature for 3-3.5 hours, then crushing; and (iv) carrying out secondary mixing of bioremediation agent with raw materials.    USE - Used as soil conditioner.    ADVANTAGE - The soil conditioner supplements biologically active component and nutrient composition to the soil, and enhances water retention, fertility and permeability of the soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for soil conditioner, comprising silicon fertilizer, humic acid-containing natural peat, clay mineral and bioremediation agent.
NOVELTY - Sewage treatment of secondary settling tank floating sludge includes dividing floating sludge based on number of filamentous microorganisms division, particularly primary alert level, secondary alert level and tertiary alert level, performing appropriate measures to control depending on alert level, adjusting nitrification liquid for primary alert level at mass ratio of 1-3:1, maintaining sludge reflux ratio to 0.5-1:1, and adjusting dissolved oxygen concentration to 2-4 mg/L in aerobic biological aeration tank.    USE - Method for treating secondary settling tank floating sludge.    ADVANTAGE - The method is inexpensive, economical, and reduces operation cost.    DETAILED DESCRIPTION - Sewage treatment of secondary settling tank floating sludge involves dividing floating sludge based on number of filamentous microorganisms division, particularly primary alert level, secondary alert level and tertiary alert level, performing appropriate measures to control depending on alert level, adjusting nitrification liquid for primary alert level at mass ratio of 1-3:1, maintaining sludge reflux ratio to 0.5-1:1, adjusting dissolved oxygen concentration to 2-4 mg/L in aerobic biological aeration tank, adjusting nitrification liquid for secondary alert level at mass ratio of 1-3:1, maintaining sludge reflux ratio to 3-5:1, adjusting dissolved oxygen concentration to 2-4 mg/L in aerobic biological aeration tank, dosing with 5-10 mg/L fungicide in aerobic tank to control the number of filamentous microorganisms, adjusting nitrification liquid for tertiary alert level at mass ratio of 5-7:1, adjusting dissolved oxygen concentration to 2-4 mg/L in aerobic biological aeration tank, dosing with 10-15 mg/L fungicide in aerobic tank to control the number of filamentous microorganisms and increasing settling tank sludge emission.
NOVELTY - A fruit special fertilizer comprises chicken manure, duck manure fermentation mixture, urea, potassium chloride, iron sulfate and calcium nitrate at weight ratio of 28:3:12.5:3.2:0.65.    USE - Fruit special fertilizer.    ADVANTAGE - The fertilizer is energy-saving, rich in organic substance, increases taste, quality and yield of fruit, provides organic matter for soil, and has low cost, high fertilizing efficiency, and synergistic effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fruit special fertilizer comprising mixing chicken manure and duck manure fermentation mixture, sterile freezing to 12-15 degrees C for 20-35 minutes, drying, adding remaining raw materials, uniformly stirring, and processing into special fertilizer at 45-60 degrees C.
NOVELTY - Organic fertilizer comprises 60% dried leaves powder, 35% river sludge, 3-4% ammonium dihydrogen phosphate, and 1-2% active bacterial strain formulation.    USE - As organic fertilizer.    ADVANTAGE - The organic fertilizer is rich in nitrogen, phosphorous and potassium.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic fertilizer, whuc involves crushing dried leaves into powder, mixing the powder with river sludge, adding ammonium dihydrogen phosphate, mixing materials, incubating mixture for 12 hours, adding active bacterial strain formulation, after 6 hours, fermenting mixture for 24 hours, drying fermentation product at 80-100 degrees C for 10-30 minutes, and making dried product into granules.
NOVELTY - Fiberglass insulation anaerobic base of the tower comprises two sets of the same monomers (1,2), assembly, docking base and metal fasteners.    USE - Fiberglass insulation anaerobic base of the tower for producing biogas.    ADVANTAGE - The fiberglass insulation anaerobic base of the tower can be reused, protects environment, economical and enables large-scale production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fiberglass insulation anaerobic base of the tower.    Monomers (1,2)
NOVELTY - Preprocessing corn straw involves selecting, drying and crushing corn straw to 20 meshes. Water is used as pre-treatment reagent for preprocessing. Tap water (1-10 times the amount) is added to the straw and mixed by stirring. The mixture is sealed with a membrane at -20 degrees C for 3 days for preprocessing. Anaerobic fermentation is performed after preprocessing. The anaerobic fermentation process requires activated sludge. The straw is added in an amount of 52g of total solute where the activated sludge is taken in an amount of 12g of total solute.    USE - Method for preprocessing corn straw used for increasing anaerobic digestion performance (claimed).    ADVANTAGE - The method enables to process corn straw in a eco-friendly, cost-effective and simple way, and provides high-quality fertilizer.    DETAILED DESCRIPTION - Preprocessing corn straw involves selecting, drying and crushing corn straw to 20 meshes. Water is used as pre-treatment reagent for preprocessing. Tap water (1-10 times the amount) is added to the straw and mixed by stirring. The mixture is sealed with a membrane at -20 degrees C for 3 days for preprocessing. Anaerobic fermentation is performed after preprocessing. The anaerobic fermentation process requires activated sludge. The straw is added in an amount of 52g of total solute where the activated sludge is taken in an amount of 12g of total solute. Tap water is added to the reaction device to a total volume of 80% and is filled with nitrogen. The reaction device is sealed with a rubber plug and reactor is fixed in a shaker at a constant temperature between 35 plus minus 2 degrees C.
NOVELTY - Yeast agent comprises Saccharomyces cerevisiae RIPP06 (CGMCC No. 8203), S.cerevisiae RIPP01 (CGMCC No. 8201) and S.cerevisiae RIPP07 (CGMCC No. 8204).    USE - The yeast agent is useful for producing ethanol from hydrolysis product of starch containing plant material and/or hydrolysis product of cellulose containing plant material (all claimed), which is used as fuel.    ADVANTAGE - The yeast agent has excellent multi-stress tolerance ability, stable genetic properties, and excellent sugar utilization rate and hence high ethanol production ability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method (M1) for preparing yeast agent involves inoculating Saccharomyces cerevisiae RIPP06, S.cerevisiae RIPP01 and S.cerevisiae RIPP07 in a ratio of 1:0.5-2:0.5-2 into yeast culture medium, where the total inoculation amount of yeast is 103-108 cells with respect to per g of total sugar content in the yeast culture medium; and (2) method (M2) for producing ethanol involves mixing ethanol fermentation raw material solution with the yeast agent.
NOVELTY - A semi-solid-state complex no-tillage dry direct seeding method involves carrying out dry direct seeding tillage technique, maintaining water layer in ditch before harvesting previous crop, scattering crop seeds on carriage side after harvesting crop straw or wheat straw, applying fertilizer, starting the crop seeds to seedling up at carriage side, spreading crop seeds, semisolid biomass material and biological pesticide mixture, followed by controlling moisture content of the biological material, maintaining no irrigation after planting, and maintaining the carriage side at arid state.    USE - Semi-solid-state complex no-tillage dry direct seeding method for crop seeds.    ADVANTAGE - The method enables seeding the crop seeds with better ecological benefit, reduced operation energy consumption, improved pesticide stubble cleaning, and reduced haze and irrigation with water.    DETAILED DESCRIPTION - A semi-solid-state complex no-tillage dry direct seeding method involves carrying out dry direct seeding tillage technique, maintaining water layer in ditch to 1-5 cm before harvesting previous crop, scattering crop seeds on carriage side after harvesting crop straw or wheat straw, applying fertilizer, starting the crop seeds to seedling up at carriage side, spreading crop seeds, semisolid biomass material and biological pesticide mixture at a mass ratio of (1-10):(70-800):(1-3), followed by controlling moisture content of the semi-solid biological material at 40-80%, maintaining no irrigation after planting, maintaining the carriage side at arid state for 3-7 days, forming semi solid layer, basal layer of straw and soil layers from top to bottom of the carriage side.
NOVELTY - Processing livestock and poultry excrement comprises piling poultry and livestock manure in cultivation site, and using as organic fertilizer in farmland and orchard, as organic feed to crops which can be harvested and processed as livestock and poultry feed; and subjecting sewage, urine and flushing liquid to multistage anaerobic fermentation, and using as fertilizer in farmland and orchard.    USE - Method for processing livestock and poultry excrement to produce fertilizer (claimed).    ADVANTAGE - The method is simple; not only enables effective utilization of livestock and poultry excrement, but also rational utilization of sewage and other waste; and realizes ecological waste recovery and recycling with harmless emission.
NOVELTY - A steam ejector-type organic waste processing system comprises feeding robot, bag-breaking drum screening machine, permanent magnetic separator, winnowing machine, pulverizer, steam ejection-type organic waste processor, drum-type dryer, cylindrical initial cleaning sieve and organic fertilizer production device sequentially connected through conveyors. The organic waste processor comprises pressure ejection device, pressure ejection device rotary controller, elevated feeding funnel, feeding and lifting device, discharge guide tube, and gas-solid separator.    USE - Steam ejector-type organic waste processing system used for producing organic fertilizer.    ADVANTAGE - The system shortens fertilizer production period; has large waste processing amount, high efficiency, convenient operation and strong operability; solves environmental pollution caused by waste; and achieves recycling and environment protection.    DETAILED DESCRIPTION - A steam ejector-type organic waste processing system comprises feeding robot, bag-breaking drum screening machine, permanent magnetic separator, winnowing machine, pulverizer, steam ejection-type organic waste processor, drum-type dryer, cylindrical initial cleaning sieve and organic fertilizer production device sequentially connected through conveyors. The organic waste processor comprises pressure ejection device, pressure ejection device rotary controller and elevated feeding funnel mounted in system frame from bottom to top; feeding and lifting device arranged on one side of system frame; discharge guide tube arranged at lower part of pressure ejection device; and gas-solid separator connected with discharged guide tube.
NOVELTY - Preparing S(+) ibuprofen involves performing ester hydrolysis reaction by using ibuprofen methoxy ethyl ester as substrate and triacylglyceride diacylglycerol hydrolase as biological conversion catalyst to obtain S(+) ibuprofen crude product.    USE - Method for preparing S(+) ibuprofen (claimed).    ADVANTAGE - The method enables to prepare eco-friendly and cost-effective S(+) ibuprofen in a simple way with mild reaction conditions.
NOVELTY - Anaerobic device comprises U-type device body provided with two openings together upside down from each other, gas storage cabinet (1) and multiple stirrers. The cabinet is provided with hollow flat tube. The middle body is provided with one cylinder steel pipe, steel flat top, device ports and transverse pole. The bottom side of the device body is provided with slag discharge port.    USE - Anaerobic device.    ADVANTAGE - The anaerobic device is eco-friendly, cost-effective, easy to use, has high efficiency, high concentration and stainless steel gas cabinet, increases biogas production by automatic mixing and enables to use the waste products.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an anaerobic device.    Gas storage cabinet (1)    Bell stent (2)    Inlet (3)    Windpipe (4)    Automatic exhaust valve (9)    Overflow pipe (10)
NOVELTY - Composition comprises 15-70% potato powder, 10-20% sucrose, 5-40% cellulose, 0.5-2% potassium dihydrogen phosphate, 0.5-3% ammonium sulfate, 0.5-2% magnesium sulfate, 0.5-2% nitric acid, 0.5-2% calcium chloride, 0.5-4% ferrous sulfate, 2-15% pepton and 0.5-2% oleic acid.    USE - Composition used for treating sewage (claimed).    ADVANTAGE - The composition is economic, and does not cause pollution.
NOVELTY - Method for culturing Dendrobium, involves (a) setting each greenhouse with height of 2.5 m and width of 6 m, (b) selecting rotten wood with diameter of 5-20 cm, and length of 60-100 cm, (c) drilling wood in drilling device at pitch of 6-10 cm, and inoculating fungus into the hole, (d) screening Dendrobium seedlings, (e) planting the seedlings on the wood containing hole with roughness of 4-10 cm, (f) spraying 1-2 l/m2 water on every day (3-6 pm), and (g) harvesting fungus and Dendrobium.    USE - The method is useful for culturing Dendrobium (claimed).    ADVANTAGE - The method reduces usage amount of fertilizer.
NOVELTY - Preparation of biologic fertilizer comprises taking high density fungus suspending liquid with Bacillus subtilis (CICC 10339) culture with density of 109-1010; and cutting sea buckthorn branches into small sections, spraying high density fungus suspending liquid, and fermenting.    USE - Method for preparing biologic fertilizer used for killing sea buckthorn pathological fungus (claimed).    ADVANTAGE - The method is simple, and has no wastewater discharge, low investment, low energy consumption, easy operation, and easy industrial scale production.
NOVELTY - Fermenting biomass involves selecting biomass as adsorbent. The adsorbent adsorbs catering waste water. The proper amount of biomass and catering waste water are treated under specific condition. The catering waste water is processed before adsorption. The proper amount of biomass is placed into absorbing pool under the optimal conditions, which are certain dosage, adsorption time, property of catering waste water, proper heating at 30 degrees C, removing rate for chemical oxygen demand and oil content.    USE - Method for fermenting biomass (claimed).    ADVANTAGE - The method enables to ferment biomass, which has effective treatment to the catering waste water, absorbs waste water, shortens fermentation time and increase production of biogas.    DETAILED DESCRIPTION - Fermenting biomass involves selecting biomass as adsorbent. The adsorbent adsorbs catering waste water. The proper amount of biomass and catering waste water are treated under specific condition. The catering waste water is processed before adsorption. The proper amount of biomass is placed into absorbing pool under the optimal conditions, which are certain dosage, adsorption time, property of catering waste water, proper heating at 30 degrees C, removing rate for chemical oxygen demand and oil content. The obtained material, which is treated waste water saturated dining oiled biomass is placed into fermentation tank. The optimal conditions of fermentation tank for biogas production are adjusted pH, temperature, inoculation sludge and carbon nitrogen ratio. The fermentation time of biomass and kitchen garbage are compared. The starting time of fermentation is shortened for increasing yield of biogas.
NOVELTY - Preparing microbial nutrient solution involves mixing soybean flour and molasses in certain proportion. The soybean flour and molasses are added according to pollution and concentration of hexavalent chromium ions in soil and sediments.    USE - Method for preparing microbial nutrient solution for treating chromium contaminated soil and sediment (claimed).    ADVANTAGE - The method enables to prepare microbial nutrient, which is eco-friendly, easy to use and cost-effective as raw materials are easily available.
NOVELTY - Bioorganic fertilizer comprises 40-90 wt.% sugar refinery waste fermentation powder, 5-40 wt.% Bacillus subtilis powder, and 5-20 wt.% auxiliary agent.    USE - The bioorganic fertilizer is useful for improving plant growth, chlorophyll content, plant height, and stem diameter of plant. The plant is sugarcane (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing bioorganic fertilizer, which involves (a) preparing sugar refinery waste fermentation powder by mixing sugar refinery waste, bagasse, and molasses in a weight ratio of 2-8:2-8:1-4, adding 50-150 wt.% mixture to water, adding mixture into fermentation tank, performing fermentation at 40-50 degrees C for 10-15 days, where the fermentation is performed using microbial inoculum comprising Vibrio parahaemolyticus, Bacillus licheniformis, Streptomyces, and Candida tropicalis in a weight ratio of 1-2:1-2:1-2:1-2, and drying and grinding fermented product, and (b) adding Bacillus subtilis powder, and auxiliary agent to product obtained in step (a). Preferred Product: The bioorganic fertilizer comprises 60-80 wt.% waste fermentation powder in sugar refinery, 10-30 wt.% Bacillus subtilis powder, and 6-15 wt.% auxiliary agent.
NOVELTY - A glycosyl amide-modified tetramethylcyclotetrasiloxane derivative (I) is new.    USE - Glycosyl amide-modified tetramethylcyclotetrasiloxane derivative used for drug delivery.    ADVANTAGE - The method is environment-friendly, has high safety, simple process, and low cost, and meets industrial production requirements. The compound has excellent surface activity and aggregates into micelles-like aqueous solution.    DETAILED DESCRIPTION - A glycosyl amide-modified tetramethylcyclotetrasiloxane derivative of formula (I) is new.    R=groups of formulae (a)-(b); and    n=0, 7, 11, 15, or 17.    An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - An inertial impaction type cleaning device (200) removes moisture and fine dust among sampled landfill gas collected by collecting device (100). An ammonia and hydrogen sulfide removing apparatus (300) removes ammonia and hydrogen sulfide in first purification landfill gas. A siloxane removing apparatus (400) removes siloxane in second purification landfill gas. An oxygen removing apparatus (500) removes oxygen of third purification landfill gas which is cleaned up by siloxane removing apparatus. A nitrogen removal apparatus (600) removes nitrogen of fourth purification landfill gas.    USE - Landfill gas conversion device for conversion of methane used as fuel for vehicle, from landfill gas generated in waste landfill, sewage sludge, and organic waste anaerobic fermentation equipment.    ADVANTAGE - The moisture elimination efficiency is improved by having the inertial impaction effect and condensation cooling effect, so that the work efficiency of conversion device is improved. The economical efficiency of device is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the landfill gas conversion device.    Landfill gas collecting device (100)    Inertial impaction type cleaning device (200)    Ammonia and hydrogen sulfide removing apparatus (300)    Siloxane removing apparatus (400)    Oxygen removing apparatus (500)    Nitrogen removal apparatus (600)
NOVELTY - Cultivating Pleurotus eryngii involves (a) taking corn cob, soybean, shiitake mushrooms, limestone, and gypsum, (b) soaking shiitake mushroom particles in water, adding remaining materials to the soaked mushroom, and piling mixture for performing stack fermentation, (c) fermenting mixture naturally, inoculating P.eryngii in fermented mixture, and covering the fermented mixture, and managing growth of fruiting body, and (d) harvesting mushrooms.    USE - The method is useful for cultivating P.eryngii (claimed).    ADVANTAGE - The method conserves manpower and coal, and is environmentally-friendly.    DETAILED DESCRIPTION - Cultivating Pleurotus eryngii involves (a) taking 70-76% corn cob, 16-20% soybean, 3-4% shiitake mushrooms, 4-5% limestone, and 1% gypsum, crushing corn cob crushed to a particle size of 3-5 mm, and crushing shiitake mushrooms to a particle size of 2-3 mm, (b) soaking shiitake mushroom particles in 20-30 times water at room temperature for 18-24 hours, adding remaining materials to the soaked mushroom, and piling the mixture for performing stack fermentation, (c) fermenting the mixture naturally at 60 degrees C for 24 hours until moisture content reaches 63-65%, inoculating the P.eryngii in fermented mixture, and covering the fermented mixture, and managing growth of fruiting body, and (d) harvesting mushrooms.
NOVELTY - The reactor has a first temperature sensor (1) and a third temperature sensor (14) mounted in an upper sidewall of a cylindrical reactor tank main portion (18). A second temperature sensor (10) is mounted in inner side of tank main portion provided with an air outlet (2), an air inlet (13), a feeding port (3), a discharge port (15), a reflux port (4), a leachate outlet (16) and a water inlet (31). The tank main portion is provided with a high heat-conducting graphite material layer, a silicate insulating layer, and a heating layer connected with a silk temperature control box (32).    USE - Aerobic composting reactor for treating municipal solid waste in cold region.    ADVANTAGE - The domestic garbage in northern cold area is treated effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the aerobic composting reactor for treating municipal solid wastes in cold region.    Temperature sensor (1,10,14)    Air outlet (2)    Feeding port (3)    Reflux port (4)    Air inlet (13)    Discharge port (15)    Leachate outlet (16)    Cylindrical reactor tank main portion (18)    Water inlet (31)    Silk temperature control box (32)
NOVELTY - Manufacturing composite fertilizer involves utilizing 15-20 pts. wt. polyphenol carboxylic acid compound, 10-15 pts. wt. rapeseed cake fermented solution, 3-6 pts. wt. bovine heart core powder, 0.3-0.6 pts. wt. pyrethroid, 2-5 pts. wt. wheat husk fermented solution, 4-8 pts. wt. fallen leaves humus and 10-15 pts. wt. diluted beer. Polyhydric carboxylic acid compound, rapeseed cake fermented solution and fallen leaves humus are mixed and stirred with diluted beer in a bucket. The bucket is sealed and fermented 40 degrees C for 48-72 hours.    USE - Method for manufacturing composite fertilizer used for flowering (claimed).    ADVANTAGE - The method enables to manufacture composite fertilizer, and ensures disease resistant ability and vigorous growth of flower.    DETAILED DESCRIPTION - Manufacturing composite fertilizer involves utilizing 15-20 pts. wt. polyphenol carboxylic acid compound, 10-15 pts. wt. rapeseed cake fermented solution, 3-6 pts. wt. bovine heart core powder, 0.3-0.6 pts. wt. pyrethroid, 2-5 pts. wt. wheat husk fermented solution, 4-8 pts. wt. fallen leaves humus and 10-15 pts. wt. diluted beer. Polyhydric carboxylic acid compound, rapeseed cake fermented solution and fallen leaves humus are mixed and stirred with diluted beer in a bucket. The bucket is sealed and fermented at 40 degrees C for 48-72 hours. The fermented product is dried at low temperature and crushed through a pulverizer and sieved with 35-40 meshes. Remaining components are mixed with the powder, and then crushed through the pulverizer and sieved with 40-50 meshes.
NOVELTY - 1,6-Diethyladipate is added to reactor under dry nitrogen, and dried using anhydrous toluene. Benzophenone and metallic sodium are added to reactor, and stirred till the solution turns to dark blue color. The resulting mixture is heated, trimethylchlorosilane is dripped in the resulting mixture, stirred, maintained till the blue color of the solution disappears, stirred, and insoluble sodium chloride is filtered off. The filtrate is concentrated, toluene solvent is distilled off under pressure, and 10-12 mm mercury fraction is collected to obtain 1,2-bis(trimethylsilyloxy)cyclohexene.    USE - Preparation of 1,2-bis(trimethylsilyloxy)cyclohexene (claimed).    ADVANTAGE - The method provides 1,2-bis(trimethylsilyloxy)cyclohexene without post-treatment, by feasible and environmentally-friendly process.    DETAILED DESCRIPTION - 1,6-Diethyladipate is added to reactor under dry nitrogen, and dried using anhydrous toluene. Preset amount of benzophenone and metallic sodium are added to reactor, and stirred till the solution turns to dark blue color. The resulting mixture is heated to 50 degrees C, trimethylchlorosilane is dripped in the resulting mixture, stirred for 3-4 hours, maintained till the blue color of the solution disappears, stirred again for 1 hour, and insoluble sodium chloride is filtered off. The filtrate is concentrated, toluene solvent is distilled off under pressure, and 10-12 mm mercury fraction at 102-105 degrees C is collected to obtain 1,2-bis(trimethylsilyloxy)cyclohexene.
NOVELTY - A recombinant bacterium comprising host cell and target gene transferred into the host cell, is new. The target gene is encoding gene of Phanerochaete chrysosporium lytic polysaccharide monooxygenase (LPMO).    USE - The recombinant bacterium is used for degrading cellulosic material, preferably microcrystalline cellulose or crop straw (all claimed).    ADVANTAGE - The recombinant bacterium increases generation of glucose by 100 times, and degradation velocity and degree of the cellulose.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for constructing the recombinant bacterium; and    (2) use of the recombinant bacterium for degrading cellulosic material.
NOVELTY - Wheat bioactive peptide additive comprises greater than or equal to 90 %mass oligopeptide having molecular weight of less than 1000 Da with respect to total protein.    USE - The wheat bioactive peptide additive is used in serum-free medium for culturing Chinese hamster ovary (CHO) cells, vero cells, human embryonic kidney (HEK)-293 cells, baby hamster kidney (BHK)-21 cells, MARC-145 cells, hybridoma, and Madin-Darby canine kidney epithelial (MDCK) cells (all claimed).    ADVANTAGE - The additive reduces cost of cell culture medium, is environmentally-friendly, promotes cell proliferation, improves cell viability and enhances expression of cell products.    DETAILED DESCRIPTION - Wheat bioactive peptide additive comprises greater than or equal to 90 %mass oligopeptide having molecular weight of less than 1000 Da with respect to total protein. The oligopeptide comprises at least one or more of Val-Asn, The-Phe-Asn, Gln-Val-Ser-Gln, His-Gly-Ala-Gln, Gly-Gly-Asp-Asn-Pro, and Gly-Thr-Cys-Gly-Ala-Gly. INDEPENDENT CLAIMS are included for the following:    (1) serum-free medium; and    (2) method for preparing the wheat bioactive peptide additive.
NOVELTY - A gene encoding L-alanine oxidase, which is obtained from yeast cDNA library, comprising fully defined 1272 bp (SEQ ID NO: 1) given in the specification, is new.    USE - The gene or L-alanine oxidase is useful for asymmetric deacetylation degradation of DL-alanine; and for producing D-alanine.    ADVANTAGE - By using the gene or L-alanine oxidase, the method improves the efficiency of degradation of DL-alanine, shortens D-alanine production process, reduces production cost, and reduces environmental pollution.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) L-alanine oxidase comprising fully defined 423 amino acids (SEQ ID NO: 2) given in the specification, and having a molecular weight of 49523.12 Da; (2) a recombinant expression plasmid derived from recombinant gene encoding L-alanine oxidase; (3) a genetically engineered bacterial strain, preferably Escherichia coli strain that is transformed by the recombinant plasmid; and (4) a method for preparing L-alanine oxidase comprising: (a) cloning gene encoding L-alanine oxidase; (b) constructing recombinant expression plasmid; (c) linearization and purification of the recombinant expression plasmid; (d) obtaining genetically engineered bacterium that is transformed by recombinant expression plasmid; and (e) purifying and identifying genetically engineered bacterium expressing L- phenylalanine oxidase.
NOVELTY - Carbon-steel reinforced structure anaerobic power supply station comprises an anaerobic tank unit, a purification tower, an anaerobic tank heating system and a generator. The construction material for the anaerobic tank is steel. The structure of carbon steel is steel column frame structure.    USE - Used as carbon-steel reinforced structure anaerobic power supply station.    ADVANTAGE - The power supply station realizes clean energy production, ensures recycling of the farm, the livestock and the urban waste, and is environmentally friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the carbon-steel reinforced structure anaerobic power supply station.
NOVELTY - Enamel reinforced concrete structure-type anaerobic gas power station comprises an anaerobic tank unit, a purification tower, an anaerobic tank heating system, a power generation unit which is provided with four major components. The anaerobic tank unit is provided with building materials, preferably enamel. The enamel is provided with Canadian steel column beam frame structure.    USE - The station is useful in towns; farms; sewage farms; multi-stage anaerobic fermentation, stirring, heating and warming using straw raw material; automatic alarm devices; and production of biogas by stirring and warming slurry in tank body (claimed).    ADVANTAGE - The station has high biogas production efficiency, saves raw materials sources, and is environmental friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the enamel reinforced concrete structure-type anaerobic gas power station.
NOVELTY - Chinese herbal medicine biological foliar fertilizer includes 5-8 pts. wt. dyers woad leaf, 3-4 pts. wt. dandelion, 2-5 pts. wt. blackberry lily, 3-4 pts. wt. radix isatidis, 3-5 pts. wt. honeysuckle, 1-2 pts. wt. tuckahoe, 1-2 pts. wt. Polygonum cuspidatum, 2-3 pts. wt. radix stemonae, 2-3 pts. wt. betelnut, 3-4 pts. wt. Chinaberry fruit, 2-3 pts. wt. quisqualis, 5-6 pts. wt. hairyvein agrimony, 1-2 pts. wt. radix sophorae flavescentis, 1-3 pts. wt. Pseudolarix, 2-4 pts. wt. cortex dictamni, 3-6 pts. wt. sweet wormwood and 3-5 pts. wt. golden cypress.    USE - Chinese herbal medicine biological foliar fertilizer used for preventing crop diseases, and repelling insects, pests and worms.    DETAILED DESCRIPTION - Chinese herbal medicine biological foliar fertilizer comprises 5-8 pts. wt. dyers woad leaf, 3-4 pts. wt. dandelion, 2-5 pts. wt. blackberry lily, 3-4 pts. wt. radix isatidis, 3-5 pts. wt. honeysuckle, 1-2 pts. wt. tuckahoe, 1-2 pts. wt. Polygonum cuspidatum, 2-3 pts. wt. radix stemonae, 2-3 pts. wt. betelnut, 3-4 pts. wt. Chinaberry fruit, 2-3 pts. wt. quisqualis, 5-6 pts. wt. hairyvein agrimony, 1-2 pts. wt. radix sophorae flavescentis, 1-3 pts. wt. Pseudolarix, 2-4 pts. wt. cortex dictamni, 3-6 pts. wt. sweet wormwood, 3-5 pts. wt. golden cypress, 1-2 pts. wt. Carpesium abrolanoides and 2-3 pts. wt. Chinaberry bark. An INDEPENDENT CLAIM is included for preparation of Chinese herbal medicine biological foliar fertilizer comprising dissolving sodium silicate in boiling water, adding potassium hydroxide, dissolving, adding 300-400 g/L Chinese herbal medicine and water, mixing, hydrolyzing at 90-100 degrees C for 6 hours, filtering, and adding copper, iron, zinc, manganese, molybdenum, boron and 20-25 pts. wt. EDTA solution.
NOVELTY - Usage method of blast furnace dust and electric field dust-removal ash at sinter head involves mixing blast furnace dust and electric field dust-removal ash, sintering, reducing, recycling iron-containing material, separating gaseous mixture comprising zinc, potassium and lead oxide, dissolving, adding sodium sulfide, centrifuging, adding sodium carbonate, centrifuging, evaporating, crystallizing, separating precipitate, obtaining lead slag, filtering remainder product, smelting, separating zinc material, processing resultant crude and recycling potassium chloride as fertilizer.    USE - Usage method of blast furnace dust and electric field dust-removal ash at sinter head (claimed).    ADVANTAGE - The method enables usage of blast furnace dust and electric field dust-removal ash at sinter head by environmentally-friendly process with reduced energy consumption.    DETAILED DESCRIPTION - Usage method of blast furnace dust and electric field dust-removal ash at sinter head involves mixing blast furnace dust and electric field dust-removal ash at sinter head, sintering in rotary kiln, reducing volatile content, recycling iron-containing material, separating gaseous mixture comprising zinc, potassium and lead oxide, collecting using rotary kiln de-dusting system, dissolving resultant material, adding sodium sulfide, centrifuging, adding sodium carbonate, centrifuging, evaporating, crystallizing, separating precipitate, obtaining lead slag, filtering remainder product, smelting, separating zinc material, evaporating resultant crude, crystallizing potassium chloride, recycling potassium chloride as fertilizer, separating resultant residue and dissolving in mother liquor.
NOVELTY - Cultivating three years persistent pseudoginseng during seedling stage comprises applying fertilizer in pseudoginseng as a winter topdressing during the 12th month of growth and applying 10% fertilizer in the pseudoginseng seedling emergence stage.    USE - The method is useful for cultivating three years persistent pseudoginseng during seedling stage (claimed).    ADVANTAGE - The method increases pseudoginseng seedling survival rate.
NOVELTY - Organic fertilizer comprises 1-5 parts mass nutritional solution, 20-25 parts mass organic materials, 70-75 parts mass water conserving medium and 3-5 parts mass antimicrobial agent.    USE - The organic fertilizer is useful in remediation of lead-zinc ore polluted soil (claimed).    ADVANTAGE - The organic fertilizer has water retention capacity, improves soil fertility, eliminates soil toxicity, and strengthens phytoremediation ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic fertilizer which involves mixing nutritional solution, organic materials, and water conserving medium, adding the antimicrobial agent to the mixture, and fermenting the mixture at 30 degrees C for 15 days.
NOVELTY - Preparation of 5-substituted-2,4-di(methylthio)pyrimidine compounds (I)-(III) involves reacting 5-bromo-2,4-dichloropyrimidine with sodium thiomethoxide to produce 5-bromo-2,4-di(methylthio)pyrimidine (IV), reacting compound (IV) with butyl lithium at low temperature under nitrogen and reacting with trimethyl borate, N,N-dimethylformamide or solid carbon dioxide, adjusting the pH to 3-4 with dilute hydrochloric acid, extracting with an organic solvent, separating or filtering, drying and concentrating.    USE - Compounds (I)-(III) are used as pharmaceutical and pesticide intermediates.    ADVANTAGE - The method enables simple preparation of compounds (I)-(III) with high yield, purity and reaction selectivity in an environmentally-friendly manner.    DETAILED DESCRIPTION - Preparation of 5-substituted-2,4-di(methylthio)pyrimidine compounds of formula (I)-(III) involves reacting 5-bromo-2,4-dichloropyrimidine with sodium methanethiolate to produce 5-bromo-2,4-di(methylthio)pyrimidine of formula (IV), reacting compound (IV) with butyl lithium at low temperature under nitrogen, reacting the obtained compound with trimethyl borate, N,N-dimethylformamide or solid carbon dioxide, adjusting the pH to 3-4 with dilute hydrochloric acid, extracting with an organic solvent, separating or filtering, drying and concentrating to produce 2,4-di(methylthio)pyrimidine-5-boronic acid (I), 2,4-di(thiomethyl)pyrimidine-5-carboxaldehyde (II) and 2,4-di(thiomethyl)pyrimidine-5-carboxylic acid (III), respectively.
NOVELTY - Preparing organic fertilizer involves mixing organic waste matter, conditioning it, and then composting. The product is fermented and trace element is added to increase nitrogen through high voltage electric shock. High voltage electric shock is performed with conditions of relative humidity (60-85%) and compost moisture content (40-50%).    USE - Method for preparing organic fertilizer for planting fruit and vegetable in greenhouses (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer in a simple, efficient and eco-friendly manner. The organic fertilizer ensures uniform fertility, and do not burn seedlings.
NOVELTY - Electrochemical cell (1) comprises a proton conducting electrolyte (3) made of aluminosilicate, sandwiched between a porous metal anode (2) and an electronically conductive porous cathode (4).    USE - The electrochemical cell is useful in electrolysis of liquid water or vapor for reduction of oxidized compounds, for production of hydrogen and/or oxidation of reduced compounds (all claimed).    ADVANTAGE - The electrochemical cell: is simple and economical; and can be operated at 100-400 degrees C, thus limiting the corrosion of electrodes.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) manufacturing the electrochemical cell, comprising at least the steps of manufacturing aluminosilicate-based proton conducting electrolyte, depositing the electrolyte on the porous metal anode by a hydrothermal method, and depositing the electrically conductive porous cathode on the electrolyte to form the electrochemical cell; and    (2) use of the electrochemical cell for the reduction of oxidized compounds, such as oxidized compounds containing e.g. carbon dioxide by reactive chemical species formed by electrolysis of water, where the reduction is carried out in the cathode compartment at 100-400 degrees C, for the production of hydrogen in the cathode compartment and/or for the oxidation of reduced compounds in the anode compartment.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic sectional view of the electrochemical cell.    Electrochemical cell (1)    Anode (2)    Proton conducting electrolyte (3)    Cathode (4)    Generator (5)
NOVELTY - The hydrogen generator has an electrolyte reservoir that is provided to obtain the mixture containing hydrogen and oxygen, and in which water and electrolyzer (E) are formed. A central electrode (7) is provided with anode profile and cathode profile. An outer electrode (2) is located between the plastic housing (1) and top carrier (4). The neutral electrodes (6-1-6-6) are provided with the electrolyzer.    USE - Hydrogen generator.    ADVANTAGE - The high rate of energy on the small area with the large surface electrodes is obtained. The back burning occurred in the electrolyte reservoir is prevented. The exhaust emission substances and fuel consumption are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the hydrogen generator.    Plastic housing (1)    Outer electrode (2)    Top carrier (4)    Neutral electrodes (6-1-6-6)    Central electrode (7)    Electrolyzer (E)
NOVELTY - The system (1) has a hydrolyzing unit which decomposes electrolyte solution using sunlight energy has pair of electrode. An optical semiconductor catalyst is supported by side in pair of electrode. The sunlight energy is irradiated to optical semiconductor catalyst. A moisture-content replenishment unit replenishes the electrolyte solution of hydrolyzing unit with generated water produced by fuel cell using the hydrogen produced by disassembly of electrolyte solution.    USE - Sunlight replenishment system.    ADVANTAGE - The generated water of fuel cell is returned to hydrolyzing apparatus, such that the need of supplying water from exterior unit is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the sunlight utilization system. (Drawing includes non-English language text)    Sunlight replenishment system (1)    Water gauge (50)    Sunshine measure (60)    Gas utilization apparatus (70)    Control circuit (80)
NOVELTY - The method involves refrigerating air to near cryogenic temperatures by contacting the air with cryogenic fluid and distributing the air to a space (A) by a distributor pipe (5) at near cryogenic temperatures. The space is in or attached to a vehicle, where the vehicle transports goods in need of refrigeration. The air is fed to the space by a device selected from a group consisting of a pump and a blower (D), where the distributor pipe contains distribution nozzles, holes and openings.    USE - Method for providing refrigeration to a space to be refrigerated by contacting air with cryogenic fluid such as liquid nitrogen, liquefied natural gas and liquid air (all claimed).    ADVANTAGE - The method enables providing near cryogenic air as a heat transfer medium, thus reducing size and power required to operate an air blower to circulate the air through the refrigerated space. The method enables providing electrical sources for enabling easy battery backup in event of loss of primary power while pneumatic sources can be operated by warmed high pressure nitrogen gas that is exhausted from the refrigerated space. The method enables permitting simplified and flexible operation of the two cryogenic heat exchangers by an air heat transfer medium so as to improve temperature uniformity and control options for refrigeration spaces and associated differing temperatures.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for providing refrigeration to a space.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an arrangement of a heat exchange system for in-transit refrigeration.    Space (A)    Heat exchangers (B, C)    Blower (D)    Lines (1-4)    Distributor pipe (5)
NOVELTY - A methanol gasoline lubricating agent is obtained by mixing 30 %mass liquid paraffin, 30 %mass silicone oil, 20 %mass lubricating oil, 20 %mass octanol.    USE - Lubricating agent is used for methanol gasoline (claimed) used in vehicle.    ADVANTAGE - The vehicle using the methanol gasoline provided with the lubricating agent has excellent anti-swelling property with respect to fuel pump, fuel injector and cylindrical piston.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage method of methanol gasoline lubricating agent, which involves mixing methanol gasoline lubricating agent and methanol gasoline in mass ratio of 1:99.
NOVELTY - Preparation of silver nanoparticles comprises respectively providing silver nitrate (AgNO3) solution and colorless aqueous extract of Pimpinella anisum seeds, and combining AgNO3 solution with P. anisum seed extract.    USE - Method for preparing silver nanoparticles (claimed) used in food, medicine, clothing, sunscreen and cosmetics.    ADVANTAGE - The method is simple, cost-effective, environment-friendly and suitable for large scale production; does not require toxic chemical solvents; and has low energy consumption. The silver nanoparticles have size of 3.2-16 nm, preferably 8 nm, high antimicrobial properties and high dispersibility; and are easier to handle because they are less susceptible to aggregation than silver nanoparticles prepared using other methods.
NOVELTY - Use of biomass-derived authentic domestic fuel in major electric power company and fuel-supply section, is claimed.    USE - Use of biomass-derived authentic domestic fuel in major electric power company and fuel-supply section, and electric power generation in hybrid electric vehicle (claimed).    ADVANTAGE - The biomass-derived authentic domestic fuel enables stable supply of electric power which is not influenced by weather. The hybrid electric vehicle using the biomass-derived authentic domestic fuel is safe.
NOVELTY - A soil improvement material comprises an organic soil improvement material containing sludge and charcoal component as an essential component.    USE - Soil improvement material is used in cultivation of plants e.g. sunflower, cucumber, and eggplant.    ADVANTAGE - The soil improvement material has excellent soil improvement effect and growth promotion effect with respect to plants, without losing a fertilizer component.
NOVELTY - A gas-adsorption material comprises carbon fiber aggregate formed by aggregating carbon fiber. The mean density of the carbon fiber aggregate is 0.2-1 g/cm3. The gas adsorption amount per unit volume at a gas pressure of 1 MPa is 50 mL/cm3 or more.    USE - Gas-adsorption material used in gas storage tank (claimed) e.g. low pressure adsorbed natural gas methane storage tank in methane fermentation system, fuel tank of adsorbed natural gas methane motor vehicle, domestic cylinder for storing propane, and tank for storage of hydrocarbon gas e.g. methane, ethane and butane, and carbon dioxide, hydrogen, nitrogen and nitrogen oxide.    ADVANTAGE - The gas-adsorption material has high gas-adsorption ability by containing carbon fiber aggregate of high density.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of gas adsorption material, which involves preparing (S10) and aggregating (S20) carbon fiber to obtain the carbon fiber aggregate, and increasing (S30) the density of the carbon fiber aggregate by adding and shaking a polar solvent to the carbon fiber; and    (2) gas storage tank, which has a container filled with the gas-adsorption material.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of manufacture of the gas-adsorption material. (Drawing includes non-English language text)    Carbon fiber preparation process (S10)    Carbon fiber aggregation process (S20)    Density increasing process (S30)
NOVELTY - Production of biodiesel involves adding lipid, lower alcohol and sulfonated graphene in mass ratio of 1:0.1-2:0.05-0.2 to three-necked flask, heating, refluxing for 3-15 hours, filtering, separating catalyst from reaction mixture, subjecting filtrate to liquid separation, separating lower glycerol layer, adding 5-10 %mass sodium bicarbonate to upper layer, washing, drying using magnesium sulfate for 4-10 hours and evaporating at reduced pressure. The lipid is vegetable oil, animal fat or waste oil. The lower alcohol is chosen from methanol, ethanol, propanol and butanol.    USE - Production of biodiesel (claimed).    ADVANTAGE - The method enables production of biodiesel with high yield, within short period of time, by environmentally-friendly process.
NOVELTY - One of biomass gas gasification furnace, comprising a feeding port, cracking gas outlet, gasification furnace heat preservation layer, heat cracking chamber, a carbon chamber, gas in furnace arrange carbon port, rotating grate equal part. Wherein feeding hole and arrange carbon set with fast opened sealing furnace cover, suitable feedstock and , and the leak tightness of the furnace body. Cracking gas outlet pipe set with spherical valve, and close the furnace body discharging cracking gas and suitable, heat cracking chamber at lower part of gasification furnace, pouring present cone body shape, and is set with carbon furnace, rotary grate in furnace carbon outlet is set with the heat cracking indoor positive middle, lower driving rotating action on motor peristaltic promoting arrange carbon. The device is especially suitable for application in all kinds of biomass thermal cracking process, cracking gas conversion rate high, and can joint no pollute.
NOVELTY - This new utility model claims of one of air flow bed gasification biomass synthesis gas for preparing small test device. Nitrogen bottle through nitrogen mass flow controller, a pneumatic feeder connected to air flow bed gasification furnace, oxygen bottle through mass flow controller after oxygen and nitrogen bottle connected with one level pre-heater, a one level pre-heater and water steam generator connected with three-way pipe valve, three-way pipe valve connected with second level pre-heater, second level pre-heater connected to air flow bed gasification furnace, the bottom installed with chilling water, the outlet gas through cyclone separator, a condenser air flow bed gasification furnace bottom, upper filter connected to air pump, air extracting pump connected with online coal analyzer; air flow bed gasification furnace installed with thermocouple and pressure meter. This new utility model device comprises reaction temperature high, efficient conversion, synthesis gas and little ash content, tar content at least equal, can meet biomass air flow bed gasification test research.
NOVELTY - The utility model claims a new use for a biomass gasification combustion supply heat system of industrial kiln furnace, comprising: furnace smoke gas outlet and equipped with entrance combustion, a pyrolyzer and heating equipped with a pyrolysis gas outlet and material outlet, a heating entrance connected with kiln furnace and a smoke gas outlet, a gasification furnace comprising a reaction zone, gas outlet material outlet, a gasification furnace and a pyrolysis gas outlet by pipeline way to a cell, material entrance of the gasification furnace through pipeline connected with the way the pyrolyzer to combustion entrance, and a kiln furnace heat exchanger, said heat exchanger comprises a connected high temperature of entrance, low temperature outlet, and connected a low temperature of entrance, exit, the entrance connected with high temperature furnace and kiln gas outlet, the high temperature outlet through pipeline way to a cell a. The system increase a heat use efficiency, a biomass fuel gas a steady efficient supply heat for industrial kiln. The utility model can applied to a biomass fuel gas kiln furnace to supply heat.
NOVELTY - Special coatings production involves performing partial or full carbonization of commercial pure glycerin byproduct of biodiesel with or without pre-treatment or glycerin derived from any source or modified glycerin at 100-1000 degrees C in presence of catalyst. The formed coating is deposited on a support.    USE - Method for producing special coatings on different substrates.    ADVANTAGE - The method produces the special coatings in a simple manner with controlled surface area, porosity, and hydrophobicity without requiring any additional process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic photograph of deposits of material with undefined forms on the surface of vermiculite clay.
NOVELTY - Preparation of a 3-7 carbons alcohol, comprises preparing a beta-lactone (I) and hydrogenating (I) to form the 3-7 carbons alcohol.    USE - The process is useful for preparing 3-7 carbons alcohol, which is useful in a fuel composition (claimed).    ADVANTAGE - The process produces 3-7 carbons alcohol has significantly higher calorific values close to gasoline.    DETAILED DESCRIPTION - Preparation of a 3-7 carbons alcohol, comprises preparing a beta-lactone of formula (I) and hydrogenating (I) to form the 3-7 carbons alcohol.    R3 = H or 1-2C alkyl; either    R4 = H; and    R5 = H or 1-2C alkyl; or    R4R5 = ethylidene or methylidene.    INDEPENDENT CLAIMS are also included for:    (1) process (A) for preparation of propanol and/or butanol, comprising (a) carbonylation of methanol or ethanol to form acetic acid or propanoic acid, respectively, and (b) reduction of acetic acid or propanoic acid to form ethanol or propanol, respectively, (c) carbonylation of ethanol or propanol to form propanoic acid or butanoic acid, respectively, or carbonylation of a mixture of ethanol and propanol to form a mixture of propionic acid and butyric acid, and (d) reduction of butanoic acid to form butanol and optionally (e) hydrogenating a mixture of propionic acid and butyric acid to form a mixture of propanol and butanol; and    (2) a fuel composition comprising the alkane compounds prepared by the process (A).
NOVELTY - Device comprises a mobile container (1), which has a pressure container for receiving the biomass and which is enclosed by several wall elements (2-8), which are disengageable rotatably or in at least one direction of thrust from a transport position to at least one axis of rotation, and an increased volume relative to the transport position is enclosed in an operating position achievable by twisting or disengagement.    USE - The device is useful for location-independent treatment of biomass (claimed).    ADVANTAGE - The device provides largest possible variability and adaptability, together with a large mobility.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a mobile container.    Mobile container (1)    Wall element (2)    Connecting piece (9)
NOVELTY - The method involves detecting carbon dioxide (CO), methane, carbon monoxide and hydrogen content in water by a hydrogen analyzer. The hydrogen analyzer is connected with a sampling pipe, a follow-up pipe and a turn-off valve. The follow-up pipe is closed for 40s by the turn-off valve when the hydrogen content of the hydrogen analyzer reaches an alarm value. The hydrogen analyzer is provided with a platform that is connected with a circuit. The alarm value of the hydrogen analyzer is about 1000Vppm.    USE - Method for increasing production detecting speed of hydrogen and carbon monoxide in a hydrogen analysis device.    ADVANTAGE - The method enables improving air supply period to ensure approval of carbon oxide production client requirement.
NOVELTY - The aqua fuel kit has a container, an electrolyte solution, and metal electrodes (103). The container is made of ceramic material, and has two chambers for the formation of hydrogen gas and oxygen gas separately. The top portion of the container is provided with eight holes for the insertion of six rods and two holes for exhaust gas. The electrolyte solution contains water solution and potassium hydroxide in the ratio of 4:1.    USE - Aqua fuel kit for hydrogen-oxygen gas generator.    ADVANTAGE - The aqua fuel kit eliminates the use of a separate unit, which is required to separate the hydrogen gas and oxygen gas from a gaseous mixture of hydrogen and oxygen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the front view of the hydrogen-oxygen gas generator without the bottom base cover.    Separating block (101)    Washers (102)    Rods (103)
NOVELTY - An aqueous stamping ink contains 20-30 pts. wt. polymethacrylate resin, 10-20 pts. wt. cellulose acetate resin, 1-5 pts. wt. silver nitrate, 2-8 pts. wt. pigment, 1-10 pts. wt. diethanolamine, 3-7 pts. wt. aqueous wetting agent, 2-8 pts. wt. antifoaming agent, 1-6 pts. wt. thickening agent, and 25-35 pts. wt. deionized water.    USE - Aqueous stamping ink is useful in food and pharmaceutical packaging applications.    ADVANTAGE - The aqueous stamping ink has excellent adhesion, weather resistance, gloss and color retention properties, and is environmentally-friendly.
NOVELTY - The generator has a combustion chamber (33) that is provided between a wind cap (15) and a fire grate (11) whose bottom surface is set with an ash chamber (9). A bottom portion of a reaction chamber (6) is provided with a fuel gas outlet (3) and a middle portion of left wall of chamber is set with an exhaust gas pipe (31) which is connected with an air pipe (28). The left wall of ash chamber is connected with an air inlet motor (27). A bottom end of a main box (21) is set with discharging port connected with a feedstock pipe (23) which is located in upper end of reaction chamber.    USE - Biomass fuel gas generator.    ADVANTAGE - Ignition of gas generator is easy, quick, adjustable and stable.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass fuel gas generator.    Fuel gas outlet (3)    Reaction chamber (6)    Ash chamber (9)    Fire grate (11)    Wind cap (15)    Main box (21)    Feedstock pipe (23)    Air inlet motor (27)    Air pipe (28)    Exhaust gas pipe (31)    Combustion chamber (33)
NOVELTY - A low-methanol diesel contains diesel, methanol, biodiesel, oleic acid, ethyl acetate, methyl tert-butyl ether, emulsifier (I), emulsifier (II) and additive. The diesel is No. 0 diesel or Fischer-Tropsch diesel. The emulsifier (I) is Span 80 (RTM: Sorbitan monooleate). The emulsifier (II) is fatty alcohol ethoxylate or nonylphenol ethoxylate. The additive comprises octanol, isooctanol, isoamyl alcohol, cyclohexanone, isobutanol, acetic acid and/or amyl acetate.    USE - Low-methanol diesel (claimed).    ADVANTAGE - The low-methanol diesel can be prepared in an economical manner with excellent transparency and stability and reduced emission of harmful substances, does not damage engine, improves service life of engine, and is non-hierarchical.    DETAILED DESCRIPTION - A low-methanol diesel contains 65-90 pts. wt. diesel, 5-20 pts. wt. methanol, 0.5-2 pts. wt. biodiesel, 0.5-5 pts. wt. oleic acid, 0.5-1 pt. wt. ethyl acetate, 0.5-1 pt. wt. methyl tert-butyl ether, 0.2-0.8 pt. wt. emulsifier (I), 0.2-1 pt. wt. emulsifier (II) and 2-8 pts. wt. additive. The diesel is No. 0 diesel or Fischer-Tropsch diesel. The emulsifier (I) is Span 80 (RTM: Sorbitan monooleate). The emulsifier (II) is fatty alcohol ethoxylate or nonylphenol ethoxylate. The additive comprises octanol, isooctanol, isoamyl alcohol, cyclohexanone, isobutanol, acetic acid and/or amyl acetate. An INDEPENDENT CLAIM is included for preparation of low-methanol diesel, which involves adding methanol to diesel, uniformly oscillating at room temperature, adding emulsifier (I) and emulsifier (II) to mixture, evenly shaking to form emulsion, then adding oleic acid, uniformly oscillating until oleic acid is completely dissolved, followed by adding biodiesel, ethyl acetate and methyl tert-butyl ether, evenly shaking, adding additives to mixture and stirring at 500-800 rpm for 10-20 minutes.
NOVELTY - A bismuth tungstate photocatalytic nano thin film consists of a nano sheet and a layer grown on a fluorine-doped tin oxide electroconductive glass in vertical direction.    USE - Preparation of bismuth tungstate photocatalytic nano thin film for use in photoelectrochemical hydrogen production by water electrolysis (claimed).    ADVANTAGE - The method enables simple, quick and controllable preparation of bismuth tungstate photocatalytic nano thin films having large specific surface area and excellent visible-light photocatalytic activity, under mild reaction conditions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of bismuth tungstate photocatalytic nano thin film, which involves adding potassium iodide powder and bismuth nitrate powder to deionized water, adjusting pH to obtain 0.02-0.06 moL/L solution, adjusting pH of obtain bismuth iodate solution to 1.5-1.9, carrying out cathode electrodeposition using fluorine-doped tin oxide electroconductive glass as working electrode, platinum electrode as counter electrode, and silver/silver chloride electrode as reference electrode for 1-30 minutes at -0.2 V to -0.05 V to form a bismuth iodate nano thin film, adding deionized water to sodium tungstate powder to obtain 0.05-0.2 moL/L sodium tungstate aqueous solution, adding the solution and glass nano thin film to a crystallization kettle, carrying out hydrothermal ion-exchange for 2-12 hours at 100-140 degrees C, baking for 1-3 hours in air at 500-600 degrees C; and    (2) usage method of bismuth tungstate photocatalytic nano thin film in photoelectrochemical hydrogen production by water electrolysis.
NOVELTY - The utility model belongs to the biogas production device area, especially relates to a solar marsh gas device, comprising a marsh gas tank and a solar energy water heater, each marsh gas tank of top part is opening, a marsh gas tank is set with circulation water pipe, a circulation water entrance pipe through water inlet main pipe connected with solar energy water heater water outlet, a water inlet pipe is set with water pump, circulation water pipe is connected with a water outlet pipe, a water outlet pipe connected with solar energy water heater, marsh gas tank is set with enter is ball shell structure, and is of a split type, provided with a tank port is set with a feedstock tube, a feedstock are connected with feedstock. The marsh gas generating device a reasonable, connecting is simple, material enter, using the gas and water circulation, a can increase production efficiency, reduce cost and production process.
NOVELTY - The utility model relates to a new waste of a fermentation chamber, comprising a sealing chamber, a sealing chamber are divided the three middle layer, sealing a layer of chamber for fermentation layer, provided with a opening upwards and enter a port for pouring waste and a the ferment layer on one side, used for a fermentation layer by heating the fermentation layer and a fermentation layer and then is heating layer, a heating layer, a ferment layer is clapboard between the marsh gas layer, layer fermented marsh gas layer and formed with a hole used for marsh gas by marsh gas layer. Can effectively using waste and a collecting get up by ferment, they produce a gas used for the normal life and production, a heating layer can make the waste and placing in a fermentation layer in a fermentation to generate marsh gas would rising to a marsh gas layer, at the same time with energy saving environmental protection,.. character equal.
NOVELTY - The utility model claims organic material biogas fermentation device, comprising Anaerobic digestion pool, wherein the upper cover of Anaerobic digestion pool with arc of light shed, cover with transparent insulating film to open in the Anaerobic digestion pool, bottom of Anaerobic digestion. laying a arrange marsh gas with a relux, a relux a gap provided with a marsh gas of the marsh gas nozzle, the arrange a marsh gas relux a gathering pipe connected with a marsh gas output pipe, provided with a water circulation pipeline on the inner wall upper part of Anaerobic digestion marsh liquid pool, a water circulation pipeline by a valve connected with boiler; the Anaerobic digestion pool feedstock pipe connected with a pre-processing pool, a pool edge provided with feeding machine, Anaerobic digestion pool matched with biogas liquid pump, liquid pump through pipeline connected with a pressure tank, a liquid outlet port and a pressure tank connected pre-processing pool. And the present technique compared to the organic material biogas ferment device by a temperature a small, low energy consumption, high yield, a suitable, suitable for large-scale popularization and application.
NOVELTY - The utility model claims a... biogas slurry anti-sediment sleeve AO degradation device matched aerobic degradation pool, it by aerobic degradation pool body (1), an aeration pipe (2), a relux pump (3), an aeration pump (4) make up of a device designed for multistage aerobic fermentation degradation are, before aerobic fermentation in a set up with aeration device, the aeration device too. According to different design and installation site internal in aerobic ferment finish a suction, aeration device can use microorganism strain and full contact biogas fermentation, back end is set with the relux pump can make a microorganism strain relux circulation cultivation, can get in reducing quantity of microorganism strain.
NOVELTY - The utility model claims a device for linear marsh gas fermentation system to promote uniform strain distribution, wherein it comprises a feedstock tube, a discharging tube, a pipe ferment, wherein the ferment pipe is straight pipe, pipe respectively connected with fermentation feedstock tube and discharge tube with two end side, between installed on fermentation pipe top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, pipeline and fermentation feedstock a position feedstock with a plate, fermented pipe and discharging pipe connecting seat to set with a discharging blocking plate, a fermentation pipeline also is set with multi-number between the feedstock has a blocking plate and a blocking plate and a discharging plate, the space between the adjacent blocking plate forming one of fermentation area, a top of a fermentation zone connected with gas-guide tube, the gas-guide pipe is set with a valve with a biogas circulation stirring a strong flow, a biogas liquid flow stirring to promote uniform distribution of strain, and promote the fermentation raw material into a fermentation system, It increase the fermentation system and system.
NOVELTY - The utility model claims a marsh gas ferment system of one-way flow promoting feedstock, wherein it comprises a feedstock tube, a discharging tube and a pipe ferment, wherein the ferment pipe is straight pipe, pipe respectively connected with fermentation feedstock tube and discharge tube with two end side, between installed on fermentation pipe top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, pipeline and fermentation feedstock a position feedstock with a plate, fermented pipe and discharging pipe connecting seat to set with a discharging blocking plate, a fermentation pipeline also is set with multi-number between the feedstock has a blocking plate and a blocking plate and a discharging plate, the space between the adjacent blocking plate forming one of fermentation area, a top of a fermentation zone... connected with gas-guide tube, the gas-guide pipe is set with a valve with a biogas circulation stirring a strong flow, a biogas liquid flow stirring to promote uniform distribution of strain, and promote the fermentation raw material into a fermentation system. It increases the fermentation system and system.
NOVELTY - The utility model claims a new type burdock marsh gas generating system to promote relux stir the biogas device, wherein comprising: a feedstock, a discharge pipe, a fermentation pipe, a fermentation level pipe set, a feedstock material and a vertical U-type fermentation pipeline connected with a terminal a, a fermentation pipe of a hydraulic part, a feedstock tube connecting seat for feedstock a drainage hole, a discharging pipe and a position for discharging a drainage hole, a pipeline and fermentation feedstock pipe connecting seat is set with a feedstock to a baffle, a fermentation pipe and discharging pipe connecting seat is set with a discharging pipe to plate, discharging tube between blocking board and a feedstock-blocking plate is set with at least a one with a plate, a disc feeding/discharging pipe and between adjacent blocking plate or between the adjacent blocking plate forming one of fermentation area, top part of each fermentation area is set with two independent with the gas collecting pipe, each fermentation area of top part and connecting with the independent gas collecting pipe, a gas collecting tube is set with with a valve, a U-shaped channel type fermentation device. Fermentation line a, a water pressure and a one-way valve and a, biogas slurry realize full flow within a system, and a uniform distribution of strain, a preventing crust, high yield, suitable for large scale production.
NOVELTY - The utility model claims a new type multi-cell fermentation bend beyond the high efficient methane generating system, wherein comprising: a feedstock, a discharge pipe, a fermentation pipe, a fermentation level pipe set, a feedstock material and a vertical U-type fermentation pipeline connected with a terminal a, a fermentation pipe of a hydraulic part, a feedstock tube connecting seat for feedstock a drainage hole, a discharging pipe and a position for discharging a drainage hole, a pipeline and fermentation feedstock pipe connecting seat is set with a feedstock to a baffle, a fermentation pipe and discharging pipe connecting seat is set with a discharging pipe to plate, discharging tube between blocking board and a feedstock-blocking plate is set with at least a one with a plate, a disc feeding/discharging pipe and between adjacent blocking plate or between the adjacent blocking plate forming one of fermentation area, top part of each fermentation area is set with two independent with the gas collecting pipe, each fermentation area of top part and connecting with the independent gas collecting pipe, a gas collecting tube is set with with a valve, a U-shaped channel type fermentation device and fermentation line a. .... a a and one-way valve, biogas slurry realize full flow within a system, and a uniform distribution of strain, a preventing crust, high yield, suitable for large scale production.
NOVELTY - The utility model claims a new type burdock beyond efficient marsh gas ferment system, wherein comprising: a feedstock, a discharge pipe, a fermentation pipe, a fermentation level pipe set, a feedstock material and a vertical U-type fermentation pipeline connected with a terminal a, a fermentation pipe of a hydraulic part, a feedstock tube connecting seat for feedstock a drainage hole, a discharging pipe and a position for discharging a drainage hole, a pipeline and fermentation feedstock pipe connecting seat is set with a feedstock to a baffle, a fermentation pipe and discharging pipe connecting seat is set with a discharging pipe to plate, discharging tube between blocking board and a feedstock-blocking plate is set with at least a one with a plate, a disc feeding/discharging pipe and between adjacent blocking plate or between the adjacent blocking plate forming one of fermentation area, top part of each fermentation area is set with two independent with the gas collecting pipe, each fermentation area of top part and connecting with the independent gas collecting pipe, a gas collecting tube is set with with a valve, a U-shaped channel type fermentation device and fermentation line...... a and a one-way valve. Biogas slurry realize full flow within a system, and a uniform distribution of strain, a preventing crust, high yield, suitable for large scale production.
NOVELTY - The utility model claims a Anaerobic biological treatment technology area, especially relates to a kind of a. Anaerobic fermentation biogas experiment device of continuous feedstock. The a continuous feedstock. Anaerobic fermentation biogas experiment device comprises continuous a feedstock, Anaerobic reaction unit and methane collecting unit; the Anaerobic a continuous feedstock a pipeline connected with, the other end a pipe and a marsh gas collecting unit... Anaerobic reflecting unit. Anaerobic reactor,.. Anaerobic reactor set with insulating layer. The utility model is a model of a continuous supply of feedstock Anaerobic fermentation biogas experiment device via the connection of the third element, and Anaerobic fermentation of biogas is set with insulating layer, the utility model is a new type provide a continuous feedstock and the experiment device realize continuous feedstock and mixing full, at the same time can increase production rate, has a simple structure, a suitable equal.
NOVELTY - The method involves arranging a porous material i.e. meso-porous material, in a reaction channel. Diameter of the porous material is maintained in a nanometer level. A pressurizing process is performed for purifying mixed gas after filling the mixed gas into an inside of the reaction channel. The mixed gas is mixed with water solution. A reaction process is performed for maintaining water content in the reaction channel at a preset range. A de-composing process is performed in the reaction channel for obtaining to-be separated gas.    USE - Porous material i.e. meso-porous material, based gas separation method.    ADVANTAGE - The method enables improving gas-water contact area, aquo-complex generation speed and gas separation factor.    DETAILED DESCRIPTION - The to-be separated gas is selected from methane, ethane, ethylene, propane, isobutane, n-butane, nitrogen, carbon dioxide, hydrogen vulcanization or hydrogen. An INDEPENDENT CLAIM is also included for a porous material based gas separation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a porous material based gas separation method.
NOVELTY - A neutral or cationic mononuclear ruthenium divalent complex (I), is new.    USE - New neutral or cationic mononuclear ruthenium divalent complex is used as catalyst for hydrogenation, hydrosilylation and reductive reaction of carbonyl compound for manufacturing alkane, amine and alcohol compound (all claimed).    ADVANTAGE - The neutral or cationic mononuclear ruthenium divalent complex provides catalyst having excellent catalytic activity, and temperature and pressure tolerance. The hydrogenation reaction is carried out using catalyst at room temperature under mild reaction conditions.    DETAILED DESCRIPTION - A neutral or cationic mononuclear ruthenium divalent complex of formula (I), is new.    R1-R6=H, or alkyl, aryl, aralkyl, organosilyl, monoorganosilyl amino, diorganosilyl amino, monoorganophosphinyl, diorganophosphinyl, monoorganosilyl, diorganosilyl, or triorganosilyl (all optionally substituted by X);    X=halo, organosilyl, monoorganosilylamino, diorganovinylsiloxy or organothio;    L=2-electron ligand other than thiourea ligand and CO;and    m=3 or 4.    INDEPENDENT CLAIMS are included for the following:    (1) catalyst, which consists of mononuclear ruthenium complex (I);    (2) manufacture of addition compound, which involves performing hydrosilylation reaction of compound having aliphatic unsaturated bond in presence of catalyst, and organohydropolysiloxane or hydrosilane having silicon-hydrogen bond;    (3) manufacture of alkane compound, which involves hydrogenating compound having aliphatic unsaturated bond in presence of catalyst;    (4) manufacture of amine compound, which involves reducing organohydropolysiloxane or hydrosilane having silicon-hydrogen bond in presence of catalyst; and    (5) manufacture of alcohol compound, which involves reducing aldehyde compound, ketone compound, or ester compound with hydrosilane or organohydropolysiloxane in presence of catalyst.
NOVELTY - The new type utility claims have one kind MBR integrated sewage treatment device, comprising in turn connected with the MBR reaction pool, in the MBR film pool and device, the MBR reaction pool comprises connected in series connected with the biological pool and biologic O pool A, in the A pool with Anaerobic biological fungus, bottom set with air diffusion device, in O pool provided with biologic filler, upper filler set with aerobic bacteria, bottom set with air diffusion device; in the MBR film pool provided with film holder, upper film holder provided with an MBR reaction film, in device inside set with fan and suction pump, a fan through pipeline and air diffusion device connected with the suction pump by pipe and MBR reaction film connection. The device by film separation technology and biological technology organic combined to sewage processing process, device structure is compact, small volume, small square meter small, organic pollutant removing rate high, stable water quality.
NOVELTY - The new type utility claims have one plant sewage treatment pipeline blocking device, comprising a rope, iron hook, an iron,, mesh, a cylindrical shell, one end of rope is connected with iron hook, iron hook hooks the iron ring, is of inverted water drop, fine mouth tail part connected with mesh, the iron ring will mesh together with iron fine wherein the tail end fixing part, and provided with a cylindrical grid shell. And the iron hook can be open, woven bag and rope. And the cylindrical shell comprises inner cylinder and external ring, inner cylinder and external ring separated between one of the cylinder inner wall, external ring side surrounds the inner cylinder, inner cylinder and external ring of soluble material is covered and set with bacteria. The cylindrical shell is high as 23 cm to 41 cm, the diameter is about 5 cm to 13 cm. The utility model is new type structure is simple, suitable operation, can effective eliminate sewage of pipeline or pump station lipid equal organic matter, prolong the supplementary bacteria at the same time period.
NOVELTY - The new type utility claims one kind have made hydrogen tail sum recovery using device, comprising coal, coke furnace gas co-produced production device, sum fuel benzene removing device, made hydrogen production device and coke furnace, the coke furnace through pipe connected coal gas cabinet, cabinet through coal transport pipe connected with can for coke furnace is coke furnace coal gas production device is co-produced fuel sum, the coke furnace co-produced natural gas production device through gas pipe can be connected to sum for benzene fuel and fuel sum benzene removing device, the rich fuel sum benzene producing device through gas transmission pipe connected made hydrogen production device, the hydrogen production device made by gas circulation pipe connected coke furnace and coal cabinet, a finish made hydrogen tail sum recovery use. The hydrogen made tail sum recovery using device, using the coal cabinet inlet pipe front made hydrogen tail sum input coke furnace co-produced natural gas circulation device, increase yield of days fuel gas, reducing energy waste.
NOVELTY - A marsh gas processing pool system performing dry fermentation by livestock manure comprises straw growing pool, material mixing pool connected with the straw growing pool, and anaerobic fermentation tank for biogas fermentation, the straw growing pool by the first conveyor connected with chaff, the straw growing pool is connected with hay cutter by first conveyor, and connected with microbial inoculum tank via first pipeline; the straw growing pool and preparing mixing pool by the second conveyor connected with, the material mixing pool is connected with cow dung pool by third conveyor and connected with marsh gas pool by the fourth conveyor, at the same time the material mixing pool is connected with Ca (OH) 2 liquid storage tank through the second pipeline; material mixing pool and anaerobic fermentation tank are connected by lifting machine and feed machine; the anaerobic fermentation tank is provided marsh gas input pipe; the utility model can effectively control smell, with good killing effect on pathogen and insect eggs in waste, by diluting Ca (OH) 2, controls PH to prevention acid poisoning, efficiency is high.
NOVELTY - This utility model claims a high-efficient solid waste sorting processing device, comprising a reaction device, a hydraulic pressure homogenizer, a spiral converying device, a feeding port, a micro-pore aerator, a marsh gas air blower, a discharge pipe, a rotary recovery machine arm, an air outlet pipe, a biological organic material outlet, a sedimentation part outlet. Reaction device comprises sedimentation part, mixing part, on the floating part. Sedimentation part is inverted conical, spiral converying device connected with sedimentation part outlet. Mixing part to sedimentation part boundary and equipped with micro-pore aerator connected with marsh gas air blower micro-pore aerator, micro-pore aerator method set at feeding port, a feeding port above is hydraulic pressure homogenizer, biological organic material outlet and discharging pipe is set on mixing part and on the floating part, biological organic material outlet connection pipe extending to mixing part, rotating recovery machinery arm is connected with the air outlet pipe mounted reaction device at the top. The utility model has simple structure, and it can complete separating biological organic waste and non biological organic waste.
NOVELTY - The utility modelrelates to a straw particle processing device, specifically is one kind 220V oil electric dual-purpose biomass particle granulator. The biomass particle granulating machine comprises machine frame, motor, a differential mechanism, a speed reducer, a pressure bearing connector, a main shaft, a mould frame, a mould, pressure device and a material barrel, after the electric machine, a differential mechanism, a speed reducer, a pressure shaft and main shaft in turn connected with connector set on machine frame on the machine frame above the mould frame as follows with the discharging mouth is set on main shaft outside the mould set on the mould frame and is sleeved on the main shaft on the said pressure device and connected with main shaft, the barrel set on upper mould frame in mould cover and outside the compression device, the main upper shaft also set with stirring stick. The utility model is new type has simple and rational structure, small volume, and maintain suitable use is suitable for 220V oil power.
NOVELTY - The new type utility claims one plant cultivation waste water treatment recycling system, comprising collecting precipitate reaction pool, centrifugal dehydrating device, fermentation pool,, organic fertilizer collecting storehouse, waste water sediment regulating pool, Anaerobic reaction pool, marsh gas water separation device, marsh gas, marsh gas storage tank, an aeration pool, contact oxidation pool, flocculation precipitate pool and disinfecting pool, collecting precipitate reaction pool, centrifugal dehydrating device, centrifugal dehydrating device, fermentation pool, fermentation pool,, filter and organic fertilizer collecting storehouse recovery marsh gas and organic fertilizer, centrifugal dehydrating device, Anaerobic reaction pool, marsh gas water separation device, marsh gas water separation device, marsh gas and marsh gas storing jar-shaped tower into biogas sum recovery, gas water separating device, an aeration pool, contact oxidation pool, flocculation precipitate pool and disinfecting pool for waste water discharge, the cultivation waste water process to have effective treatment and recovery using, which avoids cultivation waste water for human and animal health and ecological environment equal generating bad influence, it also avoids have resource waste.
NOVELTY - The new type utility claims have one plant sludge gasification cement kiln system, the sludge gasification cement kiln system, comprising cement kiln and decomposing furnace, the inlet and outlet of the decomposing furnace of the cement kiln connected, the air outlet and the air inlet gasification furnace and the decomposing furnace through gas pipe is connected, wherein the feedstock gasification furnace through the transport system and storage connected, a slag outlet of the gasification furnace by slag system and raw system connected. The utility model is new type can greatly increase located scale and sludge, reducing have solid sludge directly enter the kiln shape and coal powder, the diffrence between cement raw material fineness, add have mass transfer heat transfer effect.
NOVELTY - The new type utility claims have one plant marsh gas recovery using device, comprising high concentrated waste water process system 1. Anaerobic biological treatment system 2 marsh gas storage tank 3, a PLC controller 4 and boiler 5, the high-concentration waste water Anaerobic processing system, biological treatment system and gas storage tank connected in turn, the gas outlet of air storage tank 3 to set with pressurizing blower (6) and booster fan through the transport pipe 7 and furnace front distribution valve 8 connected with, front furnace distribution valve by the dividing pipe 9 respectively and two multi-connection in the combustion unit mounted on the boiler, the PLC controller respectively and booster fan, burner and electric connection. The utility model is new type of beneficial effect is, save energy, increase resource use rate, protecting environment.
NOVELTY - The utility model is new type supply one kind anti-ozone flushing-free toilet, comprising the in parallel with discharge through hole in toilet and multi-row toilet pit, wherein one every row or every two rows below the toilet pit is provided with storage tank, inside the groove set with stirrer and filler. Suitable can by formed of washroom pit at the lower part of the groove, and set on the stirrer and filler in the groove, supplement or change new filler after using the toilet pit drain through hole falling down excrement directly enter in the storage groove, and mix and lower filler in stirrer action, make filler full absorption, degradation, completely eliminate peculiar smell, at the same time not again with water for flushing, saves have the precious water resource, and using one time segment is, in addition the use of filler may also as agricultural fertilizer.
NOVELTY - The new type utility claims one kind extracting rectifying and flash coupling separating propylene and propane and device, propylene and propane and separation device, comprising rectifying tower and extracting tower, the extracting rectifying tower upper part set with extracting agent inlet, lower part set with extracting rectifying tower raw material inlet on the tower top of the extracting rectifying tower extracting rectifying tower provided with the first outlet, the extracting rectifying tower provided with the second outlet, upper part of the flash tower provided with raw material inlet, the top part of the flash tower provided with the first outlet, bottom provided with the second outlet tower, rectifying tower extracting the second outlet of the extracting rectifying tower connected with the flash tower bottom raw material inlet, flash tower provided with the tower outlet connected with the second extracting rectifying tower upper part of the extracting agent inlet, after the utility model is new type for propylene and propane by using extracting rectifying technology separate out propane, for extracting rectifying tower containing extracting agent and propylene mixture by reducing pressure and cooling, reducing have the energy consumption in production operation process.
NOVELTY - The new type utility claims have one wet forming of plant biomass forming machine, composed of main clamping sleeve of the protecting cylinder, a forming cylinder coat, feeding hopper, piston bar, an outer housing, a double oil jar, oil pipe joint and machine frame, outer cover set on the machine frame on the upper cover set with oil pipe joint inner cover provided with double oil jar, piston bar through outer cover connected with double oil jar, upper piston bar set with feeding hopper, clamping sleeve set on upper protecting cylinder, the protecting cylinder connected with piston bar, maintaining tube and piston bar connecting terminal provided with forming cylinder coat. The utility model is new type device structure is simple, using the device technology is simple, suitable operation, low energy consumption, is 4kw.h/t, production efficiency high, productivity is 2t/h, reducing processing cost.
NOVELTY - Composition comprises bagasse as an immobilized carrier-containing fungi, preferably Trichoderma trichoderma and bacteria, preferably Klebsiella.    USE - The composition is useful in bioremediation of soil-containing phenanthrene (claimed).    ADVANTAGE - The composition improves the bioavailability of phenanthrene, and the microbial degradation efficiency of phenanthrene. The method is economical, and environmental friendly; and has simple preparation procedure.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the composition, comprising washing bagasse immobilized carrier, drying, cutting into pieces, adding into an Erlenmeyer flask, sterilizing by adding sterile inorganic salt-containing liquid culture medium, mixing bacterial suspension and fungal-bacterial suspension at 30 degrees C, sealing, shaking the culture at a speed of 150 rotations/minute in a shaker for two days, to obtain the final product containing maximum microbial biomass, where the ratio of liquid culture medium and inorganic salt with bagasse, is 10:3 (ml/g); and    (2) use of composition in bioremediation of soil contaminated with phenanthrene.
NOVELTY - Preparing immobilized particles, comprises screening sludge degrading strain, including Bacillus subtilis, Bacillus cereus, Bacillus megaterium, Bacillus licheniformis and Bacillus pumilus; placing in a shaker, and culturing to obtain fermentation broth; mixing the fermentation broth, and spray-drying into powder; and preparing immobilized particles using PVA-saturated boric acid powder.    USE - The immobilized particles are useful for reduction of activated sludge (claimed).    ADVANTAGE - The method achieves easy solid-liquid separation, and less secondary pollution.    DETAILED DESCRIPTION - Preparing immobilized particles, comprises (i) screening sludge degrading strain, including Bacillus subtilis, Bacillus cereus, Bacillus megaterium, Bacillus licheniformis and Bacillus pumilus; placing in a shaker, and culturing to obtain fermentation broth; where the weight ratio of Bacillus subtilis, Bacillus cereus, Bacillus megaterium, Bacillus licheniformis and Bacillus pumilus is 4-6:4-6:6-9:5-7:4; (ii) mixing the fermentation broth, and spray-drying into powder, where the drier air inlet temperature is 175-190 degrees C, the air outlet temperature is 80-90 degrees C, atomizer speed is 200-220 revolutions per minute, and the feed rate is controlled to 30-50 ml/minute; (iii) preparing immobilized particles using PVA-saturated boric acid powder, where the method includes dissolving 80 g polyvinyl alcohol in 1000 ml water by placing in water bath, then cooling to 30-40 degrees C, adding 10 g/l bacteria powder, 0.02% sodium alginate, and 4% silica, stirring and mixing; to obtain saturated boric acid solution, adjusting the pH to 6.5-7, mixing the above liquid solution, immobilizing to form pellets, having diameter of 2-5 mm, curing the formed beads at 4 degrees C for 1-2 days, then washing with saline 3-5 times.
NOVELTY - A high ammonia nitrogen plant cultivation biogas liquid of biological purification device, comprising biological filtering tower, second time purification filtering pool, biological filtering tower is multi-layer building structure, bottom mounted between network shape structure bracket, layer and there is gap layer, each layer of lower part is filled with biogas slurry processing biological film and absorbing solid, the upper filling immobilized bacteria body equal porous biological filter material, most lower layer is bottom incline shape separate water pool, second time purification filtering pool for runway and biological filter chamber, inner track fill of biological filter material, water out end of filter chamber is set with large specific surface area and high density biological film folding filter screen. The utility model is new type structure is simple, using suitable, low cost, low energy consumption, and ammonia nitrogen and can reduce efficient biogas liquid cultivation, using the conversion as nitrate nitrogen, the biogas slurry processing can use for mico-algae scale cultivation, as mico-algae sewage process provide one strip economic and efficient sewage pre-processing of new.
NOVELTY - Device for producing d-alpha tocopherol acetate comprises a reactor for containing reaction solution (1) and a stirrer (2), where the stirre is equipped with the reactor. The reactor below the surface of the reaction solution is provided with a filling box body structure of zinc powder (3). The box body structure is provided with a multiple of apertures not greater than minimum diameter of zinc powder particle.    USE - Device for producing d-alpha tocopherol acetate.    ADVANTAGE - The device for producing d-alpha tocopherol acetate in simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing d-alpha tocopherol acetate, which involves:    (A) adding zinc powder in the box body structure and then d-alpha tocopherol and excess acetic anhydride in the reactor at 130 degrees C for 3 hours;    (B) recovering the acetic anhydride after reaction completion and then adding the obtained material with hexane;    (C) stirring the obtained material and then removing the solvent; and    (D) distilling the obtained material to remove impurity in crude product and to obtain the desired product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for producing d-alpha tocopherol acetate.    Reactor for containing reaction solution (1)    Stirrer (2)    Filling box body structure of zinc powder (3)    Supporting structure (4)    Voids (9)
NOVELTY - Preparing catalyst involves grinding expanded vermiculite to obtain particles of expanded vermiculite and then dipping the expanded particles in nickel salt solution to obtain catalyst precursor. The catalyst precursor is subjected to perform microwave heat treatment to obtain the catalyst.    USE - Method for preparing catalyst used in synthesis gas methanation process to catalyze the reaction of carbon monoxide or carbon dioxide and hydrogen to produce methane (claimed).    ADVANTAGE - The method enables to prepare catalyst with good heat stability and catalytic activity, and has improved selectivity and yield of methane.
NOVELTY - Ultrasound-assisted wet anaerobic fermentation of household waste organic matter comprises (i) sorting municipal household waste; (ii) shearing and crushing the household waste, adding water, wet grinding, to obtain mixed waste slurry; (iii) carrying out ultrasonic disruption treatment; (iv) mixing the ultrasonic disruption treatment slurry with the remaining mixed waste slurry, adding into acidified reactor, and carrying out hydrolysis acidification; (v) carrying out anaerobic fermentation, and collecting the generated biogas, biogas residues and slurry in the fermentation reactor.    USE - The method is useful for ultrasound-assisted wet anaerobic fermentation of household waste organic matter (claimed).    ADVANTAGE - The method increases production rate and shortens the time of Anaerobic fermentation of marsh gas.    DETAILED DESCRIPTION - Ultrasound-assisted wet anaerobic fermentation of household waste organic matter comprises (i) sorting municipal household waste, removing plastic bags, metal, glass and other hard-biodegradable materials; (ii) shearing and crushing the household waste, adding 0.5-2.5 times volume of water, wet grinding in a ball mill, to obtain mixed waste slurry; (iii) carrying out ultrasonic disruption treatment of 10-40 vol.% mixed waste slurry, or adding 10-30% mixed waste slurry and 1-2 times volume of sewage residual sludge into ultrasonic disruption reactor, and carrying out ultrasonic crushing treatment; (iv) mixing the ultrasonic disruption treatment slurry with the remaining mixed waste slurry, adding into acidified reactor, and carrying out hydrolysis acidification for 3-5 days; (v) adding the acidified mixed waste slurry into the anaerobic fermentation reactor, adding 0.3-0.5 times the volume of sewage residual sludge or manure, carrying out anaerobic fermentation at 35-55 degrees C, collecting the generated biogas, biogas residues and slurry in the fermentation reactor.
NOVELTY - The system has an anaerobe reaction bath (110) that produces methane gas with anaerobic treatment box. An immersed membrane module (10) is equipped within anaerobic film distillation separation tub to filter wastewater. The rotary disc (20) is equipped in both sides of immersed membrane module and rotated to generate turbulence of the wastewater in mobility filter media (120). Fluid path is equipped inside the immersed membrane module such that moisture of wastewater is steamed by temperature difference of cooling water and wastewater.    USE - Film distillation coupled type anaerobic sewage and wastewater treatment system.    ADVANTAGE - The water quality can be improved by combining the bioreactor and film distillation process. The contamination of the immersed membrane module surface can be reduced effectively by using rotary disc and mobility filter media and the energy efficiency can be improved. The replacement or corrective maintenance of the separation film can be achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a film distillation coupled type anaerobic sewage and wastewater treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the film distillation coupled type anaerobic sewage and wastewater treatment system. (Drawing includes non-English language text)    Immersed membrane module (10)    Rotary disc (20)    Anaerobe reaction bath (110)    Mobility filter media (120)    Water level sensor (150)
NOVELTY - Biomass fuel production involves crushing plant straw, wood residues and wood waste into granules into 2 mm particles. The plant straw crops include rice straw, wheat straw crops, corn crop straw, cotton crop straw, canola crop straw or peanut crop straw. The wood-processing residues include sawdust or wood shavings. The wood waste includes wood waste, old wood, scrap wood furniture or disposable waste wood. The crushed straw, wood processing residues and wood waste particles are dried. The dried straw, wood processing residues and wood waste particles are uniformly mixed.    USE - Method for producing biomass fuel (claimed).    ADVANTAGE - The method produces the biomass fuel in a simple manner with high heat value, compact structure, strong performance and good durability, easy combustion performance, and longer combustion time.    DETAILED DESCRIPTION - Biomass fuel production involves crushing plant straw, wood residues and wood waste into granules into 2 mm particles. The plant straw crops include rice straw, wheat straw crops, corn crop straw, cotton crop straw, canola crop straw or peanut crop straw. The wood-processing residues include sawdust or wood shavings. The wood waste includes wood waste, old wood, scrap wood furniture or disposable waste wood. The crushed straw, wood processing residues and wood waste particles are dried. The dried straw, wood processing residues and wood waste particles are uniformly mixed. The obtained mixture is compressed into blocks, and then cooled naturally at room temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the biomass fuel production method. (Drawing includes non-English language text).
NOVELTY - Preparing water soluble fertilizer paste involves stirring chelated trace element liquid additive, water and moisture fixing additives for 5-10 minutes in a groove to obtain homogeneous liquid phase that is stirred with urea, agricultural ammonium nitrate and monoammonium phosphate in second level groove at 50-80 degrees C for 10-20 minutes. The obtained solution is stirred with potassium chloride, potassium sulfate, ammonium sulfate, monoammonium phosphate, magnesium sulfate heptahydrate, borax and ammonium molybdate in three level inner groove at 50-80 degrees C for 15-30 minutes.    USE - Method for preparing water soluble fertilizer (claimed).    ADVANTAGE - The method enables to prepare water soluble fertilizer that ensures fast dissolution, less residue, high efficiency, no device requirement, low manufacturing cost, no agglomeration and simple preparation.    DETAILED DESCRIPTION - Preparing water soluble fertilizer paste involves stirring chelated trace element liquid additive, water and moisture fixing additives for 5-10 minutes in a groove to obtain homogeneous liquid phase that is stirred with urea, agricultural ammonium nitrate and monoammonium phosphate in second level groove at 50-80 degrees C for 10-20 minutes. The obtained solution is stirred with potassium chloride, potassium sulfate, ammonium sulfate, monoammonium phosphate, magnesium sulfate heptahydrate, borax and ammonium molybdate in three level inner groove at 50-80 degrees C for 15-30 minutes to obtain uniform paste that is discharged from discharge valve to paper box and molded using paper and polyvinyl chloride film bag. The molded product is kept for 2-8 hours and then cooled, crystallized and cured to obtain product.
NOVELTY - Extraction of bio-preservative involves crushing cleaning and crushing dandelion, peony bark, and purslane in weight ratio 1:2:1, soaking in a weight ratio of 1:1-3 for 3-4 hours, boiling, simmering for 20-30 minutes, filtering, and refrigerating the filtrate at 2-4 degrees C in a refrigerator, adding water to the residue in a liquid ratio of 1:0.5-1, soaking for 1-2 hours, extracting for 30-60 minutes, filtering, combining the filtrates, and refrigerating at 2-4 degrees C.    USE - Extraction of bio-preservative for fruits e.g. strawberry, cherry, raspberry, bayberry and hawthorn (all claimed).    ADVANTAGE - The method provides safe, nontoxic and environmentally-friendly bio-preservative, which replaces chemical fungicides and preservatives.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of bio-preservative in preservation of fruits, which involves immersing fruit in the filtrate for 3-5 minutes, drying, packaging in polyethylene film, opening holes in polyethylene film, inspecting, and storing at relative humidity of 90-95% and 1 plus minus 0.5 degrees C.
NOVELTY - A biodiesel comprises 40-60 pts. wt. catering waste oil, 30-50 pts. wt. swill oil, 20-40 pts. wt. rice bran, 10-20 pts. wt. rapeseed oil, 40-60 pts. wt. methanol, 10-20 pts. wt. hexadecyl alcohol, 1 -3 pts. wt. sodium hydroxide, 0.2-0.6 pts. wt. potassium bicarbonate, 0.1-0.3 pts. wt. ferrocene, 10-20 pts. wt. alkyl amino, 1-3 pts. wt. triethylamine, 10-20 pts. wt. ethyl acetate, 0.1-0.3 pts. wt. isopropyl nitrate, and 1-3 pts. wt. catalyst.    USE - Biodiesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biodiesel comprising:    (A) filtering using catering waste oil and hogwash oil water filter, removing solid impurity;    (B) dehydrating the food after filtering waste oil and hogwash oil water at 60-80 degrees C, adding rice bran oil, vegetable oil, methanol and cetyl alcohol;    (C) stirring, reacting at 40-80 degrees C for 10-20 minutes;    (D) adding the products of steps (B) and (C) to the autoclave, adding the remaining ingredients, and heating at 300-400 degrees C and 10-12 MPa for 10-20 minutes; and    (E) cooling to room temperature, and carrying out phase separation process.
NOVELTY - A composite fuel comprises 30-50 pts. wt. benzene, 5-10 pts. wt. gasoline, 40-60 pts. wt. cracked kerosene, 10-20 pts. wt. sulfonated oil, 0.03-0.06 pts. wt. ferrocene, 1-3 pts. wt. isopropyl nitrate, 0.3-0.8 pts. wt. diisobutyl sodium succinate, 0.1-0.3 pts. wt. ethylene glycol monomethyl ether, 0.1-0.3 pts. wt. disodium hydrogen phosphate, 0.1-0.3 pts. wt. sodium hydroxide, 0.1-0.3 pts. wt. succinimide, 2-4 pts. wt. cetane improver, 5-10 pts. wt. reducing stabilizer, 10-20 pts. wt. viscosity modifier, and 0.1-0.3 pts. wt. compound additive.    USE - Composite fuel.    ADVANTAGE - The composite fuel has low cost, low fuel consumption, and simple manufacturing technique, uses raw materials that can be easily obtained, is safe and easy to use, and can meet environmental requirements.
NOVELTY - Pharmaceutical grade soybean linoleic acid preparation involves placing soy mixed fatty material into thin film evaporator at 70-90 degrees C in vacuum for removing dissolved gases, moisture and volatile impurities. The formed material is treated through film evaporator distillation at 200-260 degrees C in vacuum for distilling saturated fatty acids having lower boiling points. The obtained material is treated through film evaporator distillation at 220-280 degrees C in vacuum to obtain pharmaceutical grade soybean linoleic acid.    USE - Method for preparing pharmaceutical grade soybean linoleic acid (claimed).    ADVANTAGE - The method prepares the pharmaceutical grade soybean linoleic acid in a simple and feasible manner by using stable and eco-friendly operation.
NOVELTY - The fermentation system has a liquid fermentation tank that is filled with the biogas slurry and connected with multiple solid fermentation tanks. The upper portion of the liquid fermentation tank is connected to the biogas inlet through a constant flow pipe and an input pipe. The biogas inlet is connected to a sprayer installed in the solid fermentation tank for spraying the biogas slurry. The lower portion of the solid fermentation tank is connected to the lower portion of the liquid fermentation tank through a constant flow pump and an output pipe.    USE - Energy grass liquid-solid biogas fermentation system.    ADVANTAGE - The operation of the energy grass liquid-solid biogas fermentation system is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an operating method of energy grass liquid-solid biogas fermentation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the energy grass liquid-solid biogas fermentation system.
NOVELTY - Preparing bio-organic fertilizer involves utilizing composite microorganism microbial inoculum, comprises 15-20 wt.% Bacillus subtilis, 15-20 wt.% Aspergillus oryzae, 30-40 wt.% Trichoderma viride, 10-15 wt.% Phanerochaete chrysosporium and 10-15 wt.% Geobacillus stearothermophiIus. Composite microorganism microbial inoculums is prepared by culturing Bacillus subtilis at 28-32 degrees C for 1-3 days to maintain pH at 7.2-7.4, Aspergillus oryzae at 25 degrees C for 4-7 days and Trichoderma viride at 25-28 degrees C for 4-7 days.    USE - Method for preparing bio-organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare bio-organic fertilizer is enriched in nitrogen, phosphorus, potassium and organic matter, and increases urease and cellulose contents in soil.    DETAILED DESCRIPTION - Preparing bio-organic fertilizer involves utilizing composite microorganism microbial inoculum, comprises 15-20 wt.% Bacillus subtilis, 15-20 wt.% Aspergillus oryzae, 30-40 wt.% Trichoderma viride, 10-15 wt.% Phanerochaete chrysosporium and 10-15 wt.% Geobacillus stearothermophiIus. Composite microorganism microbial inoculums is prepared by culturing Bacillus subtilis at 28-32 degrees C for 1-3 days to maintain pH at 7.2-7.4, Aspergillus oryzae at 25 degrees C for 4-7 days, Trichoderma viride at 25-28 degrees C for 4-7 days and Geobacillus stearothermophiIus at 60 degrees C for 1-3 days and maintain pH at 6.8 to obtain liquid culture medium. Liquid culture medium (1-8 kg) is fermented at 25-30 degrees C for 15-40 days, and then crushed in a pulverizer to obtain granules less than 2 cm.
NOVELTY - Bio-organic fertilizer comprises 100-1000 pts. wt. straw and 1-15 pts. wt. composite microorganism microbial inoculums. Composite microorganism microbial inoculums comprise Bacillus subtilis, Aspergillus niger, Trichoderma viride, Phanerochaete chrysosporium and Geobacillus stearothermophilus.    USE - Bio-organic fertilizer.    ADVANTAGE - The bio-organic fertilizer improve soil structure, increases crop yield and quality, ensures normal composting fermentation in 15 days, accelerates straw decomposition, and enhances degradation of cellulose, hemicellulose and lignin.
NOVELTY - Bio-organic fertilizer comprises 100-1000 pts. wt. straw, 1-10 pts. wt. wheat straw rotten agent, 10-100 pts. wt. animal excrement and 1-10 pts. wt. inorganic fertilizer, where straw rotten agent is Bacillus subtilis, Aspergillus niger, Trichoderma reesei, Phanerochaete chrysosporium or Geobacillus stearothermophilus.    USE - Bio-organic fertilizer used for improving soil (claimed).    ADVANTAGE - The bio-organic fertilizer increases soil urease and cellulase activity.
NOVELTY - Compound fertilizer comprises 75-85 wt.% diammonium phosphate, 5-9 wt.% humic acid powder, 6-9 wt.% potassium containing shale powder, 1-4 wt.% Bacillus mucilaginosus and 1-4 wt.% Bacillus megaterium, where diammonium phosphate has 12% nitrogen element content and 16% phosphorus element content.    USE - Compound fertilizer.    ADVANTAGE - The compound fertilizer ensures synergistic effect and disease-resistant property to crop.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing compound fertilizer, which involves;    (A) drying diammonium phosphate in drying device;    (B) mixing humic acid powder and Bacillus megaterium liquid;    (C) adding obtained mixture in dry roller drying device;    (D) adding potassium shale powder and Bacillus mucilaginosus liquid in drying device;    (E) coating obtained granule with coating solvent to obtain coated granule; and    (F) drying and sieving granule to obtain product.    .
NOVELTY - Preparing liquid fertilizer involves collecting waste mushroom after removing it from bag to obtain regeneration matrix. Regeneration matrix matrix is mixed with dry chicken manure and crop straw in ratio of 1:1:1 to obtain fermentation matrix. Water and composite culture medium are mixed in the fermentation matrix and carried out fermentation in a fermentation tank at low temperature for 12 hours to obtain fermentation liquid. Fermentation liquid is dried and material is added.    USE - Method for preparing liquid fertilizer used for butterbur (claimed) for preventing and treating plant diseases and insect pests.    ADVANTAGE - The method is economical and eco-friendly, reduces agriculture products waste, and enables to prepare liquid fertilizer that promotes growth of butterbur.    DETAILED DESCRIPTION - Preparing liquid fertilizer involves collecting waste mushroom after removing it from bag to obtain regeneration matrix. Regeneration matrix matrix is mixed with dry chicken manure and crop straw in ratio of 1:1:1 to obtain fermentation matrix. Water and composite culture medium are mixed in the fermentation matrix and carried out fermentation in a fermentation tank at low temperature for 12 hours to obtain fermentation liquid. Fermentation liquid is dried and material is added. Material comprises of 5-10 g/l urea, 3-4 g/l ferric nitrate, 1-2 g/l zinc nitrate, 3-4 g/l ammonium phosphate, 0.5-0.7 g/l surface active agent, 0.5-1.5 g/l humic acid and 0.05-0.1 g/l pH stabilizer.
NOVELTY - Fertilizer composition comprises organic fertilizer, chemical fertilizer, humic acid, microorganisms, and salinization or conditioning agent. Organic fertilizer comprises food waste, manure, and straw. Microorganisms comprise nitrogen-fixing bacteria, phosphorus bacteria, fungi and fermentation bacteria. Chemical fertilizer comprises potassium, nitrogen, phosphorus, and potash fertilizer. Salinization or conditioning agent comprises gypsum, furfural residue, calcium superphosphate and ferrous sulfate.    USE - Fertilizer used for sugar beet (claimed).    ADVANTAGE - The fertilizer is cost-effective, and obtained by a simple method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) weighing organic fertilizer components such as food waste, straw, manure, and ferrous sulfate;    (B) fermenting the weighed product;    (C) mixing obtained product with superphosphate, microorganisms, humic acid, gypsum and furfural residue to obtain granules; and    (D) mixing obtained product with nitrogen, phosphate, potash and microelement fertilizer to obtain fertilizer composition.
NOVELTY - Selenium-enriched soil fertilizer comprises 6-8 kg manure, 0.8-1.2 kg lime, 4.0-6.0 kg poultry and livestock manure, 3.5 kg cake fertilizer and 3-5 g sodium selenite. Poultry and livestock manures are obtained by mixing Sorghum, wheat and soybean in ratio of 6:3:1, and then crushed to obtain fermentation substrate. Fermentation substrate is mixed uniformly with selenium yeast in ratio of 5:1 and water is mixed to carry out fermentation at 28 degrees C for 70 days to obtain fermented product. The fermented product is mixed with poultry and livestock feed.    USE - Selenium-enriched soil fertilizer used for planting vegetable (claimed).    ADVANTAGE - The selenium-enriched soil fertilizer regulates pH of acidic soil, maintains normal growth of Osmunda japonica in highly acidic soil, and increases yield of vegetable.    DETAILED DESCRIPTION - Selenium-enriched soil fertilizer comprises 6-8 kg manure, 0.8-1.2 kg lime, 4.0-6.0 kg poultry and livestock manure, 3.5 kg cake fertilizer and 3-5 g sodium selenite. Poultry and livestock manures are obtained by mixing Sorghum, wheat and soybean in ratio of 6:3:1, and then crushed to obtain fermentation substrate. Fermentation substrate is mixed uniformly with selenium yeast in ratio of 5:1 and water is mixed to carry out fermentation at 28 degrees C for 70 days to obtain fermented product. The fermented product is mixed with poultry and livestock feed to obtain poultry and livestock manure.
NOVELTY - Organic compound fertilizer comprises 50-70 pts. wt. earthworm manure, 30-50 pts. wt. pig manure, 20-30 pts. wt. dairy manure, 20-30 pts. wt. fly ash, 20-30 pts. wt. alfalfa, 5-15 pts. wt. lees and 1-5 pts. wt. urea.    USE - Organic compound fertilizer.    ADVANTAGE - The organic compound fertilizer reduces waste problem in green and environment-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic compound fertilizer, which involves;    (A) mixing earthworm manure, pig manure and dairy manure;    (B) fermenting obtained mixture for 30-50 days; and    (C) mixing fly ash, lees, urea and crushed alfalfa root with fermented materials to obtain product.
NOVELTY - Alcohol-based fuel comprises 94-98 pts. wt. methanol, 0.15-0.35 pts. wt. ethanol, 2-4 pts. wt. benzene, 0.03-0.05 pts. wt. ferrocene, 0.5-0.6 pts. wt. petroleum ether, 2-4 pts. wt. solvent oil, 0.2-0.4 pts. wt. glycerol, and 0.4-0.6 pts. wt. ethyl acetate.    USE - Used as alcohol-based fuel.    ADVANTAGE - The fuel enhances component solubility, increases combustion performance, adopts strict operating procedures, produces strong and stable flame, which is light red with high calorific value, complete combustion and high thermal efficiency, is economical, has high quality, is suitable for hotel and household use, and has good economical and social benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing alcohol-based fuel comprising (i) adding metanol into container, (ii) taking ferrocene, mixing with benzene and diluting, stirring uniformly to obtain the mixture A, (iii) adding ethyl acetate into mixture A and stirring uniformly to obtain mixture B, (iv) dissolving glycerol in ethanol, adding in the container, adding petroleum ether and solvent oil, continuously adding into container, and (v) taking prepared mixture B and adding in the container, fully stirring for 3-6 hours, placing for 10-14 hours to obtain the finished product.
NOVELTY - Method for processing kelp involves screening microbial strains, decomposing kelp using screened microbes, and extracting active components from decomposed kelp.    USE - The method is useful for producing kelp seaweed fertilizer including paste fertilizer, drip irrigation fertilizer, fungus fertilizer, granule fertilizer, water-soluble powder fertilizer, and foliar fertilizer, and kelp seaweed extract as single nutrient comprising polysaccharide, oligosaccharide, and amino acids (claimed).    ADVANTAGE - The method shortens degradation time of kelp, and is environment-friendly.
NOVELTY - Bio-organic fertilizer comprises Bacillus subtilis broth (2-3%) of concentration 109 colony forming unit/ml, soybean residue (15-25%), peat (35-45%), chicken manure (8-12%), wood (2-4%), and straw (20-30%).    USE - Bio-organic fertilizer used for tomato for preventing disease caused by root-knot nematode.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-organic fertilizer used for tomato, which involves mixing raw material with water to obtain water content of mixture to 10%, and fermenting the obtained mixture for 30 days to obtain final product.
NOVELTY - Ecological fertilizer comprises 20-30 wt.% ecological organic fertilizer, 5-10 wt.% humic acid, 1-2 wt.% humic acid chelated micro-element and 60-70 wt.% inorganic fertilizer.    USE - Ecological fertilizer used for planting watermelon (claimed).    ADVANTAGE - The ecological fertilizer increases yield and quality of watermelon in low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing ecological fertilizer, which involves;    (A) obtaining bacterial strain that is utilized to obtain ecological organic fertilizer;    (B) mixing inorganic fertilizer raw materials uniformly to to obtain inorganic fertilizer;    (C) mixing ecological organic fertilizer, inorganic fertilizer, humic acid and humic acid chelated micro-element uniformly;    (D) granulating obtained mixture; and    (E) pelleting, drying and sieving granules to obtain product that is packaged.    .
NOVELTY - An ammonium nitrate production wastewater biological treatment device comprises anaerobic fermentation sequencing batch reactor (1), sludge pump, pH on-line monitoring instrument (1.2), stirrer, temperature control device (1.5), sludge valve, centrifuge, mixing pool (2), ammonium nitrate wastewater adding pump (2.1), nitric acid adding pump (2.2), upflow anaerobic fixed film reactor (3), gas drying device, drainage valve, and sponge filler (3.7). The pH on-line monitoring instrument is connected to water tank and second drainage valve.    USE - Device and method of biological method processing wastewater of ammonium nitrate.    ADVANTAGE - The device has combination of sequencing batch reactor and upflow anaerobic fixed film reactor to achieve both sludge reduction and ammonium nitrate wastewater denitrification.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ammonium nitrate production wastewater biological treatment device.    Anaerobic fermentation sequencing batch reactor (1)    pH on-line monitoring instrument (1.2)    Temperature control device (1.5)    Mixing pool (2)    Ammonium nitrate wastewater adding pump (2.1)    Nitric acid adding pump (2.2)    Upflow anaerobic fixed film reactor (3)    Sponge filler (3.7)
NOVELTY - Liquid organic fertilizer preparation device comprises extrusion crusher, hydrolysis unit, hydrolyzed settling tank, feed pump, anaerobic fermentation reactor, sedimentation storage tank, high-temperature sterilization device, return pump, and hollow cylinder rotatable device. The extrusion crusher and settling tank are connected with anaerobic fermentation reactor through feed pump. The storage tank is connected with return pump. The hydrolysis unit comprises hollow cylindrical surface holes, internal baffles, and inoculum.    USE - Liquid organic fertilizer preparation device.    ADVANTAGE - The device prepares organic fertilizer cost-effectively with high quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the liquid organic fertilizer, which involves crushing fruits and vegetables waste containing impurities, separating solid-liquid, degrading organic liquid carbohydrate, fermenting the mixture under anaerobic fermentation reactor, crushing solid mixture, adding solid mixture into hydrolysis tank, preparing hydrolyzate, controlling the temperature of the mixture at 30-37 degrees C and 20-25 revolutions per minute (rpm), performing anaerobic fermentation of the hydrolyzate at 37-38 degrees C, adding hydrolyzate into sedimentation storage tank, and sterilizing product.
NOVELTY - Sorting, recovering and resource utilizing landfill garbage by adding waste separation sorted waste sand waste landfill type waste, combustible garbage, and metal, rock and earth garbage waste into quantitative feeding machine, sorting, discharging waste sand at less than 25 M/M, separating out separated soil and sand used as organic fertilizer raw material, and sorting out the combustible garbage used as combustible garbage regenerated fuel.    USE - Sorting, recovering and resource utilizing landfill garbage (claimed).    ADVANTAGE - The method fully realizes garbage waste energy, saves resource, and utilizes waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for landfill garbage sorting, recovery and resource utilization device.
NOVELTY - Method for preparing biological soil remediation agent, involves (a) mixing anaerobic Bacillus strain TIBCC1.002, Micrococcus luteus strain TCCC23001, Pseudomonas fluorescens strain AS1.867, and Burkholderia cepacia strain NKCCMRNK.T2-2 in a weight ratio of 3-6:2-5:1-4:1-3, and adding activated sludge to the mixture, (b) filtering slurry using hollow fiber membrane having pore size of 0.1-0.2 mu m, and (c) mixing activated sludge and slurry in a weight ratio of 3-9:1-5, and stirring mixture.    USE - The method is useful for preparing biological soil remediation agent (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage method of the biological soil remediation agent, which involves preparing the biological soil remediation agent, adding agent into contaminant containing soil, and detecting contaminated soil for every 5-15 days.
NOVELTY - A metal organic framework material comprises framework material of copper oxide silver octahedron (CuO4(OH)3Ag) and naphthalene dicarboxylic acid in bridged form in which copper hydroxide silver octahedron belongs to rhombic system with base of 11. 914 and 6. 877 and height of 21.341, beta of 123, cell volume (V) of 2455.3, Z of 4 and density of 386 g/cm3. Ratio of metal organic skeleton material and copper and silver atom is 1: 0.05-0.9. Aperture is 0.43-0.47 nm, volume is 65% and total volume is 90%.    USE - Metal organic skeleton material for natural gas storage (claimed).    ADVANTAGE - Selective absorption of methane is increased.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of metal organic framework material which involves dipping polyhydric alcohols solid particle in silver salt water solution after drying in which boiling point range of multi-element alcohol is 220-300 degrees C, drying, mixing naphthalene dicarboxylic acid mixture, stirring uniformly, dropwise adding of hydrofluoric acid, stirring uniformly, transferring mixture to reaction kettle, sealing at 80-120 degrees C, processing for 1-4 hours at 150-250 degrees C, preferably 190-220 degrees C for 2-6 hours then at 300-400 degrees C for 5-15 hours, cooling to room temperature, through filtering, water washing, drying and calcining; and    (2) application of metal organic skeleton material in natural gas storage.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the network shape dimension of metal organic framework material.
NOVELTY - Preparation of ( alpha )-carotene (I) involves performing Wittig-Horner condensation of diethyl ((2E,4E)-3-methyl-5-(2,6,6-trimethylcyclohex-2-en-1-yl)penta-2,4-dien-1-yl)phosphonate (II) and (2E,4E,6E)-2,7-dimethylocta-2,4,6-trienedial (III) at 0-30 degrees C.    USE - Preparation of ( alpha )-carotene (claimed).    ADVANTAGE - The method enables preparation of ( alpha )-carotene with high yield by simple, economical and environmentally-friendly process.    DETAILED DESCRIPTION - Preparation of ( alpha )-carotene of formula (I) involves performing Wittig-Horner condensation of diethyl ((2E,4E)-3-methyl-5-(2,6,6-trimethylcyclohex-2-en-1-yl)penta-2,4-dien-1-yl)phosphonate of formula (II) and (2E,4E,6E)-2,7-dimethylocta-2,4,6-trienedial of formula (III) at 0-30 degrees C.
NOVELTY - A gene encoding alanine isomerase, which is obtained from yeast cDNA library, comprising fully defined 1200 bp (SEQ ID NO: 1) given in the specification, is new.    USE - The gene is useful for preparing D-alanine.    ADVANTAGE - By using the gene encoding alanine isomerase, the method can improve conversion efficiency and can shorten D-alanine process. Also, the method can reduce production cost and can reduce environmental pollution.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) an alanine isomerase comprising fully defined 399 amino acids (SEQ ID NO: 3) and having molecular weight of 46880.57773 Da; (2) a recombinant expression plasmid comprising the gene; (3) a genetically engineered bacterium, e.g. Escherichia coli that is transformed using the recombinant expression plasmid; and (4) a method for preparing alanine isomerase comprising: (a) cloning gene encoding alanine isomerase; (b) constructing recombinant expression plasmid; (c) linearization and purification of recombinant expression plasmid; (d) screening recombinant expression plasmid; and (e) inducing expression of genetically engineered bacteria to obtain alanine isomerase, and purifying.
NOVELTY - A recombinant vector comprising fusion gene comprising pediocin leader peptide gene and mature colicin V gene, is new.    USE - The recombinant vector or recombinant Lactobacillus plantarum is useful for preparing probiotics; and useful in food industry (all claimed).    ADVANTAGE - The recombinant Lactobacillus plantarum can simultaneously secrete pediocin PA-1 and colicin V; has good inhibition effect against Escherichia coli and Listeria bacteria; does not produce toxic side effects and residues; and provides environmental and food safety.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a method for preparing recombinant vector; (2) a host cell comprising the recombinant vector; and (3) a colicin V secreted recombinant Lactobacillus plantarum comprising the recombinant vector.
NOVELTY - An Hvsusiba2 gene for reducing methane emission in rice plants is new.    USE - The Hvsusiba2 gene is useful for reducing methane emission in rice plants.    ADVANTAGE - Since the Hvsusiba2 gene reduces methane emission in rice plants, this helps reduce greenhouse effect in the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a vector comprising the Hvsusiba2 gene.
NOVELTY - Method for performing remediation for sewage, involves (a) isolating and purifying indigenous beneficial microorganisms by collecting eutrophication sediment, adding sterilized distilled water, suspending the sediments in distilled water, shaking mixture, and identifying beneficial species capable of degrading toxic substances, (b) collecting water, observing unicellular algae species and separating Chlorella by capillary action, and (c) adjusting temperature and pH, performing large cultivation of Chlorella and beneficial species and purifying sewage.    USE - The method is useful for performing remediation for sewage (claimed).    DETAILED DESCRIPTION - Method for performing remediation for sewage, involves (a) isolating and purifying indigenous beneficial microorganisms, collecting eutrophication sediment, adding sterilized distilled water, suspending the sediments in distilled water, shaking the mixture, inoculating the mixture in agar medium and screening and identifying beneficial species capable of degrading toxic substances, (b) collecting water, observing unicellular algae species under microscope and separating Chlorella by capillary action, and (c) adjusting temperature and pH of lake, performing large cultivation of Chlorella and beneficial species in the step (a) and purifying sewage.
NOVELTY - Preparation of atorvastatin intermediate i.e. 4-(3-chloro-4-methoxybenzylamino)-2-methyl thiopyrimidine-5-carboxylate (I) comprises cyclization reacting ethyl cyanoacetate (IV) with methyl thiourea (V) and triethyl orthoformate (VI) in the presence of an alkali to prepare 2-methylthio-4-amino-pyrimidine-5-carboxylic acid ethyl ester (II), and substitution reacting with 3-chloro-4-methoxy-benzyl halide (III) in an alkaline condition to obtain (I).    USE - Preparation of atorvastatin intermediate i.e. compound (I) (claimed).    ADVANTAGE - The method uses easily obtained raw materials, is environment-friendly and has high total yield.    DETAILED DESCRIPTION - Preparation of atorvastatin intermediate i.e. 4-(3-chloro-4-methoxybenzylamino)-2-methyl thiopyrimidine-5-carboxylate of formula (I) comprises cyclization reacting ethyl cyanoacetate of formula (IV) with methyl thiourea of formula (V) and triethyl orthoformate of formula (VI) in the presence of an alkali to prepare 2-methylthio-4-amino-pyrimidine-5-carboxylic acid ethyl ester of formula (II), and substitution reacting with 3-chloro-4-methoxy-benzyl halide of formula (III) in an alkaline condition to obtain (I).    X=Cl, Br or I.
NOVELTY - 2-Thiophene ethylamine and formaldehyde are added to reactor, alkyl halide solvent and solid superacid catalyst are added, and reacted at 30-80 degrees C for 1-10 hours. The resulting solution is cooled to room temperature, base catalyst and 2-chlorobenzyl chloride are added, heated at 30-80 degrees C for 1-10 hours, cooled filtered, and hydrogen chloride gas is passed to the filtrate to obtain ticlopidine hydrochloride.    USE - Preparation of ticlopidine hydrochloride (claimed).    ADVANTAGE - The method provides ticlopidine hydrochloride using corrosion-resistant device, by economical and environmentally-friendly process.
NOVELTY - Method for performing biogas fermentation, involves (a) taking and crushing rice straw to mesh size of 6 mm and adding 7-9 wt.% feed solution to rice straw, (b) adding 0.1-0.3 wt.% composting agent to the mixture and reacting the mixture for 2-3 days, (c) adding 120-150 wt.% pretreatment solution to the mixture and placing the mixture in digesting tank, and (d) adding 40-50 wt.% microbial inoculum to the mixture, fermenting the mixture, and stirring the fermented mixture for once in 7-10 days.    USE - The method is useful for performing biogas fermentation which is useful for producing biogas used for cooking (all claimed).    ADVANTAGE - The method does not require livestock and poultry manure as raw material, and is cost-effective and environmentally-friendly.
NOVELTY - Method for culturing Eucalyptus dunnii seedling involves mixing yellow soil and clean sand, loading the mixture into a basket, mixing E.dunnii seeds with homogeneous matrix, covering sown seeds, spraying water on seeds, mixing coconut husk, carbonized rice husk, peat, and yellow soil, adding calcium magnesium phosphate, covering the mixture using a thin film, fermenting the mixture to obtain a light matrix, transplanting seeds, managing transplanted seedling by spraying thiophanate methyl or chlorothalonil, and applying fertilizer to plants.    USE - The method is useful for culturing E.dunnii seedling (claimed).    ADVANTAGE - The method provides thick and strong seedlings. The cultured seedling is convenient to transport and has high survival rate, environmental benefits and ecological benefits.    DETAILED DESCRIPTION - Method for culturing Eucalyptus dunnii seedling involves (a) mixing yellow soil and clean sand in a ratio of 1:1, loading the mixture into a basket, disinfecting the basket using 0.5 vol.% potassium permanganate, covering the basket with mulch a day, and opening the cover, (b) mixing E.dunnii seeds with a small amount of homogeneous matrix, evenly spreading matrix, sowing seeds, covering sown seeds, spraying water on seeds, and covering the sown seeds with a film to maintain moisture, (c) mixing coconut husk, carbonized rice husk, peat, and yellow soil in a weight ratio of 5:2.5:2:0.5, adding 4 kg per calcium magnesium phosphate per m3, covering the mixture using a thin film, fermenting the mixture to obtain a light matrix, (d) transplanting seeds after developing three leaves, and grow to a height of 3-4 cm into cup containing matrix, drenching the root in water, covering the root with a film after bagging, and finally seedling covering with a shade cloth, and (e) managing the transplanted seedling by spraying thiophanate methyl or chlorothalonil to prevent disease, and applying aqueous solution of fertilizer to plants.
NOVELTY - Mesembryanthemoidigenic acid (I), 29-hydroxyhederagenin (II), 3( beta ),6( beta )-dihydroxy-olean-12-ene-28-oic acid (III), scutellaric acid (IV), arjunic acid (V) and 3( beta ),6( beta ),23-trihydroxy-olean-12-en-28-oic acid (VI), are new.    USE - New terpenoids are used in preparation of medicine in form of oral dosage form chosen from wettable powder, tablet, granule, oral liquid, dripping pill, capsule, controlled or sustained release dosage forms or nanopreparation (all claimed) which is useful for treating type II diabetes mellitus.    ADVANTAGE - The terpenoids are prepared safely without causing pollution to the environment.    DETAILED DESCRIPTION - Mesembryanthemoidigenic acid of formula (I), 29-hydroxyhederagenin of formula (II), 3( beta ),6( beta )-dihydroxy-olean-12-ene-28-oic acid of formula (III), scutellaric acid of formula (IV), arjunic acid of formula (V) and 3( beta ),6( beta ),23-trihydroxy-olean-12-en-28-oic acid of formula (VI) or their salt, are new. INDEPENDENT CLAIMS are included for the following:    (1) preparation of triterpenoids (I)-(VI); and    (2) alpha -glucosidase inhibitor medicine, comprising predetermined amount of triterpenoid, and carrier or excipient.
NOVELTY - A 1,3-cyclohexyl-1,1-dimethylurea compound (I'), is new.    USE - New 1,3-cyclohexyl-1,1-dimethyl urea compound is used for preparing antipsychotic cariprazine (claimed).    ADVANTAGE - The 1,3-cyclohexyl-1,1-dimethyl urea compound is obtained with high yield and high purity economically by simple process, without causing pollution to environment.    DETAILED DESCRIPTION - A 1,3-cyclohexyl-1,1-dimethylurea compound of formula (I'), is new.    m,n=0 or 1;and    X=H, halo, hydroxy or sulfonyloxy.    An INDEPENDENT CLAIM is included for preparation of 1,3-cyclohexyl-1,1-dimethylurea compound (I').
NOVELTY - The equipment has a source gas (G) that contains methane and nitrogen. A nitrogen separation unit (13) separates nitrogen into a source gas supply unit from the source gas. A gas introducing unit (21a) introduces a noble gas (A) such as argon gas supplied from an outside into the source gas with which nitrogen is separated in the nitrogen separation unit. A de-oxygenation unit (12) separates oxygen into source gas supply unit from source gas. A noble-gas flow regulating valve (21c) adjusts the flow volume of noble gas to a noble-gas supply path (21).    USE - Equipment for treating gas such as global warming gas.    ADVANTAGE - The introducing unit introduces noble gas such as argon gas supplied from an outside into the source gas with which nitrogen is separated in the nitrogen separation unit from source gas in the state which when oxygen does not coexist so that the oxygen is separated in the de-oxygenation unit and returned by source gas easily and reliably without separation of nitrogen from source gas inhibited by oxygen and after nitrogen is separated in nitrogen separation unit so as to decompose the methane contained in source gas by non-equilibrium plasma using oxygen in gas treatment unit. Thus, the gas is treated efficiently by reduced energy while increasing the gas permeation area of gas permeable film and improving the separation rate and conversion capability of methane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the gas treatment equipment. (Drawing includes non-English language text)    De-oxygenation unit (12)    Nitrogen separation unit (13)    Noble-gas supply path (21)    Gas introducing unit (21a)    Noble-gas flow regulating valve (21c)    Noble gas (A)    Source gas (G)
NOVELTY - Accumulation of energy in electrical power network involves hydrolyzing hydrogen-containing compound using water, obtaining hydrogen used as fuel, decomposing water, mixing the resultant material with carbon dioxide in a reactor and reacting using catalyst, and producing methanol. The reaction process involves reacting carbon dioxide with 3 moles hydrogen and obtaining methanol and water.    USE - Accumulation of energy in electrical power network (claimed).
NOVELTY - The method involves introducing steam into a pressure-reduced reaction tube (5). Water plasma is formed by irradiating microwave into the pressure-reduced reaction tube. Biomass is decomposed by throwing-in biomass to the water plasma formation part (x) of the pressure-reduced reaction tube. The produced fuel gas is collected.    USE - Method for collecting fuel gas, such as hydrogen and carbon monoxide, from biomass using microwave non-equilibrium plasma.    ADVANTAGE - Biomass can be directly reformed to fuel gas without pre-processing. The production of carbon dioxide can be suppressed and fuel gas, such as hydrogen and carbon monoxide, can be produced with high yield.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating an apparatus for collecting fuel gas from biomass using microwave non-equilibrium plasma.    Microwave oscillator (1)    Reaction tube (5)    Vacuum pump (6)    Sample container (11)    Water plasma formation part (x)
NOVELTY - The hydrogen oxygen generator (X) has a water-electrolysis unit (2) that is provided for electrolyzing water and generating hydrogen and oxygen. A hydrogen side gas-liquid separation unit (4) is provided for separating water discharged from the water-electrolysis unit with the hydrogen from the hydrogen using the surface tension of a liquid. An auto drain unit is provided with a separation-water inflow unit and a valve unit which opens and closes automatically according to internal water level height.    USE - Hydrogen oxygen generator.    ADVANTAGE - The hydrogen oxygen generator is provided for electrolyzing water and generating hydrogen and oxygen efficiently. The operational efficiency of the hydrogen oxygen generator is improved. The hydrogen oxygen generator is formed of a simple structure and made compact. Since hydrogen oxygen generator is small and cooled easily, the gas-liquid separation unit can reduce the water vapor volume entrained to hydrogen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen oxygen generator. (Drawing includes non-English language text)    Water supply unit (1)    Water-electrolysis unit (2)    Oxygen side gas-liquid separation unit (3)    Hydrogen side gas-liquid separation unit (4)    Hydrogen oxygen generator (X)
NOVELTY - Producing a combustible log comprises: drying coffee pomace to a moisture content of 10-20%; mixing the dried pomace with a combustion agent and a cohesion agent and combustion regulator, with a rate of pomace of 50-65%; and extruding through an extruder with heating to obtain a log with a density of 800-1100 kg/m3.    USE - The method is useful for producing a combustible log.    ADVANTAGE - The method provides the combustible log that: has high proportion of coffee pomace and free of cellulosic fibers; exhibits slow and steady combustion for prolonged time; and produce firelights in safe and environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a combustible log obtained by implementing the method, where the combustible log comprises fuel composition comprising 58-62% coffee pomace, 34-37% combustion agent, and 4-8% cohesion agent and combustion regulator.
NOVELTY - A separation membrane comprises an inorganic porous support, an intermediate layer containing polysiloxane mesh structure formed on surface of the inorganic porous support, and a separation layer containing hydrocarbon group-containing polysiloxane mesh structure formed on the intermediate layer.    USE - Separation membrane is used for treating mixed gas containing acidic gas and methane gas and/or nitrogen gas.    ADVANTAGE - The separation membrane enables efficient treatment of mixed gas containing acidic gas and methane gas and/or nitrogen gas, and provides high-purity product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of separation membrane.
NOVELTY - A phospholipid alpha -linoleic acid-containing composition comprises 30 %mass or more phospholipid alpha -linoleic acid extracted from yeast and comprising phosphonyl group-containing compound (I).    USE - Composition is used as fatty acid composition, functional food, or pharmaceutical (all claimed) and cosmetic used for preventing and treating nonalcoholic fatty liver disease, and reducing blood glucose level and triglycerides.    ADVANTAGE - The phospholipid alpha -linoleic acid-containing composition can be manufactured by economical process with reduced generation of waste material.    DETAILED DESCRIPTION - A composition comprises 30 %mass or more phospholipid alpha -linoleic acid extracted from yeast and comprising phosphonyl group-containing compound of formula (I).    R1,R2=H or fatty acid, in which at least one of R1 and R2 is fatty acid;and    X=choline residue, ethanolamine residue, inositol residue or serine residue.    An INDEPENDENT CLAIM is included for fatty acid composition, which comprises 30 %mass or more alpha -linolenic acid.
NOVELTY - A solid acid catalyst is obtained by introducing sulfonic acid group into petroleum coke.    USE - Solid acid catalyst is used in manufacture of petrochemical, pharmaceutical, bioethanol and biodiesel.    ADVANTAGE - The solid acid catalyst has excellent catalytic activity, and is manufactured with high yield by simple process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of solid acid catalyst, which involves processing petroleum coke in sulfuric acid or fuming sulfuric acid at 20-300 degrees C.
NOVELTY - A thionocarboxylate compound (II) is reacted with halogen-containing compound (III) to obtain oxydifluoromethylene skeleton-containing compound (I).    USE - Manufacture of oxydifluoromethylene skeleton-containing compound used as intermediate for liquid-crystal material and pharmaceuticals.    ADVANTAGE - The method efficiently and economically provides oxydifluoromethylene skeleton-containing compound with high yield without using dibromodifluoromethane or highly toxic raw material, by simple process, and without generating any impurities which are difficult to separate.    DETAILED DESCRIPTION - A thionocarboxylate compound of formula (II) is reacted with halogen-containing compound of formula: XFn (III) to obtain oxydifluoromethylene skeleton-containing compound of formula: Ar2-Z-Ar1 (I).    X=chloro, bromo or iodo;    n=1-5;    Ar1,Ar2=aryl, cycloalkyl or alkyl (all optionally substituted);and    Z=-CF2-O-.    An INDEPENDENT CLAIM is included for manufacture of oxydifluoromethylene skeleton-containing compound of formula: Ar5-Ar6-Z-Ar7 (9-1) or Ar8-Z-Ar9-Ar5 (9-2), which involves reacting thionocarboxylate compound of formula (1-1) with halogen-containing compound (III), and then reacting obtained compound with boronic acid group-containing compound of formula: Ar5-D'.    Ar5,Ar8=Ar1;    Ar6,Ar7,Ar9=optionally substituted bivalent hydrocarbyl;    at least one of Ar3 and Ar4=group which has reactivity with respect to boronic-acid compound, or atom or group which has boronic acid group as substituent, and other is aryl, cycloalkyl or alkyl (all optionally substituted);    D'=boronic acid group of formula: -B-C(-OM2)(-OM3);    M2,M3=H, lower alkyl or monovalent metal atom;and    or M2+M3=bivalent aliphatic hydrocarbyl or cyclic structure with boron atom.
NOVELTY - The gasification reactor comprises an atmospheric gasification reactor fixed bed with variable geometry, an unbalanced motor coupled to the reactor, and a system for use of combustible gas for power generation. The gasification reactor with variable internal geometry includes convergent-divergent nozzle, and convergent bottom for better accommodation of biomass. The internal geometry reactor includes a negative angle inside the reactor, where the negative angle reduces velocity of hot gases from oxidation of condensable hydrocarbon.    USE - Gasification reactor for biomass for generating electrical, mechanical or thermal energy (claimed).    ADVANTAGE - The gasification reactor produces a better quality gas fuel having a composition with lower tar ratio, and provides a more stable operation for long periods of time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic arrangement of the reactor.    Reactor (1)    Gas cleaning system (6)    Generator (9)
NOVELTY - The device has a core comprising an array of wires, where the wires comprises first inorganic semiconductor material. A conformal coating is placed on the array of wires of the core, where the conformal coating comprises second inorganic semiconductor material. Each of the first and second inorganic semiconductor materials is independently selected from a group consisting of group IV elemental semiconductors, group IV compound semiconductors, III-V semiconductors and II-VI semiconductors. The wires of the array comprise length greater than about 100 nano meters (nm).    USE - Device for generating photoelectrochemical fuel i.e. solar fuel such as syngas or hydrogen in transportation applications.    ADVANTAGE - The device enables embedding wire arrays in a polymer matrix and removal from a substrate to allow the substrate to be reused in contrast to planar wafers, thus reducing cost. The device allows use of multiple photons without loss in efficiency, and has improved efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a photocathode including p-silicon rods decorated with particulate metal electrocatalysts.
NOVELTY - An open metal carbonyl cluster is prepared by chemically reacting closed metal carbonyl cluster and opening agent which reacts with bound carbonyl group to unbind it from the cluster and leave behind CO-labile ligand on the cluster.    USE - Preparation of open metal carbonyl cluster used as a catalyst in chemical catalytic reaction (claimed).    ADVANTAGE - The resulting cluster is stable but can be easily recarbonylated. The catalyst made from the open metal carbonyl cluster is stable and has improved catalytic activity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) open metal carbonyl cluster which is supported on a catalyst support;    (2) chemical catalytic reaction which involves conducting chemical reaction in the presence of open metal carbonyl cluster;    (3) chemical catalytic reaction which involves conducting chemical reaction in the presence of supported and treated open metal carbonyl cluster; and    (4) preparation of open metal carbonyl cluster which involves chemically reacting closed metal carbonyl cluster and opening agent which reacts with bound carbonyl group to unbind it from cluster and leave behind a CO-labile ligand on the cluster, and removing CO-labile ligand to create vacant sites.
NOVELTY - Fertilizer comprises an organic porous, swellable biomass structure of cellulose, hemicellulose and/or lignin material, or their derivatives, which is treated with at least one mineral nutrient composition, dissolved nitrogen, phosphorus and potassium compounds.    USE - Used as a fertilizer.    ADVANTAGE - The fertilizer: is a long-term fertilizer and improved to optimize the bioavailability of nutrients and at the same time mitigates the environmental problems; ensures reduced nutrient use yielding a comparable or higher level of earnings, and thus achieving significant cost savings; and prevents leaching of nutrients into groundwater. The biomass structures are very readily available to be used in the fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for improving the bioavailability of nutrients for plants, comprising firstly preparing a slow-release fertilizer by a porous, swellable biomass structure of cellulose, hemicellulose and/or a lignin material, or their derivatives, which is treated with at least one mineral nutrient composition, dissolved nitrogen, phosphorus and potassium compounds, such that the dissolved nutrients are stored in the biomass structure, and providing the obtained fertilizer obtained to the plants or plant components to be treated.
NOVELTY - Dehydrating coal sludge prepared by hydrothermal carbonization of biomass, comprises supplying heat for a device for dehydrating.    USE - The method and the device are useful for dehydrating coal sludge prepared by hydrothermal carbonization of biomass (all claimed).    ADVANTAGE - The method avoids deposition of oil on parts of the device, improves durability of the device, is economical, and does not exceed the saturation point.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for performing the above method.
NOVELTY - The utility model claims a new high efficient continuous biomass carbonizing furnace, comprising has a combustion chamber provided with a refractory lining in a furnace body, comprising a tube type air nozzle, by a grid and/or net grid composed of a furnace grate form a rigid cage bear fire ignition chamber, the furnace body and the combustion chamber below the conveying shell, flashboard valve, spiral conveyor, a spray nozzle of the spray device and bracket. This new utility model not only can make the biomass coal forming continuous carbonization, and increase the surface quality, a continuous removing coal and biomass in a biomass carbonizing process, but also production efficiency high, is easy to operate and implement.
NOVELTY - This new utility model claims of one fuel of down feeding biomass gasification furnace and a furnace body, wherein comprises furnace, hearth, hearth chamber body, hearth bottom and hearth bottom is equipped with hearth port, feeding the feeding passage divided feedstock pipe (10) and feedstock bucket (33) two part, feedstock bucket (33) upper part and feedstock pipe (10) sliding connect, using first translated upwards and feeding movement way, wherein the feedstock pipe (10) the upper part pipe body or feedstock pipe (10) of whole pipe body and the whole shape is big end up. The utility model use new feedstock passage is open, and decrease feedstock; cracking and combustion channel for tightening type, and add to collection of fuel gas. Reduction layer increase unit volume fuel comprising the heat, the carbon dioxide reduction as can combustion of carbon monoxide.
NOVELTY - The bottom a utility model claims a a fuel down feeding of the biomass gasification furnace is a furnace structure, combined (22-2), combined type (22-2) is set with furnace port, a side wall provided with a plurality of a wind hole (21-2), fire sleeve, outlet sleeve and a formula (22-2) is a wall form a sleeve type structure, the air outlet direction of a furnace air inlet passage, wherein the air inlet channel outlet furnace lining inner wall is of a lower big cone pipe wall, composed of a bottom upper furnace mouth and a furnace adjacent, and combined (22-2) outlet and the bushing is axial direction relative the cone pipe wall upwards inclined;. a wind hole (21-2) directly or through indirect belt and air or blowing device connected. A shortening of ignition timing and increase energy saving rate...
NOVELTY - The utility model claims a new biomass grain combustion of gas generator. Mainly solves the existing gasification furnace ignition difficult ignition period with large amount of flue gas discharge, gasification reaction unstable problem equal. Wherein, the middle part periphery of inner housing has a heat exchanger (16), heat exchanger (16) is provided with the middle facing wind cap (15), wind cap (15) is a chamber (6), wind cap (15) and fire grate (11) is between the combustion chamber (33), (11) bottom is ash chamber (9), a main box (21) and bottom discharging port connected with a feedstock (23), and a reaction chamber of the feedstock pipe (23) (6). The biomass particle combustion gas generator ignition is easy, quick, adjustable, stable combustion, a continuous production.
NOVELTY - The utility model claims a of a kind of a gasification furnace, comprising out bucket and inner bucket, the inner bucket equipped with a gasification chamber, a bucket top end provided with a chip and outside bucket in same diameter of backing a bucket top provided with a gas nozzle, the gas nozzle is a gasification chamber connected with, the top terminal of the outside bucket equipped with a way, a way a set provided with flame cover cylinder, the outside bucket is a bucket set. e. Internal backing and top end of the out bucket combined forming solid fuel combustion chamber, and the solid fuel combustion chamber along a provided with a week of vent hole, the utility model is a new easy ignition, the combustion process in a smoke, the fire power is stronger, the manufacture is simple, the cost is low, and it is very suitable for domestic cooking and warming of rural user equal, too is suitable for agriculture and processing a power obtained.
NOVELTY - The device has a methyl alcohol water hydrogen production reforming device (1) connected with a high temperature proton exchange film fuel battery (2), where temperature of the high temperature proton exchange film fuel battery is about 125-170 degrees Celsius. The methyl alcohol water hydrogen production reforming device, the high temperature proton exchange film fuel battery and a power supply switching module i.e. DC/DC power conversion module, are arranged in an inner side of a machine cabinet.    USE - Non-hydrogen purifying device for a reforming hydrogen fuel cell power generation module.    ADVANTAGE - The device reduces palladium gold cost and avoids platinum gold catalyst carbon monoxide poisoning problems by using the high temperature proton exchange film fuel battery.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a non-hydrogen purifying device.    Methyl alcohol water hydrogen production reforming device (1)    High temperature proton exchange film fuel battery (2)
NOVELTY - The new type utility claims have one power plant heat bath furnace type hydrogen production by reforming device, comprising feeding device (1), pipeline (2), vaporizing chamber (4), the reforming room (5), the collected hydrogen device (7), electric heating device (8), also comprises bath furnace (3), a liquid mineralized (6), vaporizing chamber (4), the reforming room (5), electric heating device (8) is set with bath furnace (3) and containing space inside, liquid mineralized (6) fill in bath furnace (3) and containing space inside, liquid mineralized (6) in temperature is 100 degree to 300 degree when is liquid pipeline (2) in turn connected with feeding device (1), vaporizing chamber (4), the reforming room (5), the collected hydrogen device (7). The utility model is new type by using liquid mineralized replaced air as heat exchanging medium, that have hydrogen production by reforming device heated not uniformly and stopping again starting time longer the problem, which is applied to water hydrogen production by reforming methanol, especially applied for fuel cell electric vehicle on the made hydrogen device.
NOVELTY - Manufacturing an organic fertilizer product, comprises providing an animal waste composition comprising an animal waste, contacting the animal waste composition with an acid to produce a stabilized animal waste composition, aerating the animal waste composition, and separating a solid component and a liquid component of the stabilized animal waste composition.    USE - The process is useful for manufacturing an organic fertilizer product (claimed).    ADVANTAGE - The process provides the organic fertilizer product that: is free from or substantially free from pathogens (claimed), and contain no phytotoxins or other plant growth retarding substances; is economical and fulfils all current USDA requirements for an organic fertilizer; has a controlled or predetermined phosphorus level, thus helping in preventing the oversaturation of phosphorus materials in soils; nourishes the soil in a natural manner; provides a balanced release (i.e. slow and fast release) of nutrients; establishes improved water retention of the soil; improves soil porosity; and delivers deeper root penetration of nutrients.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an organic fertilizer product prepared by the method.
NOVELTY - A one methanol fuel catalytic splitting stove for reactor, composed of multi-layer metal of tube plate, the tube plate is trapezoid structure, the ladder-shaped structure plate bottom semi-diameter inner pipe in turn, and the ladder-shaped structure plate pipe upper part pipe body fill in block exchange heat, the lower part tube body filling methyl alcohol splitting catalyst, plate pipe upper part opening connected with methyl alcohol liquid, plate pipe lower part outlet connected methanol burner of gas cooker. Set with fixing block used for heat changing agent and methyl alcohol splitting catalyst and porous grid plate in on tube plate. The utility model is new type use have methyl alcohol stove core and combustion product of using waste heat gasification methanol, the methanol after gasification again generating catalytic reaction generating carbon monoxide and hydrogen and set in the splitting catalyst in stainless steel tube around the stove core, thus generated gas mixture of carbon monoxide and hydrogen also has excess and unreacted gaseous state methyl alcohol again relux entering into methyl alcohol stove core matching liquid methyl alcohol together. Using low heat value liquid fuel sublimation for gas fuel of high heat value, radically improving have combustion efficiency and effect, test proves that mixed gas combustion full combustion temperature is much higher than methanol, under same condition methanol consume amount can be descending is about 10%.
NOVELTY - The train has a methyl alcohol water hydrogen production reforming fuel cell power generation system for generating electric energy by a driving motor. The methyl alcohol water hydrogen production reforming fuel cell power generation system is provided with a methyl alcohol water storage tank. A hydrogen production reforming device is connected with a fuel cell i.e. high-temperature proton exchange film fuel cell. The methanol water storage tank is connected with the hydrogen production reforming device. The fuel cell is equipped with a hydrogen purifying device.    USE - Methyl alcohol water hydrogen production reforming fuel cell electric train.    ADVANTAGE - The train prevents high pressure hydrogen from being danger and high-pressure hydrogen storage from being dangerous and increases safety of methanol water and quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a methyl alcohol water hydrogen production reforming fuel cell electric train.
NOVELTY - The system has a solid material gasification tube (B2) connected with a waste heat guide pipe (B3) and fixed with a high temperature steam generator (C) that is connected with a pipeline. A dual rotational flow slow speed multi-liner water film desulfurization dust remover (A) is connected with a rotational flow stub (A6). A wall of an ascending liner (A1) is formed with a hole (A5). A drain electric control valve (A10) is connected with a sewage filter tank (A11). A high temperature water vapor spraying pipe (B1) is connected with the solid material gasification tube.    USE - Dual air channel collision mineral or biomass water catalytic fuel preparation system.    ADVANTAGE - The system has high material utilization efficiency. The system improves combustion waste gas and smoke gas flow speed, utilizes gas square meter, ensures production mineral or biomass water catalytic fuel safety and performs collision catalytic reaction energy level matching process to obtain dual channel collision catalyst water fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a dual air channel collision mineral or biomass water catalytic fuel preparation system.    Dual rotational flow slow speed multi-liner water film desulfurization dust remover (A)    Ascending liner (A1)    Hole (A5)    Rotational flow stub (A6)    Drain electric control valve (A10)    Sewage filter tank (A11)    High temperature water vapor spraying pipe (B1)    Solid material gasification tube (B2)    Waste heat guide pipe (B3)    High temperature steam generator (C)
NOVELTY - The device has an air extracting pump (17) and a coal online analyzer (18) that are fixed with each other. A nitrogen bottle (1) is connected with a sump force feeder (9) through a nitrogen quality flow rate controller (3). A pneumatic feeder is connected with an air flow bed gasification furnace (10) and an oxygen bottle (2). A first pre-heater (5) is connected with a water steam generator (8). A second pre-heater (7) is connected with the air flow bed gasification furnace. A bottom part of the air flow bed gasification furnace is mounted with a pressure meter (26).    USE - Air flow bed gasification biomass preparing synthesis testing device.    ADVANTAGE - The device has high temperature conversion efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an air flow bed gasification biomass preparing synthesis testing device.    Nitrogen bottle (1)    Oxygen bottle (2)    Nitrogen quality flow rate controller (3)    Pre-heaters (5,7)    Water steam generator (8)    Sump force feeder (9)    Air flow bed gasification furnace (10)    Air extracting pump (17)    Coal online analyzer (18)    Pressure meter (26)
NOVELTY - The method involves performing a dry distillation and gasification process in a bi-section biomass dry distillation gasification device. A gasification furnace is utilized for supplying high temperature steam gasification of biomass and high temperature air gasifying agent. A dry ash-out seal sum chamber is connected with the gasification furnace for performing a gasification process. A gasification sum processing module is connected with a fan to pump fuel sum generation by performing cooling and filtering processes.    USE - Biomass bi-section dry distillation gasification method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass bi-section dry distillation gasification device.    DESCRIPTION OF DRAWING(S) - The drawing shows a pneumatic circuit diagram of a biomass bi-section dry distillation gasification device. '(Drawing includes non-English language text)'
NOVELTY - The apparatus has a primary channel reformed with a reforming catalyst. Fuel gas of the primary channel is burnt with the combustion catalyst. Stack exhaust gas is flowed between the primary channel and a secondary channel. Air flows away contrary is mixed to the stack exhaust gas. A cooling part is formed with a heating portion. The fuel gas is reformed in the primary channel by using a combustion unit. Another cooling part is cooled with reformed fuel gas. Combustion gas is reformed by performing water-gas shift reaction.    USE - Fuel post processing and heat exchange apparatus for a system-on-chip (claimed) of a fuel cell.    ADVANTAGE - The apparatus selects position of reforming catalyst and combustion catalyst so as to provide heat-exchange along forward and backward directions. The apparatus saves energy consumption, reduces heat loss and increases thermal efficiency, and is simple in design and convenient in operation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a fuel post processing and heat exchange method    (2) a system-on-chip.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel post processing and heat exchange apparatus.
NOVELTY - Method for producing 1,5-pentamethylenediamine, involves using L-lysine and/or its salt and a mutant lysine decarboxylase having lysine decarboxylation activity and having a mutation in at least one amino acid residue causing increased thermal stability in one of the amino acid sequences includes a 715 amino acid sequence (SEQ ID NO: 1) fully defined in the specification.    USE - The method or microorganism, preferably Escherichia coli is useful for producing 1,5-pentamethylenediamine (all claimed) which is used as resin raw materials, preferably polyamide resin, or pharmaceutical intermediate.    ADVANTAGE - The method is suitable for industrial production of 1,5-pentamethylenediamine in an environmentally-friendly manner.    DETAILED DESCRIPTION - Method for producing 1,5-pentamethylenediamine, involves producing 1,5-pentamethylenediamine from L-lysine and/or its salt by using a mutant lysine decarboxylase having lysine decarboxylation activity and having a mutation in at least one amino acid residue causing increased thermal stability in one of the amino acid sequences chosen from (a) a 715 amino acid sequence (SEQ ID NO: 1) fully defined in the specification, (b) an amino acid sequence in which one or more amino acid residues are substituted, deleted, inserted or added in the amino acid sequence of SEQ ID NO: 1, or an amino acid sequence exhibiting at least 90% sequence identity to the amino acid sequence of SEQ ID NO: 1. The amino acid sequence is substituted with one or more amino acid residues at Val in 3rd position, Ala in 590th position, and Glu in 690th position. INDEPENDENT CLAIMS are included for the following:    (1) mutant lysine decarboxylase which improved thermal stability;    (2) polynucleotide which codes the mutant lysine decarboxylase;    (3) expression vector comprising the polynucleotide; and    (4) microorganisms comprising the expression vector.
NOVELTY - A molecular sieve comprises a layer of perforated graphene or graphene-based material, provided on a polymer backing.    USE - Molecular sieve is used as filter for separating water from aqueous solution, and methane, ethane, propane and butane from oil-gas mixture (all claimed).    ADVANTAGE - The molecular sieve having excellent tear resistance and high adsorption capacity is manufactured efficiently with high productivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of molecular sieve, which involves growing graphene or graphene-based material on a growth substrate, applying polymer to the graphene or graphene-based material, removing the growth substrate from the graphene or graphene-based material, perforating the graphene or graphene-based material on the polymer, and forming a macrotube by winding the perforated graphene or graphene-based material and the polymer into a spiral shape; and    (2) method for filtering using molecular sieve, which involves contacting a crude fluid with an interior or an exterior of the macrotube of the molecular sieve.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of graphene-based molecular sieve.
NOVELTY - A microbe comprising overexpressed magnesium transporter gene and overexpressed transposable element (TE) gene, is new.    USE - The microbe is useful for producing free fatty acids (claimed). The microbe includes bacteria, yeast, and algae, preferably is Aeropyrum pernix, Agrobacterium tumefaciens, Anabaena, Candida glabrata, Canis familiaris, Gallus gallus, and Geobacter sulfurreducens.    ADVANTAGE - The method is simple and cost-effective, and consumes minimal energy. The microbe has improved viability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of producing free fatty acids, which involves (a) (i) culturing the above-mentioned microbe having (1) overexpressed acyl carrier protein (ACP) thioesterase (TE) gene, and optionally (2) overexpressed magnesium transporter gene in a culture medium under conditions effective for production of free fatty acids, where the culture medium is supplemented with more than 20 mm magnesium (Mg), and (ii) harvesting the free fatty acids or its derivative from the microbe or the culture medium or both, where the more free fatty acids or its derivative are produced in the above-mentioned method than method without magnesium supplementation, (b) culturing the microbe in culture medium with at least 20 mm magnesium under conditions effective for the production of free fatty acids, and harvesting the free fatty acids from the microbe or the culture medium or both, or (c) culturing the above-mentioned microbe in culture medium with at least 20 mm magnesium, and harvesting the free fatty acids from the microbe or the culture medium or both, where more free fatty acids are produced in the method.
NOVELTY - A high concentration machine comprises one hydrogen oxygen generating mould, mould, electrolyte regulating module, the first pipeline and the second pipeline. Oxyhydrogen generating module comprises the first, the first air outlet and multiple of electrolytic cell, the electrolytic cell set with positive plate, a negative plate, a first electrolyte and the first liquid outlet mouth. Storage module comprises the second, pressure cover, the second electrolyte, air inlet pipe extends in the second electrolyte and, the second liquid outlet mouth and the second air outlet. The first pipeline connected oxygen generating module and the first air outlet and storage module and air inlet pipe, the second pipeline connected the first liquid injection mouth and storage mode hydrogen-oxygen generating module and the second liquid outlet mouth. Electrolyte regulating module containing third air outlet, third injection mouth and regulating pipe, the third air outlet connected to inner hydrogen-oxygen generating module, regulating pipe A fill end with electrolyte, regulating pipe is connected to each third, another end connected to the first liquid outlet mouth.
NOVELTY - Performing fractioned separation of products involves using a biomass supply system, a devolatilization reactor and a chemical components separation system provided for separating fractions to obtain product. The liquid biomass comprises lignin. A recovery system is provided for recovering nitrogen fertilizer, carboxylic acid ester and gases.    USE - Method for performing fractioned separation of products for obtaining fuels and chemical raw material resulting from biomass and energy source resulting from biodegradable biomass.
NOVELTY - The utility model is new type supply have one kind of kitchen garbage waste residue and tail sum of biochemical treatment system, wherein comprising: fermentation groove, the fermentation groove for closeness cavity body, the section is U type, the top of the fermentation groove set with feedstock wherein the side wall provided with the discharging mouth, outside of the fermentation groove orderly set with heating layer and heat preservation layer, the inner interlayer is provided with heating heat-conducting medium and heater, one end the fermentation groove and provided with an exhaust port, stirring shaft, the stirring shaft is set on the fermentation groove in, the upper stirring shaft provided with double spiral stirring leaf, one end the stir shaft is connected with driver, dust removing and odour removing purifier, the dust removing and odour removing purifier comprises main body, the main body in upper part provided with multiple spraying pipes are on each of the spray pipe connected with a plurality of shower nozzle, the inner main body from upper to lower in turn provided with filter layer, spray layer and activated coal layer, the main body is an air inlet and the fermentation groove pipeline connected with the air outlet to connected with a draught fan.
NOVELTY - The new type utility claims have one kind spiral straw fuel extrusion molding machine, by forming main rod, cone cylinder, a connecting flange, a pre-heater, a spiral extruding sleeve, adding hopper and driving shaft one, and the forming rod connected with cone cylinder, cone cylinder right side provided with connection flange, flange connected with right side provided with pre-heater and pre-heater connected with extruding sleeve, extruding inner sleeve provided with driving shaft, upper driven shaft inner sleeve set with spiral extruding, extruding sleeve at right deviation position provided with the hopper. The utility model is new type, reduce have the requirement for raw material water content, impurity water content gradient of spiral leaf material is easy to make, and rubber line and the charging barrel wall friction force enlargement, from hot temperature rise, in combined strength enhancement. Can change along with the mould, adjusting product specification variety, reduce machine abrasion. When the engine low speed continuous extrusion, no noise increase have production rate.
NOVELTY - The new type utility claims have one plant marsh gas dejecta dehydration machine, it relates to one kind dejecta dehydration machine. It comprises pedestal, a universal wheel, machine tube, carrying on hopper, the feedstock tube, an overflow tube, a push rod, a dry material outlet, motor, separating liquid outlet and filter screen, bottom pedestal set with universal wheel, on pedestal set with dewatering machine tube, dehydrating machine tube one end upper part formed with carrying on hopper, hopper center for feedstock pipe is screwed, feedstock pipe upper end side also set with overflow pipe, machine tube another end bottom formed with separated liquid outlet, internal separating liquid outlet and dehydrating machine connected to set with tube filter screen, machine tube another end set with dry material outlet, machine tube set with spiral packing auger, a spiral packing auger and connected with motor and outlet also set with push rod. The utility model is new type structure is simple, suitable mobile, feedstock suitable reliability and strong practicability.
NOVELTY - The new type utility claims one kind from marsh gas heating circulation system, comprising marsh gas material device, marsh gas fermentation device, marsh gas purification device and marsh gas boiler, wherein the marsh gas material pre-processing device comprises first-stage treatment room and second grade treatment room, first processing room and between second level treatment room set with channel connected by the second level internal process room set with pumping pipeline and marsh gas fermentation device connected, the top part of the marsh gas fermentation device provided with marsh gas pipe and gas purification device connected, the gas purification device and marsh gas boiler connected; heating the methane boiler pipeline respectively extending to one level processing room, second level processing room and marsh gas fermentation device internal. The utility model is new type marsh gas from the heating circulation system, caused by the marsh gas boiler can heat to biogas material pre-processing device and marsh gas fermentation device for heating to promote efficiency pre-treated biomass material, and increase speed of fermentation, using the marsh gas fermentation process more efficient and fast.
NOVELTY - The new type utility claims have double binding Anaerobic marsh gas fermentation system, of feedstock tube, discharging tube, pipe and water pressure in fermented fermentation system composed of main body, pipe respectively connected with fermentation feedstock pipe and discharging pipe two end side, to up to fermentation pipeline connected with air pipe, pipeline and fermentation feedstock tube and connecting seat set with feedstock tube plate, fermented pipe and discharging pipe connecting seat is set with discharging pipe plate, placing for fermentation pipe of upper part, between hydraulic pressure between feedstock tube and connected with horizontal placing feedstock pipe and drain pipe, water pressure and discharging pipe connecting with horizontal placing and discharging pipe drain pipe, water pressure in upper part adopt seal formed, and water pressure in upper part connected one discharge tube, using air pressure difference realization biogas slurry in circulation in the fermentation system, no need to add power not only can realize circulation stirring the biogas and biogas slurry in circulation flow process to promote uniform distribution of strain, further increase fermentation efficiency of fermentation system.
NOVELTY - The new type utility claims have double binding Anaerobic marsh gas fermentation system and promoting feedstock device, of feedstock tube, discharging tube, pipe and water pressure in fermented fermentation system composed of main body, pipe respectively connected with fermentation feedstock pipe and discharging pipe two end side, to up to fermentation pipeline connected with air pipe, pipeline and fermentation feedstock tube and connecting seat set with feedstock tube plate, fermented pipe and discharging pipe connecting seat is set with discharging pipe plate, placing for fermentation pipe of upper part, between hydraulic pressure between feedstock tube and connected with horizontal placing feedstock pipe and drain pipe, water pressure and discharging pipe connecting with horizontal placing and discharging pipe drain pipe, water pressure in upper part adopt seal formed, and water pressure in upper part connected one discharge pipe, bottom of fermentation pipeline set with slope, the higher end side of slope the feedstock tube bottom, the lower end of the slope side discharging pipe bottom, using air pressure difference realization biogas slurry in circulation in the fermentation system, no need to add power not only can realize circulation stirring the biogas and biogas slurry in circulation flow process to promote uniform distribution of strain, further increase fermentation efficiency of fermentation system.
NOVELTY - The utility model is new type belongs to kitchen garbage made marsh technology field, especially relates to kitchen garbage Anaerobic fermentation hydrogen producing methane made integrated device, comprising producing acid tank, kitchen garbage material, methane tank, a marsh gas purifying device and circulation pool, the kitchen waste material set at the production tank in, producing the methane tank and the acid producing tank connected, the biogas purifying device and the methane production tank connected, said circulation water tank respectively and connected with the acid producing tank and producing the methane tank, the methane production tank connected with acid alkali regulating flat device. Wherein when carrying out test, when producing methane tank when the PH value is too low then show initiating production, the acid alkali regulating flat device would automatically administering to adjust, make production in methane tank and PH value recover normal, to make methane tank and production yield stable, would not show the acid accumulation excess then production rate caused by the descending problem.
NOVELTY - The new type utility claims have one pole A electrolytic groove, belonging to tritium containing heavy water treatment equal field. The electrolytic groove main comprises outside cylinder, inside cylinder, oxygen outlet pipe, hydrogen outlet pipe, an alkali liquid inlet pipe, ceramic sealing component, and control unit, the ceramic sealing component comprises ceramic ring and flexible graphite cushion block I, the ceramic insulation component comprises ceramic pipe, a cutting sleeve bolt and flexible graphite cushion block. Ceramic ring ceramic sealing component of embedded tube part in cylinder is sleeved on outside the internal cylinder, inner cylinder open end between the end face and outside cylinder bottom is closed end; said flange cover and flange matching connecting mutually, wherein inner sealing groove, and set with flexible graphite cushion block I between on end face sealing groove and the ceramic ring, hydrogen sum outlet pipe, on oxygen outlet pipe and electrolyte entrance pipe are set with ceramic insulation module. The electrolytic groove structure simple, the assembly is suitable, radiation bear and bear strong alkali corrosion, it is suitable for tritium containing heavy water treatment, and using life longer.
NOVELTY - The new type utility claims have one kind based on distributed type cold hot electric connect the system of biomass sum, generating power drive electric generator power generation by fuel gas internal combustion engine, at the same time for internal combustion engine and generating high temperature smoke sum into the fume hot water and lithium-bromide absorption type cold warm water unit finish cooling and supply heat. Use water cold and internal combustion engine generator set water cooling each combined jar and method for preparing domestic hot water, at the same time it also can as supplementary heat source driven absorption unit for preparing cold and heat. A another aspect internal combustion engine waste heat also can used for constant temperature fermentation of marsh gas, marsh gas high efficient continuous stable production. Based on cold heat electric connect the system of biomass sum realize energy step use, full recovery using biomass organic matter fermentation biogas generated, active release atomphere pollute.
NOVELTY - Preparation of strawberry wrap film involves using waste residue of Chinese herbal medicine as raw material, subjecting the raw material to hot-water extraction and ultrasonic extraction, extracting active components in raw material, and blending resultant with edible gelatin solution.    USE - Preparation of strawberry wrap film (claimed).    ADVANTAGE - The strawberry wrapped using the environmentally-friendly film provided by the method has excellent freshness.
NOVELTY - Spinach-carrot composite nutrient drink comprises 90-100 pts. wt. carrot, 3-4 pts. wt. sodium hexametaphosphate, 10-15 pts. wt. spinach, 10-15 pts. wt. celery, 1-2 pts. wt. cellulase, 1-2 pts. wt. seasoning, 1-2 pts. wt. white sugar, 1-2 pts. wt. angel yeast, 2-3 pts. wt. Lactobacillus plantarum, 0.1-0.2 pt. wt. sodium alginate, and water, and is prepared by fermentation.    USE - Spinach-carrot composite nutrient drink is used for providing antiaging effect, tonifying liver, improving eyesight, reducing blood sugar, nourishing liver and kidney, nourishing blood, moistening lungs, and enhancing immunity.    ADVANTAGE - The spinach-carrot composite nutrient drink has excellent flavor, is rich in nutrition, and can be prepared by a simple, energy-saving and environmentally-friendly method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of spinach-carrot composite nutrient drink.
NOVELTY - Traditional Chinese medicine healthcare beverage comprises 20-40 pts. wt., preferably 25 pts. wt. henon leaves, 10-20 pts. wt., preferably 15 pts. wt. Astragalus membranaceus, 10-30 pts. wt., preferably 20 pts. wt. Chrysanthemum, 10-20 pts. wt., preferably 15 pts. wt. reed rhizome, 5-15 pts. wt., preferably 8 pts. wt. Ophiopogon root, 5-15 pts. wt., preferably 10 pts. wt. medlar, and 3000-8000 pts. wt., preferably 5000 pts. wt. water.    USE - Traditional Chinese medicine healthcare beverage is used for clearing away heat, detoxifying, providing refresh feel, relaxing bowels, and quenching thirst.    ADVANTAGE - The traditional Chinese medicine healthcare beverage is free of antimicrobial agents, chemical additives, and preservatives, is natural, environmentally-friendly and nontoxic, and does not cause any side effects.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of traditional Chinese medicine healthcare beverage, which involves drying plant materials, soaking in water for 30 minutes, heat-extracting, boiling for 30-120 minutes, filtering, adding water, filtering, split-charging, sterilizing, and cooling.
NOVELTY - A traditional Chinese medicine composition comprises 85-100 pts. wt. Peganum harmala seed and 0-15 pts. wt. radix bupleuri.    USE - Traditional Chinese medicine composition used for preventing and treating chicken coccidiosis (claimed).    ADVANTAGE - The composition is environment-friendly and safe, and has small toxicity and side effect and no irritation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of traditional Chinese medicine composition comprising all mixing raw materials, crushing into coarse powder, adding water, extracting for 2 times for 2 hours, filtering, combining, statically standing for 12 hours, removing precipitate, and concentrating.
NOVELTY - A bio-purification agent comprises 15-90 wt.%, preferably 55-80 wt.% diatomaceous earth, 10-85 wt.%, preferably 20-45 wt.% humic acid, and 1-2 wt.% flocculating Bacillus.    USE - Bio-purification agent is used in treatment of sewage, drinking water, phenolic wastewater, oily wastewater, printing-and-dyeing wastewater, potato-starch production wastewater, pesticide production wastewater, and urban sewage, and cyanobacteria management.    ADVANTAGE - The bio-purification agent has a simple composition, can be prepared by a simple method, efficiently removes pollutants, and provides treated water with required discharge index.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of bio-purification agent, which involves stir-mixing all components uniformly.
NOVELTY - Organic fertilizer pellet comprises vegetables organic matter from arecaceae family, nutrient source (manure) and thermophilic bacteria degradation product.    USE - Organic fertilizer pellet used for recovering soil with nutrition deficiency (claimed).    ADVANTAGE - The organic fertilizer pellet improves soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer pellet, which involves;    (A) drying vegetable organic matter at room temperature to obtain moisture content of less than 3%;    (B) grinding dry organic matter to obtain an homogeneous mixture having average particle size of 3-5 mm;    (C) stacking homogeneous mixture in piles;    (D) adding source of nutrients to homogeneous mixture; and    (E) fermenting obtained mixture for 90-120 days in ambient conditions with thermophilic bacteria at 60 degrees C to obtain product.    .
NOVELTY - The utility model claims a biogas slurry multistage negative pressure volume reduction concentration device . With evaporation device, a condensing device, supply heat device, a negative pressure device and monitoring system composed of connection. The monitoring system so as to detect and control the vacuum degree in different level time evaporator in different magnitude, using water at its boiling point under different vacuum degree of different physical characteristics, low vacuum degree and generating the heat steam by the evaporator vacuum degree is high and the evaporator heat exchanger in heating biogas realize multistage heat more efficient use. Condenser and vacuum pump outlet are equipped with waste heat recovery system, realize circulation use of energy recovery, increase heat use efficiency, reduce energy consumption cost. Carrying out evaporation concentration to biogas slurry under low pressure at low boiling point, can avoid the biogas slurry effective component is damaged, biogas slurry realize non-destructive rapid concentration. The utility model is new type fit for popularization and application in sewage treatment, sea water desalination, extracting medicine equal large industrial field.
NOVELTY - Sludge conditioning agent comprises 10-33 pts. wt. molasses, 0.1-0.5 pts. wt. nitrogen source, 0.01-0.05 pts. wt. ammonium sulfate, 0.001-0.003 pts. wt. magnesium sulfate heptahydrate, 5-15 pts. wt. yeast liquid, 0.02-0.05 pts. wt. glucanase, 0.01-0.03 pts. wt. protease, 5-10 pts. wt. polymeric ferric sulfate and 67-90 pts. wt. water.    USE - Sludge conditioning agent.    ADVANTAGE - The sludge conditioning agent is economic, and promotes microorganism growth.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing sludge conditioning agent, which involves:    (A) adding water into molasses to obtain dilute molasses liquid;    (B) adding dilute molasses liquid into nitrogen source, ammonium sulfate and magnesium sulfate heptahydrate to obtain mixed liquid;    (C) sterilizing mixed liquid and then adding yeast liquid to obtain mixture;    (D) adding glucanase and protease into mixture and then fermenting mixture at 55-60 degrees C for 20-40 hours to obtain fermentation broth; and    (E) adding polymeric ferric sulfate into fermentation broth and then mixing to obtain the product.
NOVELTY - The utility model is new type relates to one kind separate frame cushion material chicken, comprising fermentation bed house and separating device, the fermentation bed for house for two inner side set with cushion material pool, between the two pad of material pool for two side channel is formed, the channel is set with groove, the separating device equipped with fermentation bed for house for two side, and the padding pool in, said separating device comprises two of each parallel set with the bracket, the bracket of two vertical rods and cloth are in multi-strip rod between two vertical pole is composed of transverse rod and the two bracket lower part set with one clapboard is inverted V shape. The henhouse structure is simple, it can effective solve the chicken manure processing problem, for growing the chicken providing have one of clean and sanitary and environmental.
NOVELTY - Constructing genetically modified Pichia pastoris involves integrating lipase encoding gene into the genome of Pichia pastoris, where lipase-catalyzed process takes place to obtain the finished product.    USE - Method for constructing genetically modified Pichia pastoris used for synthesizing biodiesel by lipase-catalyzed process (claimed).
NOVELTY - The methanol gasoline comprises 82-88 pts. wt. methyl alcohol, 2-4 pts. wt. modifier, and 10-14 pts. wt. heat value agent.    USE - Methanol gasoline.    ADVANTAGE - The methanol gasoline has strong power, and reduces energy consumption and provides complete cleaning of vehicle fuel injection system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing methanol gasoline, which involves:    (A) mixing ethanol, isopropanol, ethanol, and ethyl tert.-butanol in a reaction kettle with stirring;    (B) adding Tween 80, petroleum sulfonate, benzotriazole, and pyrazolone with stirring for 24 hours;    (C) mixing pentane, hexane, xylene, and petroleum ether in a reaction vessel; and    (D) adding the formed mixture with stirring for 24 hours to obtain the product methanol gasoline.
NOVELTY - The solid fuel composition comprises fruit residue, rice husk, clay, lime, phenol, carbon residue and water.    USE - Solid fuel composition.    ADVANTAGE - The solid fuel composition reduces energy consumption in a simple and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing solid fuel composition, which involves:    (A) smashing fruit residue and rice husk in a machine;    (B) heating the formed mixture at 150 degrees C;    (C) mixing clay, lime, phenol, residue and water to form a mixture;    (D) heating the formed mixture with stirring at 200-300 degrees C without oxygen for carbonization; and    (E) cooling the formed mixture at room temperature to prepare the finished product.
NOVELTY - The utility model is new type relates to one plant with pig manure biogas residue as fertilizer and production system, comprising pigsty, house bottom connected with grid grate, a grate grid channel and collecting pool connected with the collected sewage pool connected with the first regulating pool, regulating pool connected with the first second regulating pool, regulating pool and the second CSTR each connected with reactor, CSTR reactor and second time fermentation pool connected with the second time fermentation pool connected with concentrated pool, concentrated pool connected with solid-liquid separation machine. The utility model is new type of beneficial effect is: active of that have pig excrement sewage to environment and pollute, improve have ecological and environment, reducing have the disease happen, using livestock breeding industry chain elongating, reducing have use amount of chemical fertilizer and pesticide, chemical fertilizer and pesticide have caused by soil and pollute, structure is simple, the efficiency is high, the suitable operation, saves cost and space, which is good for sustainable development of economic and social, drive have the development of related industry, promoting have circulation use of resource, which is good for adjusting the energy structure of our country.
NOVELTY - The utility model is new type supply have one A processor for kitchen garbage, aiming at solve the problem of kitchen garbage resource waste and technology problem, comprising machine body, inside the machine body can be set with heat preservation and microorganism decomposing chamber, at least three of the microorganism decomposing chamber lower part and removing dirt. garbage microorganism decomposing chamber upper part set with garbage, microorganism decomposing chamber side is provided with fertilizer taking material wherein, microorganism decomposing chamber and wherein one of removing dirt chamber between for drainage is set with filter, wherein one of upper dirt removing chamber set with sludge discharge port, wherein one of removing dirt chamber provided with sewage discharge port; all dirt removing chamber connected in turn by water pipe. The utility model is new type of organic microorganism for degradation to the organic object in kitchen garbage in in microorganism decomposing chamber, residue can be directly used as fertilizer equal, bottom also with simple sewage treatment, sewage treatment after can be by direct in-situ pour flowers and trees. Use life longer, with light cost, no maintenance cost, with simple sewage treatment, floor space small, suitable mounting.
NOVELTY - The utility model is new type male relates to water hydrogen manufacture technology field and claims have one kind portable water hydrogen maker, including no bottom of tank body, and the tank body bottom connected with the bottom shell, the top of the tank body set with out water mouth, to set with water outlet cover body, inner wall of bottom shell provided with annular ring, annular baffle in the top to bottom respectively provided with upper plate, iron exchange film, lower plate, lower plate and bottom shell form air cavity and one of the side and bottom shell outside and set with discharge hole, discharge hole and gas storage cavity is connected with connected with discharge tube, discharge soft pipe outside end is provided with cover, the upper plate, the lower plate is network shape structure, inside the bottom shell also set with on circuit plate, circuit plate set with storage battery, through lead respectively and upper pole plate, lower pole plate connected with circuit plate on the outside side is provided with bottom shell and circuit board connected with the hydrogen water bottom. Therefore, the utility model is new type capable of manufacturing hydrogen with water, drink made with, carry suitable and beneficial effect, also can generate oxygen, oxygen suitable, relieving fatigue.
NOVELTY - The utility model claims a novel dry anaerobic digestion device for wine lees, comprising a reactor tank body (1) and mixing pool (8), wherein the reactor tank body (1) in two side respectively set with one layer or multiple layer side injection pipe (2) is one of or multiple of lateral injection pipe (2), a reactor tank body (1) internal the upper part provided with the injection pipe (5), a reactor tank body (1) front side provided with can opening seal door (4), and the top set with elastic (7) and discharge pipe (6), bottom set with collected liquid tank (3), a lateral injection pipe (2) and the injection tube (5) through pressure pump and mixing pool (8) connected with. The utility model increases mixture of inoculated sludge and wine lees in reaction, which avoids have use in stirrer in reaction, reducing have front process of wine grains, at the same time increase have unit volume gas yield. It can be used for high concentration lees and other organic waste water, treatment and energy recovery of solid waste.
NOVELTY - The utility model relates to a high-efficient Anaerobic type methane producing device, comprising a reaction kettle and collecting device, comprising a kettle body, a stirring device and carrying out heat preservation heating sleeve, top end of one mounting a stirring device, lower part of the stirring device is kettle body, kettle body upper part is set with pressure table, a thermometer and one time methane outlet, outside side of lower part of kettle body is wrapped set insulating heating sleeve, bottom of kettle body mounted residue; collecting device comprises a tank body, the top end of the tank body set with waste sum outlet, upper part of tank body set with quadratic methane outlet, the lower part of tank body set with one quadratic methane inlet, the one time air inlet and one alkyl alkyl time through pipeline connected with air outlet, bottom of jar body set with discharging mouth. The device quickly heating and keeping temperature constant, can bear with high temperature, corrosion resistance and sealing effect is good, sanitary without environment pollute, can continuous production for equal advantages, especially fit for mixture of straw and seed sludge for medium production methane gas and enterprise use.
NOVELTY - Method for producing biofuels, involves grinding fruit kernels, heating ground fruit kernel under reflux conditions in an alcohol, filtering residual solid obtained from the heating step, drying filtered residual solid, mixing the filtered residual solid with an acid solution, roasting the filtered residual solid and acid mixture, filtering roasted residual solid, and fermenting the filtrate to produce organic fuel.    USE - The method is useful for producing biofuels chosen from bioethanol and bioalcohol.    ADVANTAGE - The method efficiently utilizes waste materials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of fruit kernels for production of biofuels.
NOVELTY - Combustion plant oil comprises 36-44 pts. wt. plant oil, 4-6 pts. wt. potassium permanganate, 9-11 pts. wt. methanol, 9-11 pts. wt. ethanediol, 4-6 pts. wt. pentaerythritol, 9-11 pts. wt. sulfolane, 4-6 pts. wt. cyclohexane, 4-6 pts. wt. alkylphenol polyethenoxy ether, 9-11 pts. wt. ethanolamine, 19-21 pts. wt. zinc naphthenate, 5-15 pts. wt. modified additive and 6-10 pts. wt. lower ether.    USE - Combustion plant oil.    ADVANTAGE - The combustion plant oil is prepared in simple and energy saving manner and with high quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing combustion plant oil, which involves:    (A) adding plant oil and modified additive in a reaction vessel and then stirring the obtained material;    (B) adding the stirred material with potassium permanganate, sulfolane, cyclohexane, alkylphenol polyoxyethylene ether, ethanolamine, zinc naphthenate and lower ether;    (C) stirring the obtained material at 60-80 degrees C for 2-4 hours and then cooling the stirred material to 20-25 degrees C;    (D) adding the cooled material with methanol and ethanediol and then stirring the obtained material;    (E) standing the stirred material for 5-10 hours and then removing upper layer of clear liquid; and    (F) stirring the obtained material.
NOVELTY - The utility model is new type male relates to technology field of vacuum cup have one plant can heat preservation cup of water manufacturing oxygen and hydrogen, comprising outer cup, cover body, inner cup set with no inner cup, inner cup and outer cup bottom is set with annular insulating gap between lower end of cup with inner wall connected with the bottom shell, the bottom shell provided with annular ring, annular baffle in the top to bottom respectively provided with upper plate, iron exchange film, lower plate, side shell and set with discharge hole, inner end of discharge hole and gas storage cavity connected, discharge hole outside end connected with discharge pipe, outside end of discharge tube provided with cover, upper plate, lower plate is network shape structure, inside the bottom shell also set with on circuit plate, circuit plate set with storage battery, through lead respectively and upper pole plate, lower pole plate connected with circuit plate on the outside side is provided with bottom shell and circuit board connected with the hydrogen water bottom. Therefore, the utility model is new type can be manufacture with oxygen and hydrogen water, drink made with, carry suitable, carrying out heat preservation effect and good useful effect.
NOVELTY - A manual planting water grass type drain wherein water quality in situ purification device, comprising set is in the river-way drain mouth outlet pipe and outside pipe, river bottom seat set with plane spreading the aeration pipe, the aeration pipe is equipped with the first manual water upper part of belt, the first manual water belt, setting the first floating body, the upper end lower end aeration pipe and fixedly connected with the inner pipe and outside pipe composed of an annular water grass belt, laying with the inner pipe and connecting mechanism connected with the outside on the annular water pipe, with upper part connected with machine set with aquatic plant, on outside pipe set with anti-pollution, anti-dirt curtain and lower end set with suspension at river bottom of heavy object, the lower part inside the annular float grass belt is connected with machine set with the second manual grass with water, and the second manual water, with its upper end fixedly is connected with above structure, the second manual water, with its lower end set with suspension at river bottom of heavy object. Can be set with collective processing sewage, completely purification, good effect, contaminants remaining rate low, and not easy to pollute the advantages of whole channel.
NOVELTY - The patent application claims have one kind energy gradually using the organic fertilizer fermentation device, comprising fermentation tank, fermentation tank set with coil on the inlet plate and outlet pipe, plate pipe and water outlet pipe in turn connected with water heating, water heating room water pump, a boiler room, a boiler water pump, inlet, a fermentation tank top connected marsh gas pipe, upper fermentation tank provided with human hole, the top set with speed reducing motor, low speed reducing electrical machine part connected with stirring shaft, stirring shaft upper layer fixed with stirring blade, also set with coil pipe through welding plate on bracket fixedly, the wall in fermentation tank connected upper part of fermentation tank coil pipe inlet in fermentation tank, fermentation tank downward to spiral plate pipe exit, fermentation tank bottom set with discharging mouth. Using this device, using energy gradually to obtain circulation use, can reduce consume in saving and at the same time increase.
NOVELTY - The patent application claims have one kind closeness fermentation organic fertilizer supplement sum transfusion stirring device, comprising fermentation groove, supplement liquid pool, upper fermentation groove set with stirrer, and an inlet pipe, the inlet pipe respectively connected and fan and supplement liquid pool, stirrer comprises speed reducing motor, speed reducing motor through shaft fixing the hollow rotate shaft, bearing and rotating shaft in set with cavity, cavity and rotating shaft contact part set with oil seal, upper cavity set with inlet, and inlet pipe connected and rotate on shaft is set with through hole, upper rotate shaft with hollow cavity body of stirring blade, with distribution shower nozzle, a rotating shaft in the upper hollow part and stirring blade and shower nozzle. Using in hollow rotate shaft and hollow blade on set theory and gas-liquid channel, give fermentation groove in carrying out supplement sum, supplement water in rotary stirring of the same time, operate and adjust PH, give aerobic fungus provide suitable fermentation environment.
NOVELTY - The utility model claims a dry-wet two-step marsh gas fermentation device, comprising a first-stage dry fermentation mechanism and second grade wet fermentation machine, one grade dry fermentation machine comprises fill with material liquid dry fermentation tank, fill with material and soaking the net material in a liquid, a seal is set with water seal cover and box top part, dry fermentation tank and side wall respectively set with on upper material discharging pipe and the first gas-guide tube, second level wet fermentation machine comprises integrated formed for dry fermentation tank and a bottom of each connected the wet fermentation tank, is equipped with heat exchanger in wet fermentation tank and a circulation hot water phase is connected, a suspension fixed at wet fermentation tank in the biological film, wet fermentation tank side upper wall is respectively set with the second gas-guide tube, discharge tube and the following row material tube. The utility model is new type can be for flora of different respiratory type supply have the suitable and good living environment and facultative Anaerobic and full Anaerobic, but also solves the sludge pump is easy to be blocked and have problem, shortens have degradation time of fiber material, increase have use rate of fermentation raw material, add have volume production rate of device, increase have content of methane in marsh gas.
NOVELTY - The integrated system has fertilizing pipe (16) which is arranged on fertilizing water pump (10) whose one end is connected with mixing liquid tank (9), and another end is connected with irrigation main pipe (7) and irrigation solenoid valve (5). The one end of liquid pipe (17) is connected with downstream of fertilizer sucking device (11). The one end of liquid pipe (38) is connected with mixing liquid tank, liquid storage tank (12), fertilizer device and fermentation tank.    USE - Fertilizer integrated system for organic cultivation.    ADVANTAGE - The one end of the liquid pipe is connected with liquid storage tank, fertilizer device, fermentation tank and mixing liquid tank, such that the intelligent organic cultivation is realized. The management and labor production efficiency are ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fertilizer integrated system.    Irrigation solenoid valve (5)    Irrigation main pipe (7)    Mixing liquid tank (9)    Fertilizing water pump (10)    Fertilizer sucking device (11)    Liquid storage tank (12)    Fertilizing pipe (16)    Liquid pipes (17,38)
NOVELTY - Utilizing nitrogen and phosphorus sewage involves separating sewage by diving pump device into solid phase and fluid liquid. The fluid liquid is fed into sewage anaerobic fermentation process system to obtain biogas. The biogas is utilized for cultivating duckweed and indoor water algae. The duckweed is dried and then crushed to obtain duckweed powder for industrial alcohol production.    USE - Method for utilizing nitrogen and phosphorus sewage used for cultivating duckweed and algae for producing industrial alcohol (claimed).    ADVANTAGE - The method enables to utilize nitrogen and phosphorus sewage into useful resources, and provides economic benefits, and protects environment.
NOVELTY - The generating unit has main portion (10) connected to water exit portion of water tank. A bottom electrode is positioned in lower portion of diaphragm (23) and upper electrode is positioned in upper portion of diaphragm. The upper and bottom electrode are provided with corresponding electrode terminals (21c,22c) to which positive or negative voltage is applied. One side of upper electrode and bottom electrode is arranged with multiple pores (21b,22b) that are formed with tight gap in center area. The pores of upper electrode and bottom electrode are formed with specific diameter.    USE - Hydrogen generating unit for manufacturing device of hydrogen water for preventing aging, diabetes, hypertension, arteriosclerosis, cancer and dementia in human body, used in domestic and business application.    ADVANTAGE - The hydrogen generating unit for hydrogen water manufacturing device is provided with simple structure and small volume. The high-quality hydrogen water is produced effectively by providing upper and bottom electrodes whose one side is arranged with multiple pores that are formed with tight gap in center area.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the hydrogen generating unit for producing hydrogen water.    Main portion (10)    Pores (21b,22b)    Electrode terminals (21c,22c)    Diaphragm (23)    Covers (24,25)
NOVELTY - Preparing organic fertilizer involves mixing 60-70% feces, 20-30% straw or bran, 5-10% shale and 1% fermentation strain, and is prepared by mixing raw materials. The obtained mixture is fermented in fermentation pool at various temperature range. The fermented material is crushed, dried and granulated with water. The granules are fried at 70 degrees C to obtain product that is packaged.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer that prevents nutrient loss, improves physical condition of soil and repairs crop.
NOVELTY - Preparation of Sophora flavescens powder comprises crushing Sophora flavescens, sprinkling with water, adding organic manure, chemical fertilizer, crude fiber degrading bacteria and rice bran, mixing, fermenting at 15-40 degrees C, sealing with plastic film, stacking at greater than or equal to 65 degrees C, maintaining the relative water content to 60-65%, completing the fermentation process when temperature drops to ambient temperature and mixing Sophora flavescens fermentation products, organic fertilizer, perlite and vermiculite at volume ratio of 5:2:1:2.    USE - Method for preparing Sophora flavescens powder used for producing seedling or growing media (claimed).    ADVANTAGE - The product is nutrient-rich and has good water absorption and air permeability.
NOVELTY - Production of chromium-enriched mushroom cultivation material comprises taking 40-50 pts. wt. bean stalk, 30-35 pts. wt. wood flour, 18-23 pts. wt. wheat bran, 0.8-1.2 pts. wt. gypsum, 1-3 pts. wt. sucrose and 2-5 pts. wt. 20% chromium chloride solution, crushing, adding water and mixing until moisture content is 55-63%.    USE - Method for producing chromium-enriched mushroom cultivation material (claimed).    ADVANTAGE - The mushroom has supplementary essential trace elements and 2.1-3.2 ppm organic chromium content more easily absorbed by body.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the cultivation of chromium-enriched mushroom comprising taking low-pressure polyethylene tubular film with 15 cm diameter, 0.04 mm thickness and 55 cm length, sealing one end, adding cultivation material with 4-5 pH, placing into 0.9-1.1 kg plastic bag, pressure cooking at 100 degrees C, heating in low heat for 10-12 hours, cooling to 65-70 degrees C, inoculating at less than or equal to 28 degrees C, stacking at 80-90 cm high, ventilating, turning 2-3 times, covering for 40-50 days, stripping low-pressure polyethylene tubular film, removing plastic bag after 3-5 days, maintaining at 24-28 degrees C and 85-90% relative humidity, ventilating 2-3 times/day for 0.5 hour each, forcing fluffy mycelium lodging for 6-8 days, discharging brown water, illuminating at night using 30-watt fluorescent lamp at 20 m2/room for 3-5 days, harvesting and drying.
NOVELTY - Obtaining Artemisia sphaerocephala extract involves extracting Artemisia sphaerocephala leaves using ethyl alcohol.    USE - Method for obtaining Artemisia sphaerocephala extract used in insecticidal, acaricidal and herbicidal composition for promoting growth of crop and removing gramineae weeds (all claimed).    ADVANTAGE - The method enables to obtain Artemisia sphaerocephala extract that increases crop stress resistance and removes agricultural pests and mites, and ensures obvious killing effect, crop promoting effect, farmland weed inhibition effect and no residues in green and environment-friendly manner.
NOVELTY - Preparing methane catalytic combustion catalyst comprises: (i) dissolving cerium nitrate, ferric nitrate and cobalt nitrate in distilled water by stirring uniformly to obtain solution-A, adding precipitation agent urea or ammonium carbonate into solution-A, closing the reaction system to obtain a closed system, heating to 60-140 degrees C for 3-6 hours, cooling and carrying out suction filtration and drying to obtain catalyst carrier; (ii) preparing palladium nitrate solution; and (iii) grinding the catalyst carrier and immersing in palladium nitrate solution, drying and calcining.    USE - The method is useful for preparing methane catalytic combustion catalyst (claimed).    ADVANTAGE - The catalyst has short preparation period with high catalytic efficiency of methane, low catalytic temperature and good aging-resistant performance.    DETAILED DESCRIPTION - Preparing methane catalytic combustion catalyst comprises: (i) dissolving cerium nitrate, ferric nitrate and cobalt nitrate in distilled water by stirring uniformly to obtain solution-A, adding precipitation agent urea or ammonium carbonate into solution-A, closing the reaction system to obtain a closed system, warming to specific temperature i.e. 60-140 degrees C for 3-6 hours, cooling the reactor to room temperature and carrying out suction filtration and drying to obtain cerium oxide/iron oxide/cobalt oxide catalyst carrier, where the catalyst carrier is an iron cerium cobalt complex oxide; (ii) preparing palladium nitrate solution by adding proper amount of palladium nitrate into distilled water and stirring; and (iii) grinding the catalyst carrier and immersing in palladium nitrate solution for 2-3 hours, then placing in an oven for drying, and carrying out calcining, where the catalyst comprises 90-96% cerium, 3-7% iron, 3-5% cobalt and 0.5-2% palladium.
NOVELTY - Catalyst comprises a carrier and an active component loaded in the carrier. The carrier is 30-99 pts. wt. composite carrier of gamma -alumina and activated carbon or zeolite. The active component comprises 0.1-35 pts. wt. copper, 0.1-10 pts. wt. cobalt, 0.05-10 pts. wt. tin and 0.05-15 pts. wt. niobium.    USE - The catalyst is useful for direct synthesis of ethanol and co-generation of methane from syngas (claimed).    ADVANTAGE - The catalyst has synergistic effect of active components in converting syngas into ethanol and methanol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the catalyst, comprising: (a) preparing mixed aqueous solution containing different solubility metal salt using distilled water at 60-80 degrees C; and (b) immersing the carrier in mixed aqueous solution, then drying and calcining at 400-800 degrees C for 1-12 hours.
NOVELTY - Improving photoelectrocatalytic oxygen generating reaction stability of narrow band gap semiconductor photo-anode comprises modifying a hole storage layer on the narrow band gap semiconductor photo-anode surface, inhibiting degradation performance caused by photoinduced auto-oxidation corrosion reaction on the semiconductor photo-anode surface, and promoting stable photoelectrocatalytic oxygen generating reaction of the photo-anode to achieve hydrogen production from water decomposition by solar energy.    USE - The method is useful for improving photoelectrocatalytic oxygen generating reaction stability of narrow band gap semiconductor photo-anode (claimed).    ADVANTAGE - The method: improves active working life of the narrow band gap semiconductor photo-anode; and produces hydrogen from water decomposition by solar energy.
NOVELTY - Extracting conjugated linoleic acid of Suaeda salsa seeds comprises (i) crushing Suaeda salsa seeds, and inactivating; (ii) carrying out enzymatic hydrolysis; (iii) extracting oil and concentrating; (iv) degumming crude oil; (v) washing, and bleaching; (vi) deodorizing Suaeda salsa seed oil; and (vii) dewaxing.    USE - The method is useful for extracting conjugated linoleic acid of Suaeda salsa seeds (claimed).    ADVANTAGE - The method consumes less energy, produces less amount of solvent residue, and produces conjugated linoleic acid having high quality.
NOVELTY - Power generation gas supply station comprises an iron casting anaerobic unit, a purification tower, a heating pump, a power generation unit having 4 sections.    USE - The station is useful in rural, farm and breeding farm areas.    ADVANTAGE - The station improves the biogas production efficiency; is economical; purifies environment, and thus providing clean energy sources; prevents overflowing of material by using sealed doors and observation hole, and encrustation, and blockage of biogas slurry while circulating; has dual-utilization effect of supplying, and discharging material; utilizes large number of liquid material; and increases biogas production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the power generation gas supply station.
NOVELTY - Preparing conductive thin film involves dissolving high molecular material weight material in acid solution to obtain a viscous product. Cross-linking agent is added to viscous product for crosslinking reaction. Cross-linked product is cleaned, dried, and washed with water to remove crosslinking agent and to obtain final product.    USE - Method for preparing conductive thin film used for biomedical signaling (claimed).    ADVANTAGE - The method enables to prepare conductive thin film, which is eco-friendly and non-toxic to human body, and has improved sticking property.
NOVELTY - Producing microbial fertilizer involves isolating bacteria from surrounding soil and healthy plant root. Biotechnology process is performed on bacteria and healthy plant root to obtain engineering bacterial strain.    USE - Method for producing microbial fertilizer plant growth (claimed), and used for planting crop.    ADVANTAGE - The method enables to produce microbial fertilizer in a simple, cost-effective and eco-friendly manner. Microbial fertilizer reduces fertilizer and pesticide use, and ensures crop growth.
NOVELTY - Preparing medicinal fertilizer involves fermenting 8-22 parts dairy manure, 15-18 parts chicken manure, 20-40 parts straw, 10-20 parts soybean cake and 10-20 parts fermented bagasse for 40-50 days to obtain a fermented product. Fermented product is crushed, and then mixed uniformly with 40-50 parts urea, 30-40 parts calcium superphosphate, 30-40 parts potassium sulfate, 2-5 parts trace element, 3-5 parts composite amino acid, 15-25 parts Chinese herbal medicinal extraction liquid, 1-2 parts Bacillus subtilis and 0.6-1 parts Chaetomium ball.    USE - Method for preparing medicinal fertilizer used for wax apple (claimed), and for preventing and treating plant diseases caused by insect pests.    ADVANTAGE - The method enables to prepare medicinal fertilizer does not harm to wax apple fruit.
NOVELTY - Preparing medicinal fertilizer involves fermenting 20-40 parts livestock excrement, 30-50 parts plant straw and 20-30 parts weathered coal for 50 days to obtain fermented object. Fermented object is crushed into pulverizer, and then sterilized at 110-120 degrees C. Sterilized product is mixed uniformly with 40-60 parts urea, 10-20 parts calcium superphosphate, 10-30 parts potassium sulfate, 10-20 parts potassium humate and 10-20 parts Chinese herbal medicinal extraction liquid.    USE - Method for preparing medicinal fertilizer used for fructus momordicae (claimed).    ADVANTAGE - The method enables to prepare medicinal fertilizer provides nutrition for growth of fructus momordicae, and prevents fructus momordicae to viral disease.    DETAILED DESCRIPTION - Preparing medicinal fertilizer involves fermenting 20-40 parts livestock excrement, 30-50 parts plant straw and 20-30 parts weathered coal for 50 days to obtain fermented object. Fermented object is crushed into pulverizer, and then sterilized at 110-120 degrees C. Sterilized product is mixed uniformly with 40-60 parts urea, 10-20 parts calcium superphosphate, 10-30 parts potassium sulfate, 10-20 parts potassium humate and 10-20 parts Chinese herbal medicinal extraction liquid. The mixture is dried and cooled to 30-40 degrees C, and then 3-5 parts effective microorganism is added, stirred uniformly and packaged.
NOVELTY - Organic fertilizer comprises mushroom residue (65-75 wt.%), cow dung or chicken manure (10-20 wt.%), calcium superphosphate (5-10 wt.%), urea (1-5 wt.%), gypsum powder (1-5 wt.%), composting agent (0.5-3 wt.%), bran (0.5-5 wt.%), and starch (0.5-3 wt.%).    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer provides nitrogen, phosphorus and potassium to crops, and promotes growth of crops, and improves soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) pulverizing fruiting mushrooms and waste mushrooms;    (B) mixing pulverized cow dung, calcium perphosphate, urea, gypsum, bran, composting agent and starch;    (C) fermenting obtained mixture in fermentation reactor; and    (D) turning material during fermentation process to obtain soft, brown and odorless product.
NOVELTY - Organic fertilizer comprises pre-fermentation material (12-18 pts. wt.), mineral substance (6-10 pts. wt.), Bacillus subtilis (0.5-0.8 pts. wt.), edible bacteria (30-40 pts. wt.), kiln dust (5-10 pts. wt.), and water (15-20 pts. wt.). Pre-fermentation material comprises maggot (10-20 pts. wt.), marsh gas (1-3 pts. wt.), molasses (3-5 pts. wt.), sodium selenite (0.0.1-2 pts. wt.), and Bacillus subtilis 10147 (0.1-2 pts. wt.).    USE - Organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves fermenting ingredients for 1-2 weeks to obtain the final product.
NOVELTY - Biologically active organic fertilizer comprises 20-30 pts. wt. biological organic fertilizer, 3-5.8 pts. wt. microorganism powders, 2.5-5 pts. wt. urea, 1.3-2.9 pts. wt. potassium oxide, 1.3-2.9 pts. wt. diammonium phosphate, 1-1.8 pts. wt. amino acid chelated iron, 1.0-2 pts. wt. amino acid chelated calcium, 0.2-1 pts. wt. amino acid chelated zinc, 0.5-1 pts. wt. borax and 10-20 pts. wt. Clay. Microorganism powder is mixture of nitrogen-fixing bacteria, Escherichia coli and Pseudomonas in ratio of 1-2:1:1.    USE - Biologically active organic fertilizer used for rapeseed (claimed).    ADVANTAGE - The biologically active organic fertilizer inhibits growth of Sclerotinia sclerotiorum on rapeseed, improves soil plate structure, and improves quality, and yield of rapeseed more than 50%.    DETAILED DESCRIPTION - Biologically active organic fertilizer comprises 20-30 pts. wt. biological organic fertilizer, 3-5.8 pts. wt. microorganism powder, 2.5-5 pts. wt. urea, 1.3-2.9 pts. wt. potassium oxide, 1.3-2.9 pts. wt. diammonium phosphate, 1-1.8 pts. wt. amino acid chelated iron, 1.0-2 pts. wt. amino acid chelated calcium, 0.2-1 pts. wt. amino acid chelated zinc, 0.5-1 pts. wt. borax and 10-20 pts. wt. clay. Microorganism powder is mixture of nitrogen-fixing bacteria, Escherichia coli and Pseudomonas in ratio of 1-2:1:1. Biological organic fertilizer is obtained by using Lucilia fly larva through biological process. An INDEPENDENT CLAIM is included for a method for preparing biologically active organic fertilizer, which involves crushing and mixing components, and then granulating.
NOVELTY - Bio-organic fertilizer comprises 1-1.8 pts. wt. straw, 0.6-1.4 pts. wt. dairy manure and 0.005-0.1 pts. wt. straw rotten agent.    USE - Bio-organic fertilizer.    ADVANTAGE - The bio-organic fertilizer is cost-effective, ensures short fermentation time, increases high yield and quality of plant, and does not produce malodor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-organic fertilizer, which involves:    (A) drying cattle manure to control water at 85%;    (B) mixing dairy manure and straw stick in ratio of 5-9:3, and then adding fermented rotten agent;    (C) performing fermentation of the heap layer at 60 degrees C for 48 hours and then at 70 degrees C for 7 days to obtain heap layer thickness 20 cm; and    (D) drying the product and then packaging to obtain final product.
NOVELTY - Slow-release fertilizer comprises 10-14 pts. wt. organic resin film, 15-35 pts. wt. nitrogen, 9-21 pts. wt. phosphorus, 10-20 pts. wt. potassium oxide, 3-5 pts. wt. humic acid, 3-5 pts. wt. fermented animal manure and 3-5 pts. wt. chelated trace elements.    USE - Slow-release fertilizer used for flowering potted plant (claimed).    ADVANTAGE - The slow-release fertilizer is cost-effective and eco-friendly, improves soil plate structure, releases nutrient longer than 3-4 months, and adjusts nutrient requirement automatically.
NOVELTY - Compound fertilizer comprises 50-60 pts. wt. cattle and sheep excrement, 8-10 pts. wt. Chinese yam, 7-10 pts. wt. pomegranate rind, 5-6 pts. wt. radix isatidis, 2-3 pts. wt. Acanthopanax, 4-5 pts. wt. pseudoginseng, 2-3 pts. wt. garlic, 1-2 pts. wt. camphor, 1-2 pts. wt. folium artemisiae argyi, 3-4 pts. wt. dried orange peel, 5-7 pts. wt. kelp and 2-4 pts. wt. actinomycete preparation.    USE - Compound fertilizer.    ADVANTAGE - The compound fertilizer improves lily resistance, and ensures no residue, no pollution and great application value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing compound fertilizer, which involves;    (A) mixing, crushing and sieving Chinese yam, pomegranate rind, radix isatidis, root of pseudoginseng, garlic, camphor, folium artemisiae argyi, dried orange peel and kelp;    (B) extracting obtained powder in container with water at 50 degrees C;    (C) filtering extract to obtain filtered liquor;    (D) extracting filtered residue again with water at 50 degrees C;    (E) filtering extract;    (F) combining filtered liquors to obtain traditional Chinese medicine liquid;    (G) fermenting obtained liquid with cattle and sheep excrement for 15 days;    (H) drying and crushing fermented materials; and    (I) mixing crushed material with actinomycete preparation uniformly to obtain product that is packaged.    .
NOVELTY - Fertilizer composition comprises 0.003-0.005 pts. wt. sodium selenite and 40-60 pts. wt. multi-element mineral fertilizer comprising less than or equal to 4% potassium oxide, less than or equal to 20% silicon dixoide, less than or equal to 25% calcium oxide, less than or equal to 2.5% phosphorus, less than or equal to 3.2% iron, less than or equal to 7.4% magnesium and less than or equal to 0.1% zinc. The pH value of fertilizer is 8-11.    USE - Fertilizer composition used for increasing mineral absorption and anthocyanin content in blueberry (claimed).
NOVELTY - Fertilizer composition comprises 51-55 pts. wt. charcoal, 68-79 pts. wt. ammonium nitrate, 1.8-2.11 pts. wt. beneficial inoculant, 5.5-6.5 pts. wt. synergistic agent, 15-20 pts. wt. potassium sulfate, 15-25 pts. wt. natural fertilizer, 10-20 pts. wt. microbial fertilizer and 4-7 pts. wt. earthworm juice concentrate, and is prepared by mixing raw materials to obtain granular fertilizer or powder.    USE - Fertilizer composition.    ADVANTAGE - The fertilizer composition increases soil aggregate structure, extends flowering period, promotes crop roots, stems and leaf normal, and improves crop yield and quality.
NOVELTY - An isolated Pantoea ananatis strain HYL01 (CCTCC M2014530), is new.    USE - The isolated P.ananatis strain HYL01 is useful for promoting root growth of watermelon (claimed) and in preparation of complex microbial fertilizer.    ADVANTAGE - The isolated P.ananatis strain HYL01 promotes watermelon root length, root surface area, root volume, root length and root diameter of 0-0.5 mm and formation of long hairy root in watermelon seedlings, and has strong ability to dissolve phosphorus and calcium phosphate in an amount of 140.26 mg/l and to secrete indole-3-acetic acid (IAA) up to 11.39 mg/l.
NOVELTY - Preparing bio-organic fertilizer involves mixing 950-1050kg weathered coal humic acid powder uniformly with 95-105kg ammonium bicarbonate. 45-55kg Composite fungus fermentation liquid is sprayed in the mixture and carried out fermentation for 6-8 days and then packaged, where fungus number is less than 2 hundred million/g. 950-1050kg Coal gangue powder is mixed with 98-102kg of 40-50% concentrated molasses fermentation liquid and carried out fermentation for 3-5 days to maintain pH value to 6.5-8.0, and then packaged. Coconut husk brick is soaked with water.    USE - Method for preparing bio-organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare bio-organic fertilizer has improved short shelf-life.    DETAILED DESCRIPTION - Preparing bio-organic fertilizer involves mixing 950-1050kg weathered coal humic acid powder uniformly with 95-105kg ammonium bicarbonate. 45-55kg Composite fungus fermentation liquid is sprayed in the mixture and carried out fermentation for 6-8 days and then packaged, where fungus number is less than 2 hundred million/g. 950-1050kg Coal gangue powder is mixed with 98-102kg of 40-50% concentrated molasses fermentation liquid and carried out fermentation for 3-5 days to maintain pH value to 6.5-8.0, and then packaged. Coconut husk brick is soaked with water to neutralize at pH value to 6.0-7.0, and then mixed all obtained product. The mixture is subjected to composting to detect 3-30% organic matter and maintained pH value to 6.5-8.0, and then packaged.
NOVELTY - Bio-organic fertilizer composition comprises 35-40% chicken manure, 25-30% soybean meal, 10-15% clam shell, 8-10% fish scales and fish bones, 5-8% humic acid, 1.5-2% phoxim, and 0.5-1% biological bacteria.    USE - The fertilizer is useful for preventing pests (claimed), preferably lepidopteran on peanuts, wheat, rice, cotton, corn and other crops.    ADVANTAGE - The fertilizer has high organic matter and nutrients, adjusts the characteristics of the soil, so as to make soil more fertile.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the bio-organic fertilizer composition, comprising crushing chicken manure, soybean meal, clam shell, fish scales and fish bones, piling and adding into pit, adding humic acid and biological bacteria, fermenting for 2.5-3 months, maintaining temperature at 20-32 degrees C, and finally air-drying, then adding octyl sulfate, stirring and pelletizing.
NOVELTY - Preparing biological fertilizer involves mixing phosphogypsum, phosphorus slag, and coal in a ratio of 1:(0.5-3):(0.5-5) to obtain a mixture. Baggase containing moisture content 20-70%, rooting agent and lees are mixed in a ratio of 0.5:(0.05-0.5):(5-10) to obtain another mixture. Obtained mixtures are mixed to obtain third mixture. Obtained mixture is dried to obtain moisture content to 30-50%. Obtained product is fermented at 20-30 degrees C for 2-10 days to obtain biological fertilizer.    USE - Method for preparing biological fertilizer used for improving soil salinity (claimed).    ADVANTAGE - The method is cost-effective, and enables to prepare biological fertilizer, which ensures improved fertility and reduced toxicity of soil.
NOVELTY - Fertilizer comprises leaves and fruit fermentation residue (15-20 parts), urea solution (5-10 parts), amino acids (10-15 parts), calcium nitrate (2-3 parts), and borax solution (1-2 parts).    USE - Fertilizer used for fruit tree (claimed).    ADVANTAGE - The fertilizer is rich in nutrition, and ensures improved yield of fruit tree.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer used for fruit tree leaves, which involves mixing raw material with stirring for 1-2 hours, and heating the obtained mixture at 60-80 degrees C for to obtain fertilizer, and then dissolving obtained fertilizer (500 g) in water (20 Kg) before spraying.
NOVELTY - Method of preparing microbial additive for planting peanut involves (a) culturing Bacillus mucilaginosus and fermenting the obtained culture to obtain B.mucilaginosus liquid culture, (b) culturing Dermatophilus bacteria and fermenting the obtained culture in fermentation broth to obtain Dermatophilus liquid culture and (c) mixing B.mucilaginosus culture, Dermatophilus culture, actinomycetes, nitrogen-fixing bacteria, trace elements and humus uniformly.    USE - The method is useful for preparing microbial additive for planting peanut (claimed). The additive is useful as microbial fertilizer.    ADVANTAGE - The prepared microbial additive improves peanut yield.    DETAILED DESCRIPTION - Method of preparing microbial additive for planting peanut involves (a) culturing Bacillus mucilaginosus in a shaking culture flask and inoculating the obtained B.mucilaginosus culture in fermentation broth to obtain B.mucilaginosus liquid culture, (b) culturing Dermatophilus bacteria in a shaking culture flask and inoculating the obtained Dermatophilus bacteria in fermentation broth to obtain Dermatophilus liquid culture and (c) mixing 40-50 %mass B.mucilaginosus liquid culture, 30-40 %mass Dermatophilus bacteria liquid culture, 1-10 %mass actinomycetes, 1-10 %mass nitrogen-fixing bacteria, 1-5 %mass trace elements and humus (remainder) uniformly.
NOVELTY - microbial fertilizer comprises 5-15 wt.% hydrolyzed active polypeptide, 3-8 wt.% complex microbial inoculum, 40-60 wt.% organic fertilizer and 20-37 wt.% inorganic fertilizer.    USE - Microbial fertilizer (claimed).    ADVANTAGE - The microbial fertilizer is cost-effective, promotes healthy living of organisms and increases crop yield.
NOVELTY - Water splitting device comprises hydrogen storage tank (6) and oxygen storage tank (5), where oxygen storage tank comprises electric chemical reaction stack (2) and low pressure control centrifugal separator (4). The electric chemical reaction stack is provided with reactor that is connected with output pipe (3). The low pressure control centrifugal separator is connected through oxygen collector and hydrogen storage tank.    USE - Water splitting device.    ADVANTAGE - The water splitting device is eco-friendly and simple in structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a water splitting device.    Electric chemical reaction stack (2)    Output pipe (3)    Low pressure control centrifugal separator (4)    Oxygen storage tank (5)    Hydrogen storage tank (6)
NOVELTY - Microbial inoculant composition comprises long-chain fatty-acid-oxidizing bacterium, and methanogenic bacterium, where the long-chain fatty-acid-oxidizing bacterium comprises Syntrophomonas wolfei subsp.wolfei, S.sapovorans, S.bryantii, S.erecta, S.zehnderi, and S.palmitatica, and methanogenic bacterium comprises Methanospirillum hungatei, Methanobacterium formicicum, Methanosarcina barkeri, M.acetivorans, and Methanothrix soehngenii.    USE - The composition is useful in biogas fermentation system (all claimed).    ADVANTAGE - The composition improves gas production rate of a grease-rich raw material, shortens fermentation dwell time, avoids accumulation of fermentation liquid upper-layer grease, and is rich in grease raw material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the microbial inoculant composition which involves (a) mixing long-chain fatty-acid-oxidizing bacterium, and methanogenic bacterium in a volume ratio of 1-9:9-1, and (b) packaging and storing the mixture when cell concentration reaches 1x 109 cells per ml.
NOVELTY - Artificial soil comprises minerals, fermented organic material, bottom ash, natural soil, calcium-magnesium fertilizer and water-absorbent polymer. The fermented organic material is vegetable organic material or animal organic material fermented by microorganisms chosen from Bacillus pumilus, Bacillus subtilis, Bacillus licheniformis, Bacillus megaterium, Rhodobacter capsulatus and Rhodobacter sphaeroide. The mineral is chosen from zeolite, illite, perlite, vermiculite and bentonite.    USE - Artificial soil is used for forming lower bed of artificial garden and mini-park.    ADVANTAGE - The artificial soil has excellent water-retaining capacity, and increases the initial germination of plants and normal growth of plants.    DETAILED DESCRIPTION - Artificial soil comprises 100 pts. wt. minerals, 50-200 pts. wt. fermented organic material, 50-150 pts. wt. bottom ash, 100-300 pts. wt. natural soil, 10-100 pts. wt. calcium-magnesium fertilizer and 1-20 pts. wt. water-absorbent polymer. The fermented organic material is vegetable organic material or animal organic material fermented by microorganisms chosen from Bacillus pumilus, Bacillus subtilis, Bacillus licheniformis, Bacillus megaterium, Rhodobacter capsulatus and Rhodobacter sphaeroide. The mineral is chosen from zeolite, illite, perlite, vermiculite and bentonite. The calcium-magnesium fertilizer contains calcium oxide, slaked lime, carbonated lime, lime silicate, superphosphate lime, plaster, gypsum, magnesium hydroxide, magnesium sulfate and magnesium carbonate. The water-absorbent polymer is copolymer of carboxylic acid having ethylenically unsaturated bond and alkali metal salt of carboxylic acid with ethylenically unsaturated bond or copolymer of amide having an ethylenically unsaturated bond and alkali metal salt of carboxylic acid with ethylenically unsaturated bond. An INDEPENDENT CLAIM is included for manufacture of artificial soil.
NOVELTY - Coated slow release fertilizer comprises 70-99 wt.% fertilizer core coated with 0.8-25 wt.% slow release coating layer comprising 10-96 wt.% sodium alginate oligosaccharide, 0.2-5 wt.% conditioning agent, 3-86 wt.% additive and 1-4 wt.% additive, initiator, cross-linking agent and sealants.    USE - Coated slow release fertilizer used for planting economic crop, grain crops, vegetable, fruit trees, economic forest, flower, medicine material and lawn grass (claimed).    ADVANTAGE - The coated slow release fertilizer increases crop yield and fertilizer utilization rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing coated slow release fertilizer, which involves coating fertilizer core with coating solution containing conditioning agent and solvent, and then drying coated core at 74-78 degrees C, where coating solution is prepared by utilizing sodium alginate oligosaccharide, additve, adjuvant, solvent, initiator, cross-linking agent and sealing agent.
NOVELTY - Method for processing food waste, involves (a) pre-treating food waste, (b) crushing food waste and wheat bran into particle diameter of 0.3-40 mm, (c) mixing crushed food waste and crushed wheat bran in a mass ratio of 1:0.8-1.2, and fermenting mixture, and (d) mixing crushed products and fermented mixture in a mass ratio of 7:4-7:3.    USE - The method is useful for processing food waste (claimed).    ADVANTAGE - The method processes food waste cost-effectively.
NOVELTY - Treating food waste involves reacting it with reactant to facilitate degradation. Auxiliary agent and water-absorbing agent are added to food waste in a ratio of 6:9:50. Reactant comprises sodium dodecylbenzenesulfonate (25-28 wt.%), sodium hydroxide (40-45 wt.%), citric acid (4-5 wt.%), acetic acid (2-3 wt.%), and sodium hypochlorite (24-25 wt.%). Auxiliary agent comprises waste aluminum slag powder (70-71 wt.%) and sodium gluconate (29-30 wt.%). Water-absorbing agent comprises waste residue and cement clinker.    USE - Method for treating food waste used for preparing organic fertilizer (claimed).    ADVANTAGE - The method is economic and eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for treating food waste, which involves:    (A) stirring food waste;    (B) adding citric acid, glyoxal and sodium hydroxide;    (C) heating obtained mixture;    (D) reacting obtained mixture with sodium dodecylbenzenesulfonate and sodium hypochlorite at 30-50 degrees C for 5-10 minutes;    (E) adding auxiliary agent and water-absorbing agent to obtained mixture under stirring condition;    (F) drying obtained product; and    (G) pulverizing dried product.
NOVELTY - Kitchen waste energy treatment method comprises subjecting kitchen waste to mechanical dewatering and/or secondary mechanical dewatering to obtain wastewater and solid waste, adding solid waste with lime-containing adsorbent, dewatering to obtain waste residue, further dewatering with adsorbent to obtain modified fuel, and mixing with coal or other combustion fuel mixture.    USE - Method for kitchen waste energy treatment (claimed).    ADVANTAGE - The method achieves optimal use of resources, converts waste into environment-friendly products, improves operating performance of modified fuel in boiler, and it has rational design.    DETAILED DESCRIPTION - Kitchen waste energy treatment method comprises subjecting kitchen waste to mechanical dewatering and/or secondary mechanical dewatering to obtain wastewater and solid waste, adding solid waste with lime-containing adsorbent, dewatering to obtain waste residue, further dewatering with adsorbent to obtain modified fuel, and mixing with coal or other combustion fuel mixture. The modified fuel and coal or other fuel combustion mixture has weight ratio of 10-300%. The lime and coal or other fuel combustion mixture has weight ratio of 0.2-40%. The coal or other fuel combustion mixture has calcium/sulfur ratio of 1.5-3.
NOVELTY - Solar energy and seawater synergized driving photoelectric device comprises degradation chamber (1), hydrogen collector device (2), transparent window (3), catalytic electrodes (4), buoyancy plate (5) and seawater battery (6).    USE - Solar energy and seawater synergized driving photoelectric device used for degrading organic pollutants and producing hydrogen (all claimed).    ADVANTAGE - The device is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the organic pollutant degradation method comprising taking organic pollutants, adjusting wastewater pH to 7-8, soaking catalytic electrodes, degrading using inert gas or air, standing, exposing to photocatalytic light, degrading, discharging and collecting produced hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of solar energy and seawater synergized driving photoelectric device.    Degradation chamber (1)    Hydrogen collector device (2)    Transparent window (3)    Catalytic electrodes (4)    Buoyancy plate (5)    Seawater battery (6)
NOVELTY - The portable anesthetic laryngoscope has a rotating shaft (65) that is provided at the lower side of a tooth groove set (64), and joined to a main body box (66). A button (67) is provided at the lower side of the main body box, and set with a carrying handle (68). A size adjusting valve (70) is provided on the socket (69) of a tooth unit (2), and having one side with a spatula (71). A locating folding pole (73) is provided at one side of the tooth unit, and having a lower side provided with a silicon rubber pad (74) and a fixed valve (75).    USE - Portable anesthetic laryngoscope used in patient.    ADVANTAGE - The laryngoscope is featured with improved efficiency, safe operation, simple, practical and environment friendly, while providing complete function.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the portable anesthetic laryngoscope.    Tooth unit (2)    Tooth groove set (64)    Rotating shaft (65)    Main body box (66)    Button (67)    Carrying handle (68)    Socket (69)    Size adjusting valve (70)    Spatula (71)    Locating folding pole (73)    Silicon rubber pad (74)    Fixed valve (75)
NOVELTY - Ammonia-containing wastewater is injected into lower region of separation membrane aeration bioreactor, and nitration reaction is carried out. Wastewater is then injected into upper region of bioreactor and denitrification is carried out. Wastewater is then flows out through water outlet of upper portion. A hollow cylindrical inner tube structure is set in nitration zone. An aeration system is set inside the inner tube structure. An inner cylinder of hollow bell structure, is set in denitrification zone.    USE - Simultaneous nitrification and denitrification of ammonia-containing wastewater (claimed).    ADVANTAGE - Simultaneous nitrification and denitrification of ammonia-containing wastewater, is carried out with high efficiency.    DETAILED DESCRIPTION - Ammonia-containing wastewater is injected into lower region of separation membrane aeration bioreactor, and nitration reaction is carried out. Wastewater is then injected into upper region of bioreactor and denitrification is carried out. Wastewater is then flows out through water outlet of upper portion. A hollow cylindrical inner tube structure is set in nitration zone. An aeration system is set inside the inner tube structure. An inner cylinder of hollow bell structure, is set in denitrification zone. Diameter of inner cylinder of hollow bell structure, is greater than the diameter of inner tube structure.
NOVELTY - Broad spectrum bio-diesel oil pour point depressant comprises ethylacetoacetate biodiesel depressant composition and poly(methyl methacrylate) at ratio of 1-3:1. The ethylacetoacetate biodiesel depressant composition is made of organic solvent and ethylacetoacetate biodiesel depressant at mass ratio of 1:1.5-2.5. The organic solvent is butyl acetate, amyl acetate or hexyl acetate. The ethylacetoacetate biodiesel depressant composition is prepared by adding organic solvent and ethylacetoacetate biodiesel depressant into the reaction vessel, stirring and cooling.    USE - Broad spectrum bio-diesel oil pour point depressant used in ordinary diesel oil (claimed).    ADVANTAGE - The product has good depression effect; improves the low temperature fluidity of biodiesel and reduces the cold filter point by 6-9 degrees C and condensation point by 8-12 degrees C.    DETAILED DESCRIPTION - Broad spectrum bio-diesel oil pour point depressant comprises ethylacetoacetate biodiesel depressant composition and poly(methyl methacrylate) at ratio of 1-3:1. The ethylacetoacetate biodiesel depressant composition is made of organic solvent and ethylacetoacetate biodiesel depressant at mass ratio of 1:1.5-2.5. The organic solvent is butyl acetate, amyl acetate or hexyl acetate. The ethylacetoacetate biodiesel depressant composition is prepared by adding organic solvent and ethylacetoacetate biodiesel depressant into the reaction vessel, stirring at 30-50 degrees C for 0.5-1.5 hours with speed of 300-500 revolutions/minute and cooling to room temperature.
NOVELTY - Preprocessing lignocellulosic feedstock involves using aqueous solution of ethylenediamine.    USE - Method for preprocessing lignocellulosic feedstock used for producing cellulosic ethanol (claimed).
NOVELTY - Cultivating abalone mushroom involves (a) crushing bagasse, and processing abalone mushroom waste, drying and crushing, (b) adding water to dried abalone mushroom, soaking abalone mushroom in water, uniformly mixing abalone mushroom with bagasse and soybean, after processing, fermenting, adding lime and gypsum, terminating fermentation, cooling, directly spreading on furrow bed, seeding hairy bacteria and covering with sandy loam soil, and (c) spraying leaching solution on mushroom bed.    USE - The method is useful for cultivating abalone mushroom (claimed).    ADVANTAGE - The method saves manpower, coal and other resources, and reduces environmental pollution.    DETAILED DESCRIPTION - Cultivating abalone mushroom involves (a) crushing bagasse into particles with size of 3-5 mm, and processing abalone mushroom waste, drying abalone mushroom waste and crushing dried abalone mushroom into particles with size of 2-3 mm, (b) adding 20-30 times clean water to 3-4 %mass dried abalone mushroom, soaking abalone mushroom in water for 18-24 hours at room temperature, uniformly mixing abalone mushroom with 68-72 %mass bagasse and 20-24 %mass soybean, after processing, fermenting at 60 degrees C for 24 hours, adding 3-4 %mass lime and 1 %mass gypsum, terminating fermentation, cooling fermented materials, directly spreading on furrow bed, seeding hairy bacteria and covering 2-3 cm with sandy loam soil, and (c) spraying 0.01-0.02 g/ml leaching solution on 3-5 kg per square meter mushroom bed. The leaching solution is prepared by adding 20 times clean water to abalone mushroom particles, soaking abalone mushroom particles in water at room temperature for 18-24 hours, filtering and removing residues to obtain 0.05 g/ml abalone mushroom extract and diluting extract with clean water.
NOVELTY - Cultivating shiitake mushroom involves (a) processing shiitake mushroom, drying processed mushroom and crushing dried mushroom, (b) adding clean water to crushed mushroom, soaking mushroom in water, uniformly mixing mushroom with cottonseed hulls and soybean, after processing, fermenting, adding lime and gypsum, terminating fermentation, cooling, directly spreading on furrow bed, seeding hairy bacteria and covering 1 cm with sandy loam soil, and (c) spraying leaching solution on mushroom bed.    USE - The method is useful for cultivating shiitake mushroom (claimed).    ADVANTAGE - The method saves labor, coal and other resources, and reduces environmental pollution.    DETAILED DESCRIPTION - Cultivating shiitake mushroom involves (a) processing 3-4 %mass shiitake mushroom, drying processed mushroom and crushing dried mushroom into particles, (b) adding 20-30 times clean water to crushed mushroom, soaking mushroom in water for 18-24 hours at room temperature, uniformly mixing mushroom with 68-72 %mass cottonseed hulls and 20-24 %mass soybean, after processing, fermenting at 60 degrees C for 24 hours, adding 3-4 %mass lime and 1 %mass gypsum, terminating fermentation, cooling fermented materials, directly spreading on furrow bed, seeding hairy bacteria and covering 1 cm with sandy loam soil, and (c) spraying 0.01-0.02 g/ml leaching solution on 3-5 kg per square meter mushroom bed. The leaching solution is prepared by adding 20 times clean water to shiitake mushroom particles, soaking mushroom particles in water at room temperature for 18-24 hours, filtering and removing residues to obtain 0.05 g/ml mushroom extract, and diluting extract using clean water.
NOVELTY - An ecological irrigation and drainage water circulation water energy-saving pollution-reducing method involves using pour area drainage period, using pour area water period, using irrigation drainage period for introduction of field drainage through drainage ditch into circulation wetland reservoir (1), purifying submerged plant in ecological wetland by pesticide, trapping heavy metal harmful substance, purifying, processing nitrogen and phosphorus nutrient substance to reduce hazard of water body efflux, and increasing water usage efficiency, nitrogen, and phosphorus nutrient substance.    USE - Ecological irrigation and drainage water circulation water energy-saving pollution-reducing method.    ADVANTAGE - Method increases fertilizer efficiency.    DETAILED DESCRIPTION - An ecological irrigation and drainage water circulation water energy-saving pollution-reducing method involves using pour area drainage period, using pour area water period, using irrigation drainage period for introduction of field drainage through drainage ditch into circulation wetland reservoir (1), purifying submerged plant in ecological wetland by pesticide, trapping heavy metal harmful substance, purifying, processing nitrogen and phosphorus nutrient substance to reduce hazard of water body efflux, using pour area to water period from water pump station for circulation of wetland water in water body and water channel allocation to irrigation, and increasing water usage efficiency, residual nitrogen, and phosphorus nutrient substance needed for crop growth.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of ecological irrigation and drainage water circulation water energy-saving pollution-reducing methodical arrangement.    Circulation wetland reservoir (1)    Lifting pump station (2)    Water dry channel (3)    Irrigation branch canal (5)    Watering hopper (6)
NOVELTY - This utility model relates to a device for unite pre-processing active sludge producing short chain fat acid, comprising a gamma-ray irradiation device, ultrasonic wave crushing device, comprising an ultrasonic wave generating processor, ultrasonic wave detector and a ultrasonic wave, the ultrasonic wave generating processor of a tank-type container and ultrasonic wave generator composed of the tank-type container is equipped with an ultrasonic wave generator in discharging a feedstock and a gamma-ray irradiation device and tank-type container and a connected, closeness fermentation device, a closeness is a closeness fermentation tank, discharging mouth and tank container feedstock wherein a ultrasonic wave and a device generating a closeness of each connected. The device of this utility model for activated sludge by a gamma-ray irradiation and ultrasonic wave pre-processing, a process can obviously increase of sludge and protein, polysaccharide equal organic matter dissolve is water and the degree of increase production rate of acid sludge, and shortens the sludge Anaerobic fermentation of time.
NOVELTY - The utility model claims a box-type organic waste anaerobic treatment system, composed of a container shell and a storing air pocket and gas-liquid circulation system is assembled into. The top of the box body plate and a heat exchange device, a full solar use. Anaerobic digestion device can supply heat, gas-liquid circulation system through circulation liquid surface floating slag breaking shell, a bottom circulation and swelling activated sludge layer, increase Anaerobic digestion efficiency. A body using industrial production and a storing air pocket, quality is controllable, a period short, box body shell of equal device composed of container, a container shell directly using the standardization of the whole device, series, monomer volume and overall scale of every processing system can be a connected in series and a feeding port, a discharging unit and a marsh gas collecting pipe, i a is enlarged.
NOVELTY - Organic fertilizer comprises 60-80 pts. wt. humic acid material and 20-40 pts. wt. reinforced material.    USE - The organic fertilizer is useful for cultivating plant in soil (claimed).    ADVANTAGE - The organic fertilizer increases seedling survival rate, provides sufficient nutrients required by the plant, and increases water and fertilizer utilization efficiency, and plant yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic fertilizer, which involves preparing humic acid material by activating natural humic acid, using humic acid material as substrate, mixing with the reinforced material, pelletizing and performing surface treatment to obtain product.
NOVELTY - Method for producing black fungus, involves (a) taking e.g. corncob, cotton seed hull, wheat bran, mushrooms, and gypsum, crushing the above-mentioned materials and drying the crushed materials, (b) adding water to the mushroom, soaking the mushroom, extracting the mixture, adding remaining materials to the extract, piling the mixture, maintaining dry weight of the piled mixture and inserting stick in the heap, (c) turning the heap, and (d) bagging the heap in a polyethylene bags, inoculating the above-mentioned black fungus seed culture, and recovering mycelium.    USE - The method is useful for producing black fungus (claimed).    ADVANTAGE - The method is cost-effective, less labor intensive and environmentally-friendly.    DETAILED DESCRIPTION - Method for producing black fungus, involves (a) taking 48-52 wt.% rhizoma cyperi extract, 11-15 wt.% corncob, 10 wt.% cotton seed hull, 20 wt.% wheat bran, 4-5 wt.% mushrooms, 1.5 wt.% lime and 1 wt.% gypsum, crushing the above-mentioned materials and drying the crushed materials, (b) adding 20-30 times water to the mushroom, soaking the mushroom at room temperature for 18-24 hours, extracting the mixture, adding the remaining materials to the extract, piling the mixture to a height of 1-1.2 m and width of 2-3 m, maintaining dry weight of the piled mixture to 300-500 kg and inserting stick in the heap, (c) turning the heap at 60 degrees C for 24 hours, where the turning is performed for once in day and night, adding lime and gypsum, performing turning for 3-4 times for 5-6 days and maintaining moisture content of the planting material to 63-65%, and (d) bagging the heap in a polyethylene bags to a height of 15 cm and width of 0.04 mm, inoculating the above-mentioned black fungus seed culture on both sides of the bag, incubating the culture at dark room, 20-22 degrees C and 60-75% humidity for 42-45 days, and recovering mycelium.
NOVELTY - The vehicle has conveying system (1) with cab and carriage. Cab and carriage are provided with oil bucket (7). Carriage is provided with organic fertilizer reaction system (3), intelligent electric control system (5), and cooling system (6). Top portion of carriage is provided with global positioning system (GPS) location monitor system (4). Outer portion of carriage is provided with feeding system (2). Feeding system is connected with intelligent weigh system. Feeding system is connected to reaction system. Reaction system is connected to electric control system and cooling system.    USE - Urban food waste slag smart metering based in situ type organic fertilizer manufacturing compressed natural gas (CNG) vehicle.    ADVANTAGE - Tons of food wastes are local processed efficiently. The vehicle provides in situ real-time processing of food waste. The required labor is reduced. The digital management of food waste processing is performed. The treated food waste is used as the raw material for organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the CNG vehicle.    Conveying system (1)    Feeding system (2)    Organic fertilizer reaction system (3)    GPS location monitor system (4)    Intelligent electric control system (5)    Cooling system (6)    Oil bucket (7)
NOVELTY - Method for producing fertilizer, involves breeding musk deer by existing methods, separating manure from the musk deer farmyard using ditch or underground tube connected to the farmyard, collecting the manure, taking corn straw, sunflower straw, wheat straw or their broken portions, immersing in water, mixing immersed straw with collected product and stacking to obtain product.    USE - The method is useful for producing fertilizer (claimed).    ADVANTAGE - The method produces fertilizer rapidly in 5-10 days.
NOVELTY - The device has a straw pulverizer that is installed in a ventilation mouth. The crop straw, corn straw, sunflower straw, wheat straw, and rice straw are processed without conveying directly from the fields of crops to the pulverizer for crushing, and directly entered into a farmyard manure processing pool. The straw is processed into fertilizer from the vents out of processing pool, without conveying directly to the top of the fields. The top of the fields and the farm manure processing pool are filled with one meter of crops.    USE - Device for processing underground straw farmyard manure.    ADVANTAGE - The municipal environment is improved. The costs are saved. The backfill meters are provided at the top of the manure processing pool, so that crop fields with high, convenient farmland farming species are obtained.
NOVELTY - Bioactive substance extraction instrument has two portions containing fixtures and supporting consumable portion, where the fixtures comprise negative pressure system, bolt control unit and waste recovery unit and the supporting consumable components mainly by the mixed reaction room, media columns and cylindrical overall microtubule composition. All of the liquid within the respective member is driven using a negative pressure unit by rotation of the bolt holes to control the switching of the liquid passage.    USE - The instrument is useful for extracting artificial culture, blood, tissue, bone, excreta, fingerprints, soil, water, and gelatin, and substance related to life activities such as RNA, DNA, carbohydrate, lipid, and protein (all claimed).    ADVANTAGE - The instrument is simple, cost-effective, and non-polluting, and produces high-end product quality.
NOVELTY - A Cladosporium sphaerospermum strain ZF-35 (CCTCC M 2014399), is new.    USE - The C.sphaerospermum strain ZF-35 is useful for producing hydroxylated epoxy progesterone (claimed), and sex hormones and other steroid hormone drugs.    ADVANTAGE - The C.sphaerospermum strain ZF-35 produces hydroxylated epoxy progesterone simply, rapidly and environmentally-friendly with strong specificity, and is suitable for large-scale industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of C.sphaerospermum strain ZF-35 for producing hydroxylated epoxy progesterone, by taking the C.sphaerospermum from seed culture medium, using 0.1-0.3 g/ml 16( alpha ),17( alpha )-epoxy progesterone as substrate, taking anhydrous alcohol as reaction medium, culturing in a fermentation culture medium at 25-30 degrees C, centrifuging at 160-200 revolutions/minute (rpm), separating, purifying, and obtaining product.
NOVELTY - Hybrid sterility gene of rice is made of S1-J and S1-g gene, where both upstream primer and downstream primer are designed for hybrid sterility gene of rice.    USE - Hybrid sterility gene of rice.    ADVANTAGE - The hybrid sterility gene S1-J and S1-g of rice effectively resolves inter-species infertility problems, and thus promotes increase in rice production on agricultural scale in an economic-friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a primer for hybrid sterility gene of rice, which comprises upstream primer and downstream primer, where the upstream primer i.e. 48281F or 51301F is made of 28 nucleobases sequence i.e. gtcgcttcactgcttatgaccccacatt (SEQ ID NO : 3), given in the specification and the downstream primer i.e. 51682R is made of 21 nucleobases sequence i.e. ctgtattgaagctggccagta (SEQ ID NO : 3), given in the specification; and    (2) a recombinant expression vector, which comprises a vector genome that is inserted by the hybrid sterility gene at its multiple cloning site; and performing the genotyping of hybrid sterility gene S1-J and S1-g into the cloned recombinant expression vector.
NOVELTY - Culture method for improving biodiesel production from microalgae by two stage pH adjustment, involves (a) culturing the microalgae in a culture medium with predetermined pH value, to obtain maximum biomass accumulation, and (b) culturing the microalgae in a culture medium with predetermined pH value, to obtain maximum lipid accumulation and obtaining product with high total lipid content, where lipid accumulation is more when the biomass is produced in maximum quantity.    USE - The culture method is useful for improving biodiesel production from microalgae (claimed).    ADVANTAGE - The method enables to provide increased biodiesel yield.
NOVELTY - A recessive malachite green antigen is prepared by taking 4-bromobenzaldehyde or 4-iodobenzaldehyde and acrolein diethyl acetal or ketone derivative, performing Heck reaction in presence of ligand, palladium acetate, and acid-binding agent to obtain 1st compound, performing condensation of 1st compound and N,N-dimethylaniline to obtain 2nd compound, dissolving 2nd compound in 1,4-dioxane, and controlling pH to 9-10 by using saturated sodium hydroxide solution.    USE - Preparation of recessive malachite green antigen.    ADVANTAGE - Preparation process has reduced environmental pollutants and has mild reaction condition.    DETAILED DESCRIPTION - A recessive malachite green antigen of formula (II) is prepared by taking 4-bromobenzaldehyde or 4-iodobenzaldehyde and acrolein diethyl acetal or ketone derivative of formula (I), performing Heck reaction in presence of ligand, palladium acetate, and acid-binding agent to obtain 1st compound, performing condensation of 1st compound and N,N-dimethylaniline to obtain 2nd compound, dissolving 2nd compound in 1,4-dioxane, and controlling pH to 9-10 by using saturated sodium hydroxide solution.    n=1-3;    m=0 or 1; and    n'=2-4.    DESCRIPTION OF DRAWING(S) - The drawing shows a reaction diagram of recessive malachite green antigen.
NOVELTY - Method for producing fertilizer, involves breeding musk deer by existing methods, separating manure from the musk deer farmyard using ditch or underground tube connected to the farmyard, collecting the manure, taking corn straw, sunflower straw, wheat straw or their broken portions, immersing in water, mixing immersed straw with collected product and stacking to obtain product.    USE - The method or device is useful for producing fertilizer (all claimed).    ADVANTAGE - The method produces fertilizer rapidly in 5-10 days.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for producing fertilizer.
NOVELTY - Method for breeding pig and producing pig manure, involves setting adjacent joint facilities for pig breeding and pig farm manure production, including flattening pig sties and pig farm manure production pools, the flattening pigsties and the pig farm manure collection pools are connected using open ditches or underground pipes, the pig farm manure production pools are lower than the flattening pig sties and collect pig manure for pig farm manure production, performing existing pig breeding in the flattening pig sties, and collecting pig manure.    USE - The method is used for breeding pig and producing pig manure (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device, which comprises fattening pigsty, nursery bed, birthing bed and litter bed.
NOVELTY - Horse breeding and horse manure production method involves setting horse breeding and horse manure production facility adjacent to the joint. The horse manure pools lying below the plot are made for fattening of horses, and horse manure is horse manure product obtained after regular horse breeding within the stables. The horse manure is produced by soaking corn stalks or sunflower stalks in water, and adding the mixture to dung heap in suitable proportion.    USE - The method is useful for breeding horse and producing horse manure jointly (claimed).    ADVANTAGE - The method is capable of breeding horse and producing horse manure with improved efficiency.    DETAILED DESCRIPTION - Horse breeding and horse manure production method involves setting horse breeding and horse manure production facility adjacent to the joint, where the adjacent joint facilities include stables, and horse manure plot made pool, stables and horse manure product made ditches or underground pools are connected by underground pipe. The horse manure pools lying below the plot are made for fattening of stables, and horse manure is horse manure product obtained after regular horse breeding within the stables. The horse manure is produced by soaking corn stalks or sunflower stalks, straw or stubble or its broken segment in water, and adding the mixture to dung heap in suitable proportion.
NOVELTY - Preparing vermiculture base material, involves (a) heating water, adding brown sugar and urea, adding effective microorganism (EM), and performing fermentation, and (b) mixing e.g. obtained fermented material, fresh animal manure and fermented feed, composting mixture under anaerobic conditions at moisture content of 40-50% for 7-12 days, stirring the mixture once in every 3 days, adding carrot juice, and performing composting step until mosture content becomes 30-35%.    USE - The method is useful for preparing vermiculture base material (claimed).    ADVANTAGE - The method prepares base material that ensures rapid growth of earthworm.    DETAILED DESCRIPTION - Method for preparing vermiculture base material, involves (a) heating 100 parts water to 100 degrees C, adding 2-3 parts brown sugar and 0.2-0.3 part urea, reducing temperature to 40-45 degrees C and then to 30-35 degrees C, adding 1.5-2 parts effective microorganism (EM), and performing fermentation for 48 hours, and (b) mixing 100 parts obtained fermented material, 20-30 parts fresh animal manure, 3-5 parts discarded green fodder, 3-5 parts fermented feed, 25-35 parts garden soil and 20-70 parts fermentation broth containing 5-10% water, composting mixture under anaerobic conditions at moisture content of 40-50% for 7-12 days, stirring the mixture once in every 3 days, adding carrot juice, and performing composting step until mosture content becomes 30-35%.
NOVELTY - Synthesizing steroidal 4,9-diene derivative (I) involves performing addition and elimination reaction on steroidal-based compound.    USE - Method for synthesizing steroidal 4,9-diene derivative (claimed).    ADVANTAGE - The highly purified steroidal 4,9-diene derivative synthesized has wide adaptability and is obtained in large amount by this method. The steroidal 4,9-diene derivative preparation method, is thus fit for industrial production and is synthesized in an environment-friendly, simple and cost-effective manner.    DETAILED DESCRIPTION - Synthesizing steroidal 4,9-diene derivative of formula (I) involves performing addition and elimination reaction on steroidal-based compound (II).    R1=CH3, CH3CH2 group;    R2=H, OH, CN or carbonyl group; and    R3=H and R4 =H or CH3 group.
NOVELTY - A potassium-containing rock is crushed to 80-200 mesh. 10-30% Auxiliary agent and sulfuric acid are mixed in a microwave reactor. A liquid neutralizer is added to obtained reaction liquid, to obtain separated solid (s1) and liquid (d2). The liquid (d2) is concentrated and dried, to obtain potassium product. The obtained fluorine-containing gas is supplied to multistage-circulation absorption tower and absorbed, to obtain additive and white carbon black. The separated solid (s1) and sodium hydroxide are mixed, alkalized and placed in a microwave reactor, to obtain sodium aluminate.    USE - Industrial microwave processing of potassium-containing rocks (claimed).    ADVANTAGE - The method enables industrial microwave processing of potassium-containing rocks with potassium-addition recovery rate of more than 98% within short period of time, with low energy consumption.    DETAILED DESCRIPTION - A potassium-containing rock is crushed to 80-200 mesh. 10-30% Auxiliary agent and 60-98% sulfuric acid are mixed in a microwave reactor, and microwave frequency and power are adjusted. The material temperature is controlled to 70-100 degrees C. A reaction sample is solid-liquid-separated, to obtain reaction liquid (d1). A liquid neutralizer is added to reaction liquid, to obtain separated solid (s1) and liquid (d2). The liquid (d2) is concentrated and dried, to obtain potassium product. A fluorine-containing gas from microwave reactor is supplied to multistage-circulation absorption tower and absorbed, to obtain additive and white carbon black. The main reaction additives are recycled. The separated solid (s1) and 10-30% sodium hydroxide are mixed, alkalized and placed in a microwave reactor, to obtain sodium aluminate. The microwave frequency and power are adjusted and material temperature is controlled to 90-105 degrees C.
NOVELTY - Mountainous region tea tree fertilizer comprises 20-30 pts. wt. animal excrement, 10- 20 pts. wt. rice bran, 20-30 pts. wt. wheat bran, 30-40 pts. wt. plant straw, 4-6 pts. wt. humic acid, 4-6 pts. wt. minerals, 15-20 pts. wt. calcium superphosphate, 5-10 pts. wt. carbonate, 10-20 pts. wt. potassium chloride, 20-30 pts. wt. ammonium sulfate and 0.6-0.8 pt. wt. microorganism.    USE - Mountainous region tea tree fertilizer.    ADVANTAGE - The fertilizer contains organic and inorganic nutrients.
NOVELTY - Preparation of carbonyldiimidazole comprises dissolving imidazole in hexamethyldisilazane in the presence of potassium carbonate, stirring the reaction, cooling, vacuum distillation, and collecting N-trimethylsilyl imidazole; dissolving diphenyl carbonate in xylene, passing through nitrogen, adding aluminum chloride and sodium methoxide to obtain the N-trimethylsilyl imidazole, and reacting carbonyl diimidazole to obtain the reaction solution; and cooling the carbonyldiimidazole reaction mixture, concentrating, filtering and drying to obtain the carbonyldiimidazole.    USE - Method for preparing carbonyldiimidazole (claimed).    ADVANTAGE - The method is simple and environment-friendly, and has increased conversion rate and product yield.    DETAILED DESCRIPTION - Preparation of carbonyldiimidazole comprises:    (A) dissolving imidazole in hexamethyldisilazane in the presence of potassium carbonate, stirring the reaction at 100-110 degrees C for 5-6 hours, cooling to 45-70 degrees C, vacuum distillation at 75-78 degrees C/1.03 kPa, and collecting N-trimethylsilyl imidazole;    (B) dissolving diphenyl carbonate in xylene, passing through nitrogen, adding aluminum chloride and sodium methoxide to obtain the N-trimethylsilyl imidazole, and reacting with carbonyl diimidazole at 140-150 degrees C for 4-5 hours to obtain the reaction solution; and    (C) cooling the carbonyldiimidazole reaction mixture to 50-60 degrees C, concentrating under reduced pressure, filtering the solid portion and drying in vacuum to obtain the carbonyldiimidazole.
NOVELTY - Preparation of glycyrrhetinic acid comprises ultrasonic wave extracting licorice extract and filtering to obtain 9-70% glycyrrhizic acid content of licorice extract; adding catalyst under ultrasonic condition and carrying out acetylation reaction, where catalyst is sulfuric acid, hydrochloric acid, or phosphoric acid; and adding alkali under ultrasonic wave condition and carrying out deacetylation reaction.    USE - Method for preparing glycyrrhetinic acid (claimed).    ADVANTAGE - The method has short reaction time, reduced amount of solvent, less environment pollution and side reaction, and increased conversion rate, extends raw material range, and solves problems such as raw material, high cost, long reaction time, serious environmental pollution, and low production cost and product purity.
NOVELTY - Preparation of fertilizer comprises reacting wet flue gas from purified waste reactor with ammonium bicarbonate; drying the material to solid-liquid separation, obtaining liquid-cooled supernatant after crystallization as the raw material liquid, pumping into a preheater, allowing the preheated feed liquid to enter the heat exchanger, passing the raw material liquid into the mold separator, crystallizing the supersaturated raw material liquid, and then isolating the material liquid by centrifuging and drying granulated fertilizer.    USE - Method for preparing fertilizer (claimed).    ADVANTAGE - The method changes the waste into valuable, saves consumption of steam, recycles distilled water, and conserves water.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the method for preparing fertilizer (Drawing includes non-English language text).
NOVELTY - Cultivating Pholiota adiposa involves utilizing 60 wt.% herba schizonepetae, 10 wt.% Pleurotus nebrodensis, 10 wt.% cottonseed hull, 19 wt.% wheat bran and 1 wt.% quicklime. Raw materials are crushed into soybean size particles and then dried to obtain dried product. The dried product is mixed with water in ratio of 1:1.4.    USE - Method for cultivating Pholiota adiposa (claimed).    ADVANTAGE - The method enables to cultivate Pholiota adiposa having high yield in a cost-effective manner and in short period of time. The method is eco-friendly and has wide application prospect.
NOVELTY - Generating glycerol ether, comprises: reacting isobutylene with an alcohol to obtain a tertiary alkyl ether through an etherification reaction; and generating glycerol ether from the tertiary alkyl ether and glycerol through a transetherification reaction.    USE - The process is useful for generating glycerol ether.    ADVANTAGE - The process: provides the glycerol ether with improved mass transfer, improved reaction rate, improved catalyst lifetime and improved control of product selectivity; does not require the use of high purity glycerol (permit use of lower purity (and lower cost) glycerol) than existing processes and systems).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for system for generating a glycerol ether, comprising first section for generating a tertiary alkyl ether, where the first section comprises at least one tertiary alkyl ether reactor coupled to an isobutylene feed line and an alcohol feed line, at least one separation unit coupled to the tertiary alkyl ether reactor, tertiary alkyl ether outlet line coupled to the separation unit and tertiary alkyl ether storage tank coupled to the tertiary alkyl ether outlet line and configured to store a tertiary alkyl ether, and second section for generating a glycerol ether from a tertiary alkyl ether and glycerol, where the second section comprises glycerol ether production unit coupled to a tertiary alkyl ether feed line, the tertiary alkyl ether feed line is further coupled to the tertiary alkyl ether storage tank of the first section, and a glycerol feed line and glycerol ether product line configured to remove a glycerol ether from the glycerol ether production unit.
NOVELTY - An organosilane aqueous solution comprises silicon-containing compound (I), acid chosen from lactic acid and an acetic acid, and ethanol.    USE - Organosilane aqueous solution is used as antibacterial agent and antiviral agent. Uses include but are not limited to metal, glass, ceramics, resin, fiber, household material, clothing, towel, mask, foodstuff applications, etc.    ADVANTAGE - The organosilane aqueous solution has excellent anti-viral effect, antibacterial effect, and storage stability for long period of time in normal storage temperature environment, and suppresses gelatinization and cloud formation, and is prepared by simple and environmentally-friendly method.    DETAILED DESCRIPTION - An organosilane aqueous solution comprises silicon-containing compound of formula (I), acid chosen from lactic acid and an acetic acid, and ethanol.    n=1-10;    R1=10-30C alkyl;    R2,R3=1-6C alkyl;and    X-=halo ion.    An INDEPENDENT CLAIM is included for preservation of organosilane aqueous solution, which involves preserving organosilane aqueous solution at -30 degrees C to 50 degrees C.
NOVELTY - The method involves forming a coating film intermittently by coating a coating liquid to a base material. The edge portion of a linear form in the coating film is blurred. The coating liquid is discharged from an ejection opening with respect to the base material. The coating liquid is discharged at speed of V meter per second. The viscosity of the coating liquid is M Pascal per square second.    USE - Formation method of coating film in manufacturing process of fuel cell.    ADVANTAGE - The coating conditions for suppressing linear defect and blur defect are easily adjusted.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view shows the relationship between the length, distance, speed, viscosity and surface tension of the coating liquid.
NOVELTY - The system has a carbonization furnace (3) which heats and carbonizes biomass, and superheated steam generator (4) which heats water vapor and generates superheated steam. Thermal decomposition gasifier (2) has outer cylinder (11) and inner cylinder (12). Composition ratio obtained by carbonized material of gasification area is heated uniformly by radiant heat and superheated steam operates electric power generating apparatus (36) by fixed calorie amount with uniform water gas, while heating inner cylinder and thermal storage property protrusion with combustion exhaust gas.    USE - Electricity-generation-by-biomass system for generating biomass from thermal decomposition gasification of scrap wood of coppiced timber.    ADVANTAGE - The temperature distribution in an area is stabilized according to the synergistic effect. The thermal decomposition gasification efficiency is improved and composition ratio of the emitted water gas is kept constant. Since impurities, such as nitrogen, sulfur, and a tar are removed by the carbonization furnace and the thermal decomposition gasifier, the high generating efficiency is obtained. Thus, safe and efficient electric power is supplied. The temperature distribution is stabilized without using complicated temperature control unit. The energy saving and natural environment protection are achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the electricity generation-by-biomass system. (Drawing includes non-English language text)    Thermal decomposition gasifier (2)    Carbonization furnace (3)    Superheated steam generator (4)    Outer cylinder (11)    Inner cylinder (12)    Electric power generating apparatus (36)
NOVELTY - The utility model is new type relates to one kind composite type biological diesel oil refining and purifying system, including through pipeline in turn each connected with the biologic diesel oil product storage tank, vacuum filter cloth filtering device, methanol distillation tower, biologic diesel oil fine purifying tower, the second heat exchanger and biological refined diesel oil collection tank, methanol distillation tower is connected with the first heat exchanger, the first heat exchanger bottom connected with methyl alcohol collecting tank, in composite type biological diesel oil refining and purifying system increase with an inert gas storage tank, gas boiler and controller. The utility model is novel effective removing residual for the soap, glycerin of biologic diesel oil, catalyst and unreacted raw material and equal impurity, at the same time for use for recovery of excess methanol and biological diesel oil, purity and quality increase quality of biologic diesel oil and accelerates popularization and application of high quality biological diesel oil.
NOVELTY - A one application for biomass fixed bed gasification furnace and the novel banking device, wherein, set with air inlet pipe in the oxidation area part internal gasification furnace, the air inlet pipe mounted with one of intelligent valve, oxidation area of gasification furnace internal part also set with temperature measuring device, the temperature measuring and regulating valve through intelligent temperature control system realize interlocking automatic regulating control, set with discharge chimney at top part of gasification furnace, the discharge chimney with one set of pneumatic switch valve, wherein outlet end of discharge chimney mounted with one of high pressure igniter and one of pipe, high pressure igniter and pneumatic switch valve interlocking control. The utility model is new type with novel structure, furnace temperature maintain more stable, starting time short, efficiency is high, the cost is low.
NOVELTY - A two-section biomass gasification furnace A, lower suction type reaction section is set with the furnace body upper end, on the type reaction section set at lower end of furnace body, and the furnace body middle part fixedly set with jacket sleeve, upper end of sleeve is set with fuel gas input mouth, the top part of lower absorption type reaction section set with feeding port, side face of lower absorption type reaction section formed with multiple of the air inlet A, and the following side suction type reaction section also formed with one multi-temperature measuring thermoelectric couple A, internal space separating the lower sucking type reaction section with dry cell and splitting reaction area, rotating fixing fire grate is set below the fire grate rotating electrical machine and the splitting reaction area connected with the side of the upper reaction section also set with multi-type of two temperature measuring thermoelectric couple, the upper type reaction section of internal space separated with oxidation and reduction area, rotating fire grate set at oxidation area is fixed. The utility model is new type with novel structure, gasification furnace in response the control more stable, tar content low, dust containing rate low, operation is stable, use life is longer is.
NOVELTY - The utility model is new type relates to one kind of biomass straw gasification furnace, belonging to furnace with manufacturing technology field of furnace body, furnace cover, air inlet pipe, blower, a fire grate and discharge tube composed of the discharge tube connected with filter, filter by box body, water tank, dry filter box, a clapboard, a filter screen and out put pipe composed of. Water inside is installed in water tank, upper filter network and dry filter tank is equipped with dry material. Furnace body producing methane gas, through inner discharge pipe enter into water tank, net through water filter, the most tar bonded on water molecule on, again enter into dry filter tank, dry material by using the rest tar and gas adsorption filter, and pure methane after filtering through gas input tube output. The utility model is new type effectively increase have heat efficiency, large amount, and can produce fuel gas purity is higher than 90%, energy saving and environment-friendly, simple structure, suitable operation, the cost is low.
NOVELTY - A one application for the novel air inlet device of biomass gasification furnace, the cylinder wall of oxidation area of gasification furnace internal part are cloth with one multi-air inlet, the upper part of each of the air inlet are mounted with one of thermocouple, periphery of the oxidation part formed with annular, annular wind room through multi-pipe are connected to air inlet are mounted with one of electromagnetic valve of each pipeline on up, each of annular air inlet wind room and sum in furnace cylinder wall and the connecting pipe are mounted with can detachable plug, the annular wind room on installation with pressure transducer, the first way of air blower through wind pipe and furnace for gasification furnace bottom is equipped with bottom wind room connection, air blower and the second way by wind pipe and annular wind room connected; the inlet end wind room and bottom annular wind room and furnace are set with electric adjusting valve and intelligent flow meter, intelligent flowmeter mounted at front end of the electric regulating valve. The utility model is new type with novel structure, working efficiency high, automatic operation, temperature control precision, stable operation, manual cost is low.
NOVELTY - A plant set with dustproof function and new type biomass raw material feedstock device, multi-ton two overlapped for storage yard, each ton of the whole bag is filled with raw material, the bottom of every ton bag set with de-bag wherein, big hook lifting lug is lifting by the electronic weigh, the electronic weigh hook sling is suspended by the travelling crane, the upright storage hopper is placed on the storage yard, the top part is set with one storage bin number, mounted with feedstock wherein the transverse rubber cushion and a brush, to set with rubber bar, the bottom storage hopper fixedly set with transverse transport mechanism, transport mechanism and the lower end of the side of the vertical lifting transport machine is set with enter hopper, transport mechanism and upper end is set with discharging mouth, the discharging end of the transverse transport mechanism and enter the lifting transport machine connection port, place wherein material discharging mouth and gasification furnace top part of lifting transport machine is connected. The utility model is new type with novel structure, dust-preventing effect is good, measuring time and labour force when high measuring precision high, running is stable.
NOVELTY - A novel biomass fuel gas purification plant device, fuel gas and combustion room outlet of each gasification furnace connected, combustion room set with safe anti-explosion pressure relief one, a combustion chamber also set with an air inlet, the air inlet to set with electric regulating valve, inner wall of combustion room fixedly set with high temperature refractory material layer, a combustion chamber also set with temperature measuring thermoelectric couple, outlet end of room and fuel gas pipe and air inlet wherein each connected, entrance end air outlet and dust remover and then the gas phase connected pipe, gas pipe and air inlet to install with out water mouth, gas pipe and air outlet to set with one water inlet, the water inlet A and give water pump connected with the soft water tank and give water pump connected with the fuel gas pipe and the air outlet end also mounted with high temperature oxygen amount; dust collector through pipe and fan implement sum and connected with the burner and boiler is connected with a burner, a boiler set with second water inlet. The utility model is new type with novel structure, the purification effect obvious, running stability high, valid features increase the device use life.
NOVELTY - A high efficient impurity removing device for refining bio-diesel oil comprises filtering separation tank, filtering separation tank comprising sediment slot and a conduit connected with the inside from upper to lower in turn provided with shunt tap, separation chamber, a guide flow plate and the liquid outlet port, separated chamber and upper wall and lower wall are a mesh plate and clapboard are composed of real, separation chamber and side wall is multi-layer steel mesh, separating inner chamber with rotating shaft, rotating shaft connected with motor, between a multi-layer steel mesh and rotary shaft, from upper to lower in turn provided with multi-group filter plate, the filter plate is set with inclined, each filter plate group and the included angle between rotating axis different, from upper to lower in turn angle. A multi-layer steel net is equipped with one layer filter cloth. This utility modelrealizes high efficient impurity removing of waste lipid, and edulcoration effect is good, can increase product purity, and reduces process time.
NOVELTY - A plant for refining biological diesel oil with efficient hot water evaporating device, comprising main body, the main body part is connected with top of the feedstock tube, bottom set with discharging pipe, inside the body set with floating evaporating chamber and stirring heating chamber, in flow drying chamber with incline guide plate, the horizontal incline angle is 10 to 30 degrees, the lower part set with heating rod A, the lower heating rod A is provided with air outlet anti-moisture plate; the air outlet anti-moisture plate A provided with reverse incline guide plate, reverse incline horizontal incline angle of guide flow plate is-10 to 30 degrees, and the lower the provided with heating rod B, rod B is provided with heating air outlet anti-moisture plate B, an air outlet anti-moisture plate B below is heating stirring chamber; in stirring heating chamber provided with stirring rotary pole, rotary stirring pole is connected with electrical machine, stirring at rotating pole set with three multi-stirring blade, stirring in side wall of heating chamber provided with heating block, heating block provided with heat transfer anti-corrosive layer. The device can realize waste lipid efficient removing water, and dewatering effect is good, can increase product purity, reducing process time.
NOVELTY - A plant with collected dust removing function of new type biomass combustion device, gasification furnace top part is set with a feeding port, feeding mechanism and gasification furnace connection, a feeding mechanism feeding to gasification furnace feedstock and wherein, in material machine and give above suspension with platform type cover body, top part of table cover body is provided with a dust suction mouth at its upper end fixedly mounted with filter network, the top part and dust removing wind tube of table cover shape and one end each connected, another end dusting and then connected to inlet of air blower, set with wind quantity regulating bypass and connected with part of air blower inlet in dusting, dusting on also set with pressure sensor, outlet and the burner air blower connected with the gasification furnace through fuel gas pipe and connected with the burner, finally connected with burner and boiler. The utility model is new type with novel structure, dust collecting performance is strong, the de-dusting effect obvious, manual low cost, equipment investment is low, small square meter small, which is more convenient for popularization and application.
NOVELTY - The utility model claims a glycerol water washing device of biological diesel oil preparing technology, the device comprises tank body with interlayer and a separating cabin, the tank body is located under the separating cabin, bottom of the tank body provided with porous plate, top provided with atomizing shower nozzle A and atomization shower nozzle B, orderly filling with stainless steel wires and ceramic ring lower to upper on the tank body internal from and set with light phase outlet and a heavy phase outlet at left side of the separating cabin part and right side of the lower part of the light phase outlet through pipeline and the atomizing shower nozzle A and in turn equipped with a circulation pump A and pump pressure pipeline of A, a heavy phase outlet through pipeline and the atomizing shower nozzle B connected in turn and set with circulation pump B and pressurizing pump pipeline of B, the device using gravity action finish separating the glycerol of biological diesel oil, which avoids strong stirring action cause the phenomenon causing water-glycerol cannot be separated, at the same time can save water, reduce enterprise production cost.
NOVELTY - The utility model is new type supply have one kind biologic diesel esterification reaction acid value balance point sample separating device, wherein said out-like tube also connected with separator, the separator top provided with a stepping motor, the stepping motor connected with screw rod, the screw rod provided with upper compression upper scraping plate and lower scraping plate, compressing the upper compression plate and the low compression scraper scraping plate between the separating cavity inner wall is provided with upper locating convex block on the lower compression scraping plate and the separating cavity between bottom set with lower locating bump, the bottom separating cavity set with residual liquid separating tube wall of the separating cavity side wall provided with an overflow pipe, the overflow pipe at the side wall part provided with an overflow port, between the top part in the overflow port is located on the locating convex block and the separation, the bottom side wall of the overflow pipe set with liquid pipe. The utility model is new type device that have the problem influence residual acid value detection time sampling, and sampling device using residual liquid and sample liquid separated, increase balance point detection precision.
NOVELTY - The invention claims a marsh gas using pressure lifting biogas turbulence effect and high efficient marsh gas generating system, wherein comprising, a feedstock, a discharge pipe, a fermentation pipe, a fermentation level pipe set, a feedstock material and a vertical U-type fermentation pipeline connected with a terminal a, a fermentation pipe of a hydraulic part, a feedstock tube connecting seat for feedstock a drainage hole, a discharging pipe and a position for discharging a drainage hole, a pipeline and fermentation feedstock pipe connecting seat is set with a feedstock to a baffle, a fermentation pipe and discharging pipe connecting seat is set with a discharging pipe to plate, a U type pipe is set with fermentation have set... in a hydraulic connection cloth device fungus, bacteria distributing device of drain pipe, a U-shaped cloth pipe fungus, fungus a cloth composed of, from a feedstock discharge tube and one end connected with a drain pipe of Brucella device, arrange the other end side connected with a water pipe in the pipe in the U type ferment fungus a cloth, a cloth tube and shape of fungus ferment pipe... to ferment for a pipe. A U-shaped pipe of Brucella has set with a vertical upper direction of cloth of a fungus, a U-type channel type fermentation device and fermentation line...... a a and one-way valve, biogas slurry realize full flow within a system, and a uniform distribution of strain, a preventing crust, high yield, suitable for large scale production.
NOVELTY - The utility model claims new of air pressure promoting marsh liquid flow driving Brucella beyond the efficient marsh gas generating system, wherein comprising, feedstock tube, discharging tube, U type fermentation pipe, U type pipe horizontal placing for fermentation, feedstock tube and discharging tube vertical U-type fermentation pipeline connected with two end side, U type pipe upper part set hydraulic pressure ferment, and feedstock pipe connecting seat for feedstock pipe drainage hole, and a discharge tube connected with position for discharging pipe drainage hole, a U type pipe and fermentation feedstock pipe connecting seat is set with one feedstock to tube plate, U type fermentation pipe and discharging pipe connected with seat position is set with one discharging tube plate, upper U type pipe is set with fermentation has set air pipe, in also connected with cloth water pressure device fungus, bacteria distributing device of drain pipe, a U type cloth tube fungus, fungus hole composed of cloth, from feedstock tube and discharge tube one end side connected with bacteria distributing device of drain pipe, arrange the other end side connected with fixed water pipe of each suitable for the U-type inner pipe cloth ferment fungus tube, U type cloth tube and shape of fungus ferment pipe and extending to ferment in pipeline. U-type pipe of Brucella with multi-set of vertical direction of the cloth fungus hole, using U-type channel type fermentation device and fermentation line longer, using control of water pressure difference and one-way valve, biogas slurry realize full flow in in system, and uniformly distributing the driving strain, effective prevent the crusting phenomenon, high yield, suitable for large scale production.
NOVELTY - This new utility model claims of one-way flow biogas fermentation raw material flow into system to promote the efficient marsh gas ferment system, it comprises, the feedstock tube, discharging tube, U type fermentation pipe, U type pipe horizontal placing for fermentation, feedstock tube and discharging tube vertical U-type fermentation pipeline connected with two end side, U type pipe upper part set hydraulic pressure ferment, and feedstock pipe connecting seat for feedstock pipe drainage hole, and a discharge tube connected with position for discharging pipe drainage hole, a U type pipe and fermentation feedstock pipe connecting seat is set with one feedstock to tube plate, U type fermentation pipe and discharging pipe connected with seat position is set with one discharging tube plate, upper U type pipe is set with fermentation has set air pipe, in also connected with cloth water pressure device fungus, bacteria distributing device of drain pipe, a U type cloth tube fungus, fungus hole composed of cloth, from feedstock tube and discharge tube one end side connected with bacteria distributing device of drain pipe, arrange the other end side connected with fixing water pipe for the pipe in the U type ferment fungus cloth tube, U type cloth tube and shape of fungus ferment pipeline for each and extending to ferment in pipeline. U-type pipe of Brucella with multi-set of vertical direction of the cloth fungus hole, using U-type channel type fermentation device and fermentation line longer, using control of water pressure difference and one-way valve, biogas slurry realize full flow in in system, and uniformly distributing the driving strain, effective prevent the crusting phenomenon, high yield, suitable for large scale production.
NOVELTY - This new utility model claims of U-type marsh gas ferment system, it comprises, the feedstock tube, discharging tube, U type fermentation pipe, U type pipe horizontal placing for fermentation, feedstock tube and discharging tube vertical U-type fermentation pipeline connected with two end side, U type pipe upper part set hydraulic pressure ferment, and feedstock pipe connecting seat for feedstock pipe drainage hole, and a discharge tube connected with position for discharging pipe drainage hole, a U type pipe and fermentation feedstock pipe connecting seat is set with one feedstock to tube plate, U type fermentation pipe and discharging pipe connected with seat position is set with one material-blocking pipe board, upper U type pipe is set with fermentation has set air tube, a discharge tube drainage hole seat set with the one-way inner controlling fermentation biogas pipe flow into the one-way valve in water pressure, using U-type channel type fermentation device and fermentation line longer, using control of water pressure difference and one-way valve, biogas slurry realize full flow in in system, and uniformly distributing the driving strain, effective prevent the crusting phenomenon, high yield, suitable for large scale production.
NOVELTY - A drying and granulating apparatus for manufacturing methane fermentation residue comprises rotary drum (11) and polygonal drum (12). Apparatus is operated by drying remaining residue of manufactured methane gas by rotation of rotary drum and combustion heat of methane gas, granulating at timely rotation speed on polygonal drum, carbonizing, sterilizing, and deodorizing by temperature control.    USE - A drying and granulating apparatus for manufacturing methane fermentation residue used as organic fertilizer.    ADVANTAGE - Organic fertilizer can be manufactured over a short period of time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the drying and granulating apparatus for manufacturing methane fermentation residue. (Drawing includes non-English language text).    Rotary drum (11)    Polygonal drum (12)    Heater apparatus (13)    Dust removal apparatus (14)    Deodorizing apparatus (15)
NOVELTY - The device has a rotating first electrode plate (2) which generates a first gas and a second electrode plate (3) which generates a second gas. A voltage application unit applies a voltage between the electrode plates. The first electrode plate and the second electrode plate are contacted with the to-be-processed water. The first electrode plate is applied with voltage from voltage application unit while rotating and generating the first gas supplied in the to-be-processed water.    USE - Electric field type gas generation device, such as a rotary hydrogen gas generation apparatus, and a hydrogen and oxygen generation apparatus, for use in a rain water storage apparatus or a circulating-type toilet.    ADVANTAGE - Defects of gas accumulation between electrodes are eliminated by forming a rotating electrode or both electrodes which oppose from a perforated panel, and diffusing the generated gas. Deposit is not easily attached to the electrode, since the electrode is moving about the rotating electrode, thus, clean electrode is maintained, and the decline in the electric field efficiency resulting from the stain of the electrode is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the electric field type gas generation device.    First electrode plate (2)    Second electrode plate (3)    Power supply (4)    Rotating shaft (5)    Motor (6)
NOVELTY - A hydrogen generating apparatus (100) comprises reactor where raw fuel containing hydrocarbon and catalyst containing nitrogen compound circulate in which nitrogen compound reacts with hydrogen and produces ammonia and produces nitrogen oxide by heating, thermoregulator which adjusts temperature of reactor, and controller (30) which controls thermoregulator so that temperature of reactor during initial operation is lower than temperature of reactor during operation after completion of initial operation.    USE - A hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - The hydrogen generating apparatus easily suppresses mixing of ammonia concentration to hydrogen-containing gas during initial operation, the influence of selective-oxidation catalyst or ammonia to a fuel cell can be reduced, and the domestic fuel cell co-generation system can maintain excellent electric power generation performance over a long term at a low cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) fuel cell system comprising hydrogen generating apparatus and fuel cell electric-power-generated using the hydrogen-containing gas supplied from the hydrogen generating apparatus; and    (2) operation of hydrogen generating apparatus which involves circulating raw fuel containing hydrocarbon in nitrogen compound which reacts with hydrogen and produces ammonia in a reactor, controlling temperature of reactor so that temperature of reactor during initial operation is lower than temperature of reactor during operation after completion of initial operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text).    Modifier (1)    Raw fuel supply device (2)    Water supply machine (3)    Controller (30)    Hydrogen generating apparatus (100)
NOVELTY - The utility model is new type relates to one kind improved type biologic diesel esterification reactor, structure in turn connected first-stage reaction tank, nanometer colloid mill, three-way valve and connected with second grade reaction tank. The utility model is new type can effective treatment containing longer chain of macromolecule raw material lipid, reducing methanol waste rate and improve raw material methyl alcohol and the reaction rate, the biology diesel oil and product quality.
NOVELTY - The utility model is new type relates to one plant for biological diesel production and esterification reaction system, comprising first-stage reaction tank, first-stage nano colloid mill, three-way valve connected with the second grade reaction tank and second level nano colloid mill, first-stage reaction tank, first-stage nano colloid mill, three-way valve connected with the second grade reaction tank and second level nano colloid mill in turn connected, the utility model is new type also integrated with one level adsorption column, second level adsorption column, adsorption column three level and four level adsorption column, adsorption column and three-level class one adsorption column are formed as adsorption column containing the activated coal filler, second level adsorption column and four level adsorption column are set for containing activated coal filler or bald ring filler is adsorption column. The utility model is new type can effective removing of biology diesel oil and ozone substance light component, smell, effective treatment containing longer chain of macromolecule raw material lipid, reducing methanol waste rate and improve raw material and reaction rate of methanol, realize fast single circulation esterification reaction and fast switching between the two time circulation esterification reaction, the biological diesel oil and product quality.
NOVELTY - The utility model is new type supply have one kind ester exchange device increase production of biologic diesel oil, wherein the ester exchanger provided with outside circulation device, the outside circulation device part is coated with water circulation device, the outside circulation device of feedstock end provided with outside circulation control valve, the circulation control valve and outside end part connected with a three-way pipeline, the three-way pipeline connected with two of circulation pump, the circulation pump connected with spiral pipe, the spiral pipe incline is set with shower nozzle a feedstock material for shower nozzle b, the outside circulation control valve and the circulation pump set with middle temperature water circulation of the water circulation device, for the material between a shower nozzle, the material for shower nozzle b and the circulation pump set with high temperature water circulation. The utility model is new type device that have mixed effect difference of problem, increase have ester.
NOVELTY - The new type utility claims have one kind and combination heating type biomass pyrolysis device, comprising pyrolysis system, primary separation system, a condensation separation system, can not condensing gas collecting and metering system, fuel gas recycling system, the carrier supply system and control system sum equal, system, primary separation system, a condensation separation system, can not condensing gas collecting and measuring system in turn in series, gas recycling system and load sum supply system mounted in the pyrolysis system. Sum carrier supply system for biomass pyrolysis atmosphere change, control system device for carbonizing temperature, raising the temperature and gas flow rate and speed monitoring and control. Pyrolysis system producing tri-state product enter into the primary separation system, for separating bottle collecting tar, rest of pyrolysis product enter into the condensing separation system, taking pyroligneous liquid separation bottle collecting, then, may not condensing gas collecting and measuring the combustible gas measuring and collecting system, finally, part can sum after combustion through fuel gas recycling system combustion give pyrolysis system supply heat.
NOVELTY - A biofuel oil comprises 30-50 wt.% waste vegetable oil residue, 5-10 wt.% waste fusel, 30-50 wt.% wash oil, 15-30 wt.% oil and 0.5-2 wt.% additive.    USE - Biofuel oil is used for ships, boiler and heavy oil burner.    ADVANTAGE - The economical and oxygen-rich biofuel oil has excellent combustion performance and thermal efficiency, and low sulfur content, mechanical resistance and sulfide emissions, and is obtained using readily available renewable raw materials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biofuel oil.
NOVELTY - Biofuel particles comprise 45-65 pts. wt. rice straw, 5-15 pts. wt. bamboo shavings, 25-35 pts. wt. tree stems, 3-12 pts. wt. bagasse, and 0.5-1 pt. wt. aluminum-containing dechlorination agent (I).    USE - Biofuel particles are used in boilers.    ADVANTAGE - The biofuel particles have low moisture content and high lignin content, and are capable of controlling chlorine emission, and does not emit harmful gases during combustion. The boiler using the biofuel particles has excellent corrosion resistance.    DETAILED DESCRIPTION - Biofuel particles comprise 45-65 pts. wt. rice straw, 5-15 pts. wt. bamboo shavings, 25-35 pts. wt. tree stems, 3-12 pts. wt. bagasse, and 0.5-1 pt. wt. aluminum-containing dechlorination agent of formula: C23H22O6N2Al (I).
NOVELTY - The apparatus has a mill (3) for fine grinding of organic matter (1), microorganism injection device (4), receiving vessel (14) of crushed material, and blades (16). A screw end (17) arranged in bottom of vessel, leads to oxygenation tank (32) for receiving the compost for oxygenation. A transfer pipe (36) is connected to settling tank (38) and a discharge pump (40). The receiving vessel has a filtered air outlet (19) connected with the air filters (44) and a conduit air outlet (28). The air filtration system includes filled containers of filter material such as pozzolana or zeolite.    USE - Method for mechanical and biological treatment of organic materials. Uses include but are not limited to bone or hard organic material, food residues from kitchens, industrial canteens, convenience foods manufacturers, chokes services, school canteens, and fast or traditional food center, and human or animal waste, and original waste from mowing lawns or green waste of marine algae type, and organic waste like food packaging type cardboard, paper, or wood, etc.    ADVANTAGE - The treatment process of organic materials is carried out without moving or transporting the organic material. Uniform grinding of all organic materials is enabled. The injection system of bacteria provides a homogeneous mixture of organic decomposition. The stabilization of titration bacterial is achieved. Degradation treatment process is accelerated biologically. Total 100% disposal of the treated organic materials is enabled.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for mechanical and biological treatment of organic materials.    Organic matter (1)    Mill (3)    Microorganism injection device (4)    Receiving vessel (14)    Blade (16)    Screw end (17)    Filtered air outlet (19)    Conduit air outlet (28)    Oxygenation tank (32)    Transfer pipe (36)    Settling tank (38)    Discharge pump (40)    Air filter (44)
NOVELTY - The carbonizer (100) has a catalytic converter that is arranged within the exhaust stream. A heat-driven engine is thermally coupled to the exhaust stream. A motor-driven feedstock conveyor is coupled to the combustion chamber (115). A motor-driven blower is communicably coupled between fresh air supply and combustion chamber. A control circuit is coupled to the sensor (710). The set of predetermined values is selected to control quality of biochar delivered by biochar conveyor to the biochar collection chamber and to balance production of biochar and energy production by engine.    USE - Biochar production carbonizer.    ADVANTAGE - The biochar quality is improved by managing the temperature and the dwell time in the pyrolysis pot. The rate of air introduction is increased or decreased at a predetermined rate of change to maintain the level of pyrolysis temperature that maximizes quality, based on a predetermined algorithm of energy output of the feedstock. The quality is improved by increasing dwell time in the carbonizer and/or exposing the biochar to high temperatures.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the of the continuous combined heat, power and biochar carbonizer.    Biochar production carbonizer (100)    Combustion chamber (115)    Motor (700)    Drive shaft (701)    Volatile gas sensor (710)
NOVELTY - The method involves introducing a fuel stream having a reformable fuel into an anode of a molten carbonate fuel cell and an internal reforming element. The cathode inlet stream that includes carbon dioxide and oxygen (601) is introduced into a cathode of the molten carbonate fuel cell. The anode exhaust (607) is generated that includes hydrogen, carbon monoxide, and carbon dioxide. The hydrogen-rich gas stream is separated from at least a portion of the anode exhaust. The portion of the hydrogen-rich gas stream is combusted to produce electricity.    USE - Method for producing electricity using molten carbonate fuel cells..    ADVANTAGE - The method generates electrical power and heat to allow for low-emission energy production at high efficiency with reduced or minimized carbon emissions.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a process for generating electricity.    Oxygen (601)    Exhaust gas stream (603)    Cathode exhaust (604)    Anode exhaust (607)    Hydrogen turbine (650)
NOVELTY - Growing a microbe in a saccharified solution containing a saccharification product comprises obtaining a mixed saccharified solution by diluting the saccharified solution containing a growth inhibitor which inhibits the growth of the microbe with a sugar solution having a smaller growth inhibitor concentration than that of the saccharified solution such that the growth inhibitor concentration is decreased; and allowing the microbe to grow by adding the microbe to the mixed saccharified solution.    USE - The methods are used for growing a microbe in a saccharified solution containing a saccharification product; and producing bioethanol (all claimed).    ADVANTAGE - Convenient, simple and rapid growth method for a microbe which can enhance the growth of the microbe without removing growth inhibitors from a saccharified solution, and a bioethanol production method which can avoid inhibiting the growth of the microbe during fermentation, are provided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a bioethanol production method of saccharifying, with a saccharifying enzyme, a pretreatment product resulting from the pretreatment of lignocellulosic biomass, and fermenting the obtained saccharified solution with a microbe to form ethanol, by obtaining a mixed saccharified solution by diluting the saccharified solution containing a growth inhibitor which inhibits growth of the microbe with a sugar solution having a smaller growth inhibitor concentration than that of the saccharified solution such that the growth inhibitor concentration is decreased; and fermenting the mixed saccharified solution with the microbe to form ethanol.
NOVELTY - Obtaining disulfide oil having sodium level below 0.1 ppm, comprises passing a stream comprising disulfide oil having sodium level of 1 ppm through an alumina bed packed in a column, at a liquid hourly space velocity (LHSV) of 0.5-5 per hour and at a pre-determined temperature to obtain a treated stream comprising disulfide oil having sodium level below 0.1 ppm.    USE - The process is useful for obtaining disulfide oil having low sodium level, where the disulfide oil is useful as an anticoking agent in thermal cracking process, as sulfiding agent for the preparation of catalysts used in hydrotreating and hydrocracking process and in hydrogenation of non-edible vegetable oils to produce biofuels.    ADVANTAGE - The process: process provides treated stream comprising disulfide oil having sodium level below 0.1 ppm, preferably 0.01 ppm (claimed); is very simple, efficient and economical for removal of sodium from disulfide; and provides disulfide oil, which is an economical alternative to the existing anticoking agent in the thermal cracking of hydrocarbons with practically no change in the cracking product composition and/or energy requirement, an economic alternative to the existing sulfiding agents used in the hydro-processing of non edible vegetable oils to produce bio-jet or bio-diesel and an economic alternative to the existing pre-sulfiding agent used in the hydrotreaters and hydrocrackers for the pre-sulfidization of the catalyst.
NOVELTY - Generating and distributing energy with integrated water treatment using biological raw materials, comprises e.g. processing surface water and process water of 1-7 individual stations in a first station, pretreating and treating raw materials in a third station, supplying the fermentation substrate to a fermentation process and producing biogas in a fourth station, dehumidifying the produced biogas in a fifth station, converting the fermentation substrate in a sixth station, and converting biogas into electrical energy, thermal energy or chemical energy in a seventh station.    USE - The method is useful for generating and distributing energy with integrated water treatment using biological raw materials (claimed).    ADVANTAGE - The method produces biogas in quick manner.    DETAILED DESCRIPTION - Generating and distributing energy with integrated water treatment using biological raw materials, comprises processing surface water and process water of 1-7 individual stations in a first station, delivering and storing the raw materials in a second station, pretreating and treating raw materials to a liquid fermentation substrate in a third station, supplying the fermentation substrate to a fermentation process and producing biogas in a fourth station, dehumidifying the produced biogas and/or removing carbon dioxide and/or hydrogen sulfide in a fifth station, converting the fermentation substrate to liquid fertilizer, solid fertilizer and/or compost in a sixth station, and converting biogas into a form of energy, preferably electrical energy, thermal energy or chemical energy in a seventh station.
NOVELTY - Apparatus comprises a foil container (1) surrounding outside ground and/or a supporting structure. The top of the foil container is sealed in a gas-tight manner by a membrane roof (5) and in which a feeding tube (7), an overflow pipe (6) and a gas sampling tube are formed. A container film wall (4) and/or the membrane roof are permeated to be sealed from an upwardly projecting tube, in which a rod as a plunger rested in a slidable manner, which protrudes upwards out of the tube as a handle or with a handle, and at its bottom, carries an end of a mixing head protruding from the tube.    USE - The apparatus is useful for fermentation of biomass for generating gas (claimed).    ADVANTAGE - The apparatus: has structurally simple parts which can be obtained inexpensively anywhere, without having to be adapted to the specific application; allows the construction of a fast and simple structure, can be compact when folded and easy to carry; and ensures optimal mixing of the container contents in the simplest way.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic vertical section of the apparatus for fermentation of biomass.    Foil container (1)    Container film wall (4)    Membrane roof (5)    Overflow pipe (6)    Feeding tube (7)
NOVELTY - The utility model relates to a reverse osmosis membrane concentration device, comprising biogas liquid pool, sand filtering tank, pool, a metering pump, raw liquid tank, core type filter, high pressure pump, reverse permeation film column, d c, concentrated liquid pool, outlet pool, concentration liquid outlet pool, marsh liquid pool set with metering pump through the pipeline and sand filter tank contact, c and raw liquid tank contact, source liquid tank end and a sand filtering tank connected with the raw liquid tank between another end and reverse permeation film column set with high pressure pump, reverse permeation film column respectively connected with and clean liquid pool and concentrated liquid pool, clean liquid pool and concentrated liquid pool respectively set with clear liquid pool outlet and concentrated liquid pool outlet. The concentration effect device is capable of full separating concentrated liquid and has a good clean film column and capacity.
NOVELTY - Method for treating a natural gas stream containing methane and higher hydrocarbon(s), involves forming hydrogen stream by electrolysis of water, mixing portion(s) of the natural gas stream with the hydrogen stream, and supplying the mixture to a supported-precious metal hydrogenolysis catalyst provided in a hydrogenolysis tank (34) at an inlet temperature of 100-300 degrees C to generate a treated gas mixture.    USE - Treatment of natural gas stream containing methane and higher hydrocarbon e.g. ethane, propane, butane and 5C or more paraffin (all claimed).    ADVANTAGE - The method enables efficient and economical treatment of natural gas stream containing methane and higher hydrocarbon(s), by a simple method by using reduced number of heat exchangers.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for treating a natural gas stream, which consists of an unit for generating hydrogen, a mixer operatively connected to the hydrogen generating unit to mix hydrogen with a natural gas stream, and a hydrogenolysis tank containing a supported precious metal hydrogenolysis catalyst, arranged in the tank such that a stream of the mixed natural gas and hydrogen is supplied over the catalyst to generate a treated gas mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of treatment process of natural gas stream containing methane and higher hydrocarbon.    Renewable source (10)    Electrolysis unit (14)    Purification tank (30)    Hydrogenolysis tank (34)    Cooled treated gas stream (40)
NOVELTY - Grain reaping, straw gasification and grain drying integrated continuous operation device, including grain, straw gasification device, a gas storage device, a hot air furnace, grain drying device and grain storage bin, straw transport device, grain transport device, the grain harvester by straw transport device is connected with straw gasification device, the straw gasification device through air inlet pipe connected with air storage device, air storage device through the air outlet pipe connected with hot air furnace, the hot air furnace through exhaust duct connected with grain drying device, the grain by grain transport device connected with harvester grain drying device, the grain drying device by out connected with distributed food grain storage bin. The utility model is new type of beneficial effect is: grain reaping, straw gasification and grain drying for continuous operation, reducing have pollute source of grain and active control have any straw for burning and pollute environment, at the same time by the storage device the have the grain continuous drying, greatly increase have utilization rate of straw gasification.
NOVELTY - The new type utility claims have one plant for organic waste sum purification device of multi-grade pipe type gas distribution device, comprising gas pipe, a first-stage gas distribution device, second level gas distribution device and three-level gas distribution device, the gas main pipe across set in the first-stage gas distribution device, second level gas distribution device and three-level gas distribution device A side, the first-stage gas distribution device, second level gas distribution device and three-level gas distribution device and cross to the gas pipe of each connected, the first-stage gas distribution device, second level gas distribution device and gas distribution device are three grade tube ring is set with multi-hole of the ring tube shape structure. The utility model is new type increase have gas distribution uniformity, using gas and liquid fully contact, reach to maximize biochemical reaction efficiency, reduce have water output power, which avoids have roulette hole blockage, reducing gas short way, reducing have gas pressure drop and gas residence time, using processing efficiency increase is more than 30%, reducing have cost.
NOVELTY - The new type utility claims one kind of biomass energy recovery using system, to solve technology problem: aiming at present to use technology of biomass and recovery, for direct combustion or local buried, exist combustion full and no problem, influence recovery utilization rate and environment with large to pollute and biomass energy use rate and low problem. Using the technology scheme, biomass energy recovery using system, comprising gasification furnace, gas dust separator, dust catcher, a gas-liquid separator, a combustion chamber, a waste heat boiler, a draught fan, a screw conveyor, an airlock, purification circulation water tank, circulation water pump, external user, emptying valve, gasification furnace circulation water tank and cooling water pump. Advantages: the recovery using system, raw material for using process maybe production of waste water and waste gas and design have the corresponding process technology, reach to the zero pollutant discharge " requirement, the biomass material after combustion generating black carbonized material, can be manufacture as charcoal, called biological coal, the utility model is new type not only can energy recovery using the rest product also can obtain the large of economic benefit, is one part raw material of the plant.
NOVELTY - The utility model is new type supply have one plant for sewage and immobilized microorganism treatment device, wherein said microorganism is adsorption on porous material on the porous material and the fibre material is a common agent. Using porous inert medium to carry out adsorption and microorganism with fiber shape material for immobilized microorganism carrier by machine, using immobilized microorganism particle with the higher machine intensity and mass transfer performance, using a key microorganism can be applied and in the actual sewage treatment.
NOVELTY - The new type utility claims have type straw marsh gas pool, of feedstock tube, discharging tube, fermentation pipeline, composed of marsh gas pool main body, pipe horizontal placing for fermentation, feedstock tube and discharging tube vertical set and connected with fermentation pipe two end, horizontal placing for fermentation at the top pipe, respectively and side wall of feedstock tube and discharging tube connected the fermentation pipeline and pipe connection seat to feedstock with feedstock pipe plate is equipped with vertical direction, fermented pipe and discharging pipe connecting seat to set with discharging pipe blocking plate and vertical direction, on fermentation pipeline connected with air pipe, the water pressure in upper part adopt sealing structure, and upper part in water pressure connected with discharge pipe, straw more suitable feedstock, straight cylinder pipe make fermented fermentation route of straw to obtain enlargement, the whole multi-pipe air removing gas and ensure smooth, not easy to be blocked, the utility model is new type reasonable structure, the whole marsh gas pool can adopt concrete casting or glass steel material is made of PVC pipe or connection.
NOVELTY - The new type utility claims have double binding Anaerobic marsh gas fermentation system of one-way circulation flow device, of feedstock tube, discharging tube, pipe and water pressure in fermented fermentation system composed of main body, pipe respectively connected with fermentation feedstock pipe and discharging pipe two end side, to up to fermentation pipeline connected with air pipe, pipeline and fermentation feedstock tube and connecting seat set with feedstock tube plate, fermented pipe and discharging pipe connecting seat is set with discharging pipe plate, placing for fermentation pipe of upper part, between hydraulic pressure between feedstock tube and connected with horizontal placing feedstock pipe and drain pipe, water pressure and discharging pipe connecting with horizontal placing and discharging pipe drain pipe, water pressure in upper part adopt seal set, water pressure in upper part and one discharge pipe connected the feedstock pipe discharging water pipe set up with liquid from the hydraulic control one-way flow into the feedstock pipe one-way valve of feedstock water pipe, a discharging pipe on water discharging pipe set with control liquid discharging tube one-way flow into from water pressure in the discharge pipe and drain pipe check valve, using air pressure difference realization biogas slurry in circulation in the fermentation system, no need to add power not only can realize circulation stirring the biogas and biogas slurry in circulation flow process to promote uniform distribution of strain, further increase fermentation efficiency of fermentation system.
NOVELTY - The new type utility claims have one kind hydraulic Anaerobic stirring tank, comprising a tank body, a bottom layer of the tank body set with sludge discharging device, the discharging device and the sludge tank body except week on surrounding wall provided with at least one hydraulic double stirring device, the stirring device comprises hydraulic end part to stir and pumping the stirring pipe inside the tank body connected with the sludge pump, the sludge pump connected with rotational flow generator, the utility model is new type by water power stirring device for Anaerobic decomposing Anaerobic liquid area by the sludge pump and the sludge out and Anaerobic liquid again to the lower layer in the tank body and form rotational flow, using the following layer comprising Anaerobic fungus is full mixed with the sludge circulation pump work, Anaerobic decomposing area of Anaerobic fungus full attached to in organic object surface, which greatly increase have Anaerobic efficiency, the utility model is new type not damage acidification reaction area is reaction state, is good for acidification reaction and carrying out at the same time, the utility model is new type structure is simple, suitable maintenance, which greatly increase have marsh gas producing efficiency of Anaerobic tank.
NOVELTY - The new type utility claims have one A proton exchange film fuel cell generation system for cable, comprising of coated with conductor and insulation layer composed of the cable core, the conductor using silver plated soft copper strand is made, the cable core is wrapped with metal sheath layer, metal sheath layer using copper with zong binding thread composed of, outside metal jacket layer is covered with outside sheath layer. The utility model is new type structure design is reasonable, use conductor plating silver copper conductor, enhance have corrosion and bear high low temperature performance, metal sheath layer using copper with zong binding thread composed of the sheath is easy to bend, anti-corrosion, bear high low temperature, machine intensity is high. In particular, when insulation layer when using iron fluorin, composed of extruded, it can enhance anti-corrosion, bear high low temperature, anti-stain performance, when outside sheath layer using polyimide coating, bear with high temperature, low temperature bear, the advantages of corrosion resistance, also with low wear and mechanical performance, size stability is good, the heat expand coefficient small, high insulation, low thermal conductivity, good melting is not.
NOVELTY - Production of biodiesel from microalgae biomass comprises taking wet microalgae biomass, hydrolyzing in hydrolysis column to obtain fatty acids, water and crude glycerol, entering fatty acids into reactive distillation column, and esterifying by soaking in presence of heterogeneous catalyst.    USE - Method for producing biodiesel from microalgae biomass used for fuel of compression ignition engines.
NOVELTY - The new type utility claims have one kind microorganism carrier, for use for sewage processing biochemical treatment, comprising: forming microorganism film used for the fiber suspension film layer, wherein the first elastic gauze cover the fiber hanging film layer surface is one, and wherein the second elastic gauze cover another one surface the fiber hanging film layer and, wherein, said the first elastic yarn and the second elastic network yarn between hot connected fixedly. And, the microorganism carrier is always keeping extension state. Because of the silk fiber in fiber hanging film layer is fixed on the whole elastic network yarn between two, also can active the activity of microorganism when the have between multi-microorganism carrier mutual traction of the junction and tear problem, effective maintain have polyvinyl acetal fiber layer than table square meter large, hanging capacity is strong, make microorganism at a multiple of the same stock, to greatly increase sewage treatment efficiency.
NOVELTY - The new type utility claims have one plant using electric network fast pyrolyzing biomass and device, comprising upper flange blind plate, a lower flange plate and set on upper flange and lower flange blind plate between the organic glass cylinder, upper low flange plate placing one block electric wood board, power board set up with one fixed electrode and one of two moving electrode, between fixed electrode and moving electrode fixed with used for carrying sample and screen mesh arranged on the sample are also mounted with collecting card and thermocouple, the thermocouple and used for detecting temperature of external connection, acquisition card and computer with PID module of each interaction. The utility model is new type electric network device small volume, small and cost to realize high pressure operating condition. By improved protective cover, for pressurizing or the experiment under negative pressure state. The utility model is new type except for biomass particle by pyrolysis, also can be for coal powder or other solid fuel particle processing. According to experiment object only needs to select corresponding screen carrying, change and carry volatile and helium flow speed.
NOVELTY - The utility model claims a solar marsh gas processing, energy saving device, comprising a water collecting tank, solar energy heat collector, a marsh gas fermentation tank and collecting tank, the water collecting tank and solar energy heat collector is connected with the solar energy heat collector by the water inlet pipe A and the marsh gas fermentation tank connected with the internal of the marsh gas fermentation tank set with one heating coil, heating plate pipe inlet and outlet through the tank body and respectively connected with the water inlet pipe and water return pipe, the water return pipe and the water collecting tank connected with the internal middle lengthways the marsh gas fermentation tank is set with one stirring shaft, wherein lower terminal of stirring shaft connected with stirring leaf, the marsh gas generating internal tank is also set with one temperature sensor, the top part of the marsh gas fermentation tank set with feedstock mouth and air outlet pipe, the bottom of the marsh gas fermentation tank set with a slag discharging port, the air outlet pipe connected with the collecting tank, the utility model is new type of beneficial effect is: use solar give marsh gas fermentation tank can supply the necessary energy, marsh gas fermentation of keeping the needed temperature, the biogas fermentation tank in four seasons have stable gas production, increase have use rate of biogas fermentation engineering, saves have energy.
NOVELTY - A ruthenium catalyst is obtained by contacting ruthenium precursor having labile ligands and phenol derivative (I) in liquid medium.    USE - Ruthenium catalyst is used in transfer hydrogenation reactions e.g. isomerization of unsaturated alcohols, isomerization of unsaturated carbonyl, hydrogenation of alkenes, hydrogenation of ketones, dehydrogenation of alcohols especially dehydrogenation of isopulegol for manufacturing menthone, dehydrogenating esterification, dehydrogenating coupling of alcohols with amines to amides, alkylation of amines with alcohols, or oxidation of alcohols to aldehydes (all claimed).    ADVANTAGE - The catalyst has increased activity, and ensures high yield and selectivity of transfer hydrogenation products even when used in low concentration.    DETAILED DESCRIPTION - A ruthenium catalyst is obtained by contacting ruthenium precursor having labile ligands and phenol derivative of formula (I) in liquid medium.    R1-R3=H, alkyl, hydroxy;    X,Y'=chemical bond, optionally substituted alkylene, optionally substituted arylene, -O- or -S-;    R4,R5=H, alkyl, hydroxy, optionally substituted aryl;    or R4+R5=optionally substituted arylene;and    or R3,Y'-R4+C=anellated aryl.    An INDEPENDENT CLAIM is included for preparation of menthone, which involves carrying out dehydrogenation or hydrogenation reaction in the liquid phase using isopulegol, ruthenium precursor and phenol derivative (I).
NOVELTY - The device has a shell fixed between an upper cover and a lower cover. An inner part of the shell is connected with a circuit plate that is connected with a wiring terminal. A sensor module is connected with an inner part of the probe main body, where probe main body is fixed with the wiring terminal and a probe. The upper cover and an explosion-proof sheet are formed with a through hole. The shell is connected with a mounting bracket. An alarm device is provided with a loudspeaker. The sensor module is provided with a toxic gas sensor and a combustible gas sensor.    USE - Wireless sensor network technology based building fixed dangerous gas detecting device.    ADVANTAGE - The device detects air poisonous and harmful gas in an effective manner so as to avoid generation of environment pollution and improve operator safety and reduce manufacturing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of a wireless sensor network technology based building fixed dangerous gas detecting device.
NOVELTY - An environmentally-friendly energy-saving fully biodegradable disposable syringe is made of biodegradable polylactic acid substrate having molecular weight of 2000000.    USE - Environmentally-friendly energy-saving fully biodegradable disposable syringe (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of environmentally-friendly energy-saving fully biodegradable disposable syringe, which involves (1) drying biodegradable polylactic acid substrate at 45-55 degrees C for 3-6 hours, (2) adding dried substrate to injection molding machine hopper, where injection molding conditions comprise cylinder inlet temperature of 150-165 degrees C, compression zone temperature of 155-170 degrees C, metering zone temperature of 160-175 degrees C, nozzle zone temperature of 150-180 degrees C, mold temperature of 10-40 degrees C, injection pressure of 50-85 MPa, injection time of 4-5 seconds, dwell time of 0 seconds and speed of 160-180 rpm, and (3) assembling various components of disposable syringe.
NOVELTY - The device has fermentation tank (1) whose feeding port is provided with mounting skirt (2). The lower portion side face of the fermentation tank is opened with a slag (10) and drainage hole (8). The upper end of mounting skirt is provided with air guide hole (4). The diameter of the fermentation tank is slightly smaller than the feedstock. An anti-floating grid (7) is provided on the feeding port. The bottom and side wall of the fermentation tank are respectively arranged with heating device (9) and vapor heating pipe (14).    USE - Fermentation anti-floating non-binding biogas device.    ADVANTAGE - The stirring device is reduced, the structure of the device is simplified, the cost of fermentation tank is reduced, and the cost of the device is reduced. The gas production rate is improved. The temperature inside the tank portion is maintained effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the Fermentation anti-floating non-binding biogas device.    Fermentation tank (1)    Mounting skirt (2)    Air guide hole (4)    Anti-floating grid (7)    Drainage hole (8)    Heating device (9)    Slag (10)    Heating pipe (14)
NOVELTY - The new type utility claims have one kind used for human body respiratory and high purity hydrogen made made oxygen machine, wherein comprising power supply, water tank, an electrolytic pool, membrane, cathode electrode plate, anode electrode plate, the first sum water separator, the first absorbing purifier, the second sum water separator and the second absorbing purifier. The utility model is new type and existing technology compared with the following advantages and effect: using electrolytic water hydrogen made made oxygen, via the first sum and water separator and the first absorbing purifier, production of hydrogen concentration, high purity, can be for people providing hydrogen absorbing function, using antioxidant to damage the hydrogen capacity of removing release and overcome some disease, via the second sum water separator and the second absorbing purifier, producing the oxygen concentration, high purity, can ensure safety of oxygen.
NOVELTY - An edible bacterium culture medium high temperature sterilizing system, an electromagnetic steam generator to the culture medium in a sterilizing room and sterilizing, clean and environment-friendly, high efficiency, electromagnetic steam generator using using electromagnetic heater in a heating furnace to carry out heating of water method, because of a magnetic inner sleeve and a magnetic sleeve are outside a heating body, so can the water in heating furnace to carry out omni-directional heating, heating speed, heating effect is good. can size the sterilizing room according to a multi-scale of electromagnetic heater, and each of electromagnetic heater to carry out a single control, thus it not only is convenient to control and it is easy to maintain in a heating furnace. The sterilization system further using primary refrigerating and cooling device and cooling method not only can ensure the cooling effect and can save energy.
NOVELTY - Hydrogen resistant induced cracking watershed splitter, comprises a tank (16) and a seat base (8), where the upper part of the tank is provided with a spherical upper head (3) and the lower part is provided with spherical lower head (2). The top of the tank is set with an air outlet (1), and the internal part of the tank is provided with a central air inlet and manhole. The inside part of the tank is provided with intake port and vortex prevention baffle. The lower part of the tank is provided sand washing hole, and sand washing tube and level gauge hole.    USE - Used as hydrogen resistant induced cracking watershed splitter.    ADVANTAGE - The splitter has excellent anti-corrosion effect.    DETAILED DESCRIPTION - Hydrogen resistant induced cracking watershed splitter, comprises a tank (16), seat base (8), where the upper part of the tank is provided with a spherical upper head (3) and the lower part is provided with spherical lower head (2). The top of the tank is set with an air outlet (1), and the internal part of the tank is provided with a central air inlet and manhole. The inside part of the tank is provided with intake port and vortex prevention baffle. The lower part of the tank is provided sand washing hole, sand washing tube and level gauge hole; the bottom of the tank is provided with sewage hole, which is provided with outfall, and the tank inner wall is provided with thermal spraying dense alpha -alumina ceramic coating.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen resistant induced cracking watershed splitter.    Air outlet (1)    Spherical lower head (2)    Spherical upper head (3)    Seat base (8)    Tank (16)
NOVELTY - The biological additive comprises 5-20 pts. wt. fungus liquid, 50-100 pts. wt. acetic acid compound, 50-100 pts. wt. ammonium, 10-20 pts. wt. alcohols and 700-900 pts. wt. deionized water. The acetic acid compound is selected from acetic acid, sodium acetate, potassium acetate, ammonium acetate or their mixtures. The ammonium salt is selected from ammonium sulfate, ammonium chloride, ammonium carbonate, ammonium bicarbonate, ammonium nitrate or their mixture. The alcohol compound is selected from glycerol, ethylene glycol, propylene glycol or their mixture.    USE - Biological additive.    ADVANTAGE - The biological additive saves energy, reduces coke boiler, improves efficiency and extends life of the boiler.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biological additive, which involves mixing the raw material in deionized water in a reaction kettle with stirring for 20 minutes.
NOVELTY - Biofertilizer comprises 15-25 wt.% blood powder, 25-35 wt.% leaves, 20-30 wt.% bean cake powder and 20-30 wt.% cotton seed hull.    USE - Biofertilizer used for grafting and promoting root of red peony (claimed).    ADVANTAGE - The biofertilizer is cost-effetive and eco-friendly, promotes crop growth, prevents attack of insect, and does not cause harm to human body.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biofertilizer, which involves:    (A) collecting leaves in September to October, and then mixing components and stirring uniformly to obtain mixture;    (B) stacking the mixture in groove (20 cm) and covering the groove by using plastic thin film; and    (C) taking out the mixture in second year in August to obtain final product.
NOVELTY - The new type utility claims have one plant modified manganese slag clean compound fertilizer production system, comprising prefabricate manganese slag system, compound fertilizer production system and manganese slag drying tail sum processing system, the prefabricate manganese slag system comprises combustion furnace draught fan I, a combustion furnace I, a slag dryer, modified device acidification and neutralization reactor, the compound fertilizer production system comprises combustion furnace draught fan II, burning furnace II, weigh burdening system, a mixer, pulverizer raw material, the compound fertilizer dryer, fertilizer cooling machine, cold air draught fan, a sieving machine, a coating machine and measuring machine, the manganese slag drying tail sum processing system comprises heat exchanger, buffer tank, washing tower, a sediment pool and clear water tank. The utility model is new type adopts high temperature decomposing and preparing phosphoric acid and treatment method for carrying out modified manganese slag, modified manganese slag as raw material for prepare compound fertilizer product, the waste as treasure. In addition, the utility model is new type drying tail sum processing to have full process, which can ensure the environment-friendly clean production.
NOVELTY - The new type utility claims have one plant coal comprehensive utilize slag prefabricate system, comprising coal generating system and prefabricate manganese slag system, the coal generating system comprises two-section coal, tar collector, cyclone dust collector, cutter and urgency before furnace water seal tank, the slag prefabricate system comprises combustion furnace draught fan, a combustion furnace, slag dryer, modified acidification and neutralization reactor device. The utility model is new type aiming at dregs exist and the strong oxidizing substance potassium permanganate and alkaline substance KOH, it adopts high temperature decomposing and preparing phosphoric acid and processing method for processing the modified, manganese slag satisfy using compound fertilizer production requirement, not to crops and soil would cause dangerous not only solves have discharge problem of the waste, but also full use resource waste as treasure. In addition, the utility model is new type using two-section coal gas as heat source device, increase have gas and gasification efficiency, and reducing have pollute environment.
NOVELTY - Distributed type energy system based on municipal marsh gas, relating to municipal energy field, it comprises building marsh gas pool (1), a boiler (2), a methane pipe (3), a steam turbine (4), a generator (5), heat exchanger (6), a fume recovery tower (10), absorption refrigerator (7), heat water pipe (8), water pump (9), cold water out pipe (11) and hot water out pipe (12), a boiler (2) and fuel room through gas pipeline (3) and marsh gas outlet and the marsh gas pool (1), the steam entrance of the steam turbine (4) through pipeline and boiler (2) and steam outlet; the utility model is new type of popularization and use marsh gas supply fuel gas, reducing dye cost, low energy using rate high. The energy conversion ratio is 1 cubic meters of methane production 4kwh power, and with hot water resource is large with good market popularization prospect and comprehensive use value.
NOVELTY - An anaerobic ammonium oxidation bacteria multi-phase mixed culture submerged type injection reflux rapid amplification culture device comprises water flow direction arrangement and particle sludge culture area (2) providing with perforated plate, sludge flocculation culture area (4), biological film culture cell (6) filled with bioceramic particle filler with particle diameter of 4.00-6.70 mm and provided with perforated plate, containing ammonium nitrate and nitrite wastewater water inlet (1) pipeline pump, and cone hopper.    USE - Anaerobic ammonium oxidation bacteria multi-phase mixed culture submerged type injection reflux rapid amplification culture device.    ADVANTAGE - The device is simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic ammonium oxidation bacteria multi-phase mixed culture submerged type injection reflux rapid amplification culture method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of anaerobic ammonium oxidation bacteria multi-phase mixed culture submerged type injection reflux rapid amplification culture device.    Containing ammonium nitrate and nitrite wastewater water inlet (1)    Water flow direction arrangement and particle sludge culture area (2)    Sludge flocculation culture area (4)    Biological film culture cell (6)
NOVELTY - Preparing salicylate comprises adding salicylic acid into reaction vessel containing ionic liquids, adding monohydric alcohol, shaking, mixing uniformly, adding into microwave oven equipped with reflux condenser, cooling reaction mixture to room temperature with saturated, washing with saturated sodium carbonate solution to neutral, stirring, separating salicylate from the aqueous phase, dissolving ionic liquid in aqueous phase, washing sub-salicylate repeatedly with distilled water to remove residual of ionic liquid, placing under an infrared lamp and drying.    USE - The method is useful for preparing salicylate (claimed).    ADVANTAGE - The method has simple operation, mild reaction conditions, short reaction time, high yield and purity, low residual organic solvents, can be easily isolated and purified, and is environment-friendly.    DETAILED DESCRIPTION - Preparing salicylate comprises adding salicylic acid into reaction vessel containing ionic liquids, adding monohydric alcohol, where the molar ratio of salicylic acid and monohydric alcohol is 1:1.5-1.8, shaking, mixing uniformly, adding into microwave oven equipped with reflux condenser at 250W power and radiating for 25-30 minutes, cooling reaction mixture to room temperature, washing with saturated sodium carbonate solution to neutral, stirring, separating salicylate from the aqueous phase, dissolving ionic liquid in aqueous phase, washing repeatedly with distilled water to remove residual ionic liquid, placing under an infrared lamp and drying.
NOVELTY - Preparing glyphosate zinc comprises heating glyphosate and zinc containing compound solution and reacting to obtain glyphosate zinc, where the zinc containing compound is zinc oxide, zinc carbonate, zinc hydroxide or basic zinc carbonate.    USE - The method is useful for preparing glyphosate zinc (claimed).    ADVANTAGE - The method has simple reaction, does not pre-generate sodium salt, and avoids sodium wastewater treatment, is environmentally friendly, separates mother liquor with low glyphosate content, and increases glyphosate zinc yield.
NOVELTY - Jerusalem artichoke powder having particle size having mesh size of 80 plus minus 10, is claimed.    USE - The Jerusalem artichoke powder is useful for preparing purified alcohol, preferably ethanol (claimed) which is useful for producing biofuel.    ADVANTAGE - The Jerusalem artichoke powder produces 99.2% ethanol, and consumes minimal energy.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) Jerusalem artichoke fermented liquid, preparation by mixing the Jerusalem artichoke and water in a ratio of 1:4, and extracting the mixture at 80 plus minus 2 degrees C for 1 hour using hot water; (2) Kluyveromyces marxianus strain activated at 30 plus minus 1 degrees C and 200 revolutions per minute (rpm) for 12 hours; (3) one-step fermentation alcoholic fermentation, performed by taking liquid comprising 200 g/l Jerusalem artichoke powder, inoculating the K.marxianus strain, fermenting the mixture at 30 plus minus 1 degrees C for 120 hours and maintaining pH of the fermented mixture at 4.8-5.2; and (4) purified alcohol, obtained using hydrophobic adsorption, or multistage distillation.
NOVELTY - Preparing quick heart pain relieving granule comprises e.g. providing rhizoma ligustici wallichii, bark of tree peony root and borneol, taking hemlock parsley and moutan bark, adding in 3 times of mass of 90-99% alcohol aqueous solution, heating and refluxing, extracting for two times, filtering, mixing two filter liquor, using rotating film at 65 degrees C, recovering under reduced pressure at 80 degrees C, concentrating to paste, collecting paste, drying, smashing, adding borneol, mixing to obtain the mixture, adding sucrose, starch or dextrin, uniformly mixing, pelletizing, and drying.    USE - The method is useful for preparing quick heart pain relieving granule (claimed).    ADVANTAGE - The granule is economical, safe, and has quick effect, and is easy to carry. The method has short operating time, achieves high active ingredient transfer rate, ensures the safety of the operator, and is suitable for industrial large production.    DETAILED DESCRIPTION - Preparing quick heart pain relieving granule comprises (i) providing 401 pts. wt. rhizoma ligustici wallichii, 240 pts. wt. bark of tree peony root and 26 pts. wt. borneol, and (ii) taking hemlock parsley and moutan bark with volume concentration of 3 times of mass of 90-99% alcohol aqueous solution, heating and refluxing, extracting for two times, first time for 2.5 hours and the second time for 2 hours, filtering, mixing two filter liquor, using rotating film at 65 degrees C, recovering under reduced pressure at 80 degrees C, concentrating to paste at relative density of 1.15-1.20, collecting paste 20 plus minus 5%, drying, smashing, adding borneol, mixing uniformly to obtain the mixture, adding 1-5 times of sucrose, starch or dextrin and uniformly mixing, pelletizing, and drying to obtain the product.
NOVELTY - Traditional Chinese medicine comprises 5-10 pts. wt. borneol, 80-400 pts. wt. medlar, 200-400 pts. wt. Rehmannia, 100-200 pts. wt. Angelica, 2-6 pts. wt. ginseng saponin, 200-300 pts. wt. mulberry, 200-300 pts. wt. Chrysanthemum, 0.04-0.05 pts. wt. vitamin A, 0.8-1.2 pts. wt. zinc lactate, 40-50 pts. wt. Gentiana, 40-60 pts. wt. Lygodium japonicum, 30-40 pts. wt. walnut and 0.3-0.8 pts. wt. alkaloid.    USE - Traditional Chinese medicine, in the form of wet compress or ointment (claimed), used for treating eye fatigue.    ADVANTAGE - The medicine promotes blood circulation. It has simple preparation, is convenient to use, and has high stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of traditional Chinese medicine comprising mixing raw materials, performing ultrasonic wave extraction using 60-80% ethanol for 40-45 minutes, filtering, concentrating, recovering alcohol, and refrigerating.
NOVELTY - Bioactive organic fertilizer comprises organic fertilizer obtained from Sarcophaga peregrina larvae treatment together with tobacco leaves and microorganism powder obtained together with inorganic salt fertilizer. Microorganism powder comprises mixture of nitrogen-fixing bacteria, Bacillus subtilis and Enterobacter cloacae.    USE - Bioactive organic fertilizer used for cotton (claimed).    ADVANTAGE - The bioactive organic fertilizer is economic and wide industrial applicability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bioactive organic fertilizer, which involves crushing and drying components, and then mixing auxiliary material and granulating.
NOVELTY - Preparing fertilizer involves utilizing 100kg planting matrix containing selenium-chromium enriched Cordyceps militaris, 100kg biological coal obtained from bamboo coal, charcoal or straw waste, 1000kg water and 1050kg fermented strain (liquid), and then processed to prepare into solid powder, granular fertilizer or liquid fertilizer.    USE - Method for preparing fertilizer (claimed) used for cultivating plant.    ADVANTAGE - The method is simple and cost-effective, enables to prepare fertilizer that has disease-resistant, cold-resistant and drought-resistant abilities.
NOVELTY - Solubilizing homogeneous catalysis biodiesel separation of ionic liquids by adding alcohol and oil into a reactor, adding reactants of butyl p-toluenesulfonate triethyl ammonium ionic liquid catalyst, reacting, stirring to obtain a mixture containing biodiesel, cooling, layering stationary the biodiesel upper phase and a trace of methanol, removing the methanol by distillation, and recovering by filtration to obtain butyl-p-toluenesulfonate triethyl ammonium ionic liquid catalyst.    USE - Method for solubilizing homogeneous catalysis biodiesel separation of ionic liquids (claimed).    ADVANTAGE - The method has simple operation, fast reaction speed, high conversion rate, easy product separation and purification, cheap ionic liquid catalyst price, and reduced production cost; and is environment-friendly.    DETAILED DESCRIPTION - Solubilizing homogeneous catalysis biodiesel separation of ionic liquids comprises adding alcohol and oil at a mol ratio of 5:1-12:1 into a reactor, adding 10-20 mass% reactants of butyl p-toluenesulfonate triethyl ammonium ionic liquid catalyst, reacting at 80-120 degrees C, stirring for 50 minutes-5 hours to obtain a mixture containing biodiesel, cooling in a water bath for 1-1.5 hours, layering stationary the biodiesel upper phase and a trace of methanol, removing the methanol by distillation to give the desired product of lower phase glycerin, butyl p-toluenesulfonate triethyl ammonium ionic liquid catalyst and a mixture of excess methanol, and recovering by filtration to obtain butyl-p-toluenesulfonate triethyl ammonium ionic liquid catalyst.
NOVELTY - The new type utility claims have one pig manure plant efficient using system, comprising marsh gas pool, marsh gas generation device, fertilizer fermentation pool, chemical fertilizer, organic fertilizer, barbecuing and pig manure collecting groove is located under the piggery, pig manure collecting groove discharging mouth connected with the solid liquid separating device, the solid liquid separating device of material outlet respectively connected and feedstock wherein the fertilizer in fermentation pool and marsh gas pool, liquid outlet also connected and feedstock wherein the marsh gas pool, fermentation pool through fertilizer feeding mechanism and compound fertilizer drying room connected, a discharging port and marsh gas pool connected with marsh material solid-liquid separating device, marsh material solid-liquid separating device of material outlet and organic fertilizer drying room connected, the air outlet and the marsh gas power generation device of marsh gas pool connected with marsh gas generation device and barbecuing electric connection, and also chemical fertilizer, organic fertilizer, solid liquid separating device, solid-liquid separating device and marsh material feeding mechanism connected with power, the system and can give play to pig and use value.
NOVELTY - Foliar fertilizer comprises 28-30 wt.% corn flour, 8-15 wt.% sodium selenite, 15-20 wt.% monopotassium phosphate, 4-6 wt.% zinc sulfate, 3-5 wt.% fungus insecticide, 5-8 wt.% magnesium sulfate and 0.5-2 wt.% cyhalothrin.    USE - Foliar fertilizer used for planting corn (claimed).    ADVANTAGE - The foliar fertilizer increases corn yield, prevents pest attack, kills insect eggs, reduces corn loss and promotes corn root and light photosynthesis, and ensures fungicidal effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing foliar fertilizer, which involves stirring corn flour with water uniformly to obtain mixture that is stirred with remaining material at 200-240 degrees C for 2 minutes to obtain another mixture, which is cooled to obtain product.
NOVELTY - Bio-organic fertilizer comprises cotton straw (40-60 parts), lime powder (20-30 parts), human and animal feces (35-50 parts), potassium sulfate (5-10 parts), and sand (15-20 parts).    USE - Bio-organic fertilizer used for preventing fall of cotton and peach (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-organic fertilizer, which involves:    (A) mixing ingredients under stirring condition;    (B) fermenting obtained mixture in anaerobic condition in cellar for 30-50 days in summer and 60-90 days in winter;    (C) drying fermented product in air;    (D) pelletizing dried product; and    (E) packing obtained product in bags.
NOVELTY - Microbial inoculant comprises Thermosyntropha tengcongensis, Thermosyntropha lipolytica, Syntrophothermus lipocalidus, Methanothermobacter thermautotrophicus, Methanothermobacter marburgensis, Methanoculleus thermophilus, Methanothermobacter wolfeii, Methanosarcina thermophila, Methanothrix thermoacetophila.    USE - Microbial inoculant used for degrading complex fatty acids and long-chain fatty acids found in kitchen garbage, slaughtering waste, lipid processing waste and oil-rich feedstock and for synthesizing acetic acid from methane and carbon dioxide (all claimed).    ADVANTAGE - The microbial inoculant increases the gas production rate from oil-rich feedstock by shortening the fermentation time. The microbial inoculant also avoids serious upper fat accumulation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing microbial inoculant, which involves mixing Thermosyntropha tengcongensis, Thermosyntropha lipolytica, Syntrophothermus lipocalidus, Methanothermobacter thermautotrophicus, Methanothermobacter marburgensis, Methanoculleus thermophilus, Methanothermobacter wolfeii, Methanosarcina thermophila, and Methanothrix thermoacetophila to obtain a composite microbial agent, which is then stored at 2-8 degrees C to obtain the finished product.
NOVELTY - A Staphylococcus pasteuri, which is a recombinant S. pasteuri, having a preservation number of CGMCC No. 10255, is new.    USE - The Staphylococcus pasteuri is useful in a high-level oxidation reaction system and in the removal of ammonia nitrogen, humic acid and benzene in sewage under a different condition (claimed).    ADVANTAGE - The S. pasteuri can be effectively used in sewage treatment, and has the advantages that ammonia nitrogen and benzene-series compounds in industrial waste water and landfill leachate can be effectively removed, and then the quality of discharged water meets the national requirement and standard.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) a method of preparing the S. pasteuri; and (2) use of the S. pasteuri in a high-level oxidation reaction system and in the removal of ammonia nitrogen, humic acid and benzene in sewage under a different condition, and advanced oxidation reaction sewage system for UV and ozone unit oxidation reactor.
NOVELTY - Preparing collagen using porcine lung comprises: (a) pretreatment of minced porcine lung using 0.2-0.4% alkaline solution for soaking for 20-40 minutes; (b) quantitatively taking and weighing raw materials, adding deionized water, sterilization at 80-85 degrees C for 30-40 mining, and cooling to 40 degrees C; (c) taking 0.1-0.3 wt.% pretreated material and adding earthworm serine protease; (d) enzymatically controlling process conditions; (e) ultrafiltration, adding purified water, and dialyzing; and (f) drying to obtain collagen.    USE - The method is useful for preparing collagen using porcine lung (claimed).    ADVANTAGE - The lung collagen preparation method can greatly save extraction and purification time, and can reach greater than or equal to 90% yield. The collagen protein has evenly distributed molecular weight, high purity, and high activity, can be more easily absorbed under mild conditions, and is environment-friendly.
NOVELTY - Recovery of sodium iso-octoate from pharmaceutical waste liquor involves evaporating pharmaceutical waste liquor, removing residual solvent, separating semi-solid waste, acidifying resultant waste, adjusting pH value, stirring for 30 minutes, adding extractant, leaving still, separating oil phase and aqueous phase, distilling oil phase, washing, separating crude, adding ethylhexanoate and sodium alkali and reacting.    USE - Recovery of sodium iso-octoate from pharmaceutical waste liquor generated during production of ampicillin sodium, amoxicillin and cephalosporin antibiotics.    ADVANTAGE - The method enables efficient recovery of sodium iso-octoate as salt-forming agent from pharmaceutical waste liquor.
NOVELTY - Biogas is introduced into diluted enzyme solution in presence of oxygen and hydrogen sulfide, and temperature and pressure are controlled, to obtain hydrate slurry. The unhydrated gas is collected, to obtain desulfurized and decarbonized biogas. The resulting hydrate slurry is solid-liquid-separated, and the liquid phase comprises concentrated enzyme solution.    USE - Desulfurization and decarbonization of biogas (claimed).    ADVANTAGE - The method provides biogas having high methane purity, little effect on enzyme activity and reduced energy consumption, by simple method.
NOVELTY - The device (100) has a housing (110) that is provided with an electrolysis target supply unit (120) for supplying the electrolysis target for electrolysis. An electrolyte supply unit (130) supplies electrolyte for maintaining conductivity of target. A power supply unit (140) supplies he power source for electrolysis. A detection sensor (160) detects the concentration of electrolyte stored in housing. A concentration control unit (161) controls the amount of electrolyte stored in housing according to detected concentration of electrolyte.    USE - Electrolysis device of power generation blower system (Claimed).    ADVANTAGE - Since the electrolysis device supplies hydrogen and oxygen of more than predetermined amount to the turbine, the electricity is produced effectively and the energy production efficiency of the power generation blower system is raised.    DETAILED DESCRIPTION - An electrode portion (150) is equipped in the inner structure of housing, to electrolyze the electrolysis target using the power supplied through power supply unit, and produces hydrogen and oxygen. An INDEPENDENT CLAIM is included for power generation blower system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the electrolysis device. (Drawing includes non-English language text)    Electrolysis device (100)    Housing (110)    Electrolysis target supply unit (120)    Electrolyte supply unit (130)    Power supply unit (140)    Electrode portion (150)    Detection sensor (160)    Concentration control unit (161)
NOVELTY - A negative cylinder (4) is connected to negative terminal of power source while cooling water (20) is flowed in central portion of bipolar tub (2). A partition wall partition element (6) is inserted between bipolar tub and negative cylinder. The oxalic acid gas is sampled to electrolyte reservoir (12) when electrolyte (8) is received in bipolar tub. The electrolyte circulation hose (14) is connected with electrolyte reservoir to form electrolyte cycle line (16). The electrolyte is cooled by cooling unit when temperature of electrolyte flowing in bipolar tub is in certain range.    USE - Apparatus for generating hydrogen gas and oxygen gas.    ADVANTAGE - The production efficiency of the hydrogen gas and oxygen gas generating apparatus is improved and the temperature of the electrolyte is efficiently lowered due to the cooling circulation line.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen gas and oxygen gas generating apparatus.(Drawing includes non-English language text)    Bipolar tub (2)    Negative cylinder (4)    Partition wall partition element (6)    Electrolyte (8)    Electrolyte reservoir (12)    Electrolyte circulation hose (14)    Electrolyte cycle line (16)    Cooling water (20)
NOVELTY - Fertilizer comprises bacterial mixed liquid, salt, beef extract and peptone containing culture medium and solid medium. Solid medium comprises crude oil. Bacterial mixed liquid comprises Bacillus, Bacillus coagulans, Paenibacillus, Enterobacter, Bacillus licheniformis and Enterobacter. Bacterial mixed liquid is inoculated in high salt beef extract peptone culture medium.    USE - Fertilizer used for repairing petroleum polluted alkali salt soil (claimed).    ADVANTAGE - The fertilizer is prepared in a simple and cost-effecive manner, improves soil air permeability, reduces soil salinity content below 6.1g/kg, and ensures high petroleum contaminated soil degrading rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) inoculating bacterial mixed liquid in high salt beef extract peptone culture medium, and then culturing in water bath at 3 degrees C with speed of 140 revolutions per minute for 5 days to obtain microorganism liquid;    (B) reinoculating microorganism liquid in crude oil culture medium of beef extract and peptone at 30 degrees C with speed of 140 revolutions per minute, and then sterilizing for 20 minutes; and    (C) culturing the product at 37 degrees C for 3 days, and then sealing at 4 degrees C.
NOVELTY - Method for cultivating organic rice, involves soaking rice seeds in water, sterilizing rice seeds, preparing rice seedlings, planting seedlings, applying 1-5 kg/m2 bio-organic fertilizer and processed leaves, where the moisture content of the soil is 35-45%, and performing field management.    USE - The method is useful for cultivating organic rice (claimed).    ADVANTAGE - The method improves yield of rice, and provides high nutrient content.
NOVELTY - Method for preparing agent for controlling kiwifruit canker, involves using (a) amino acid soluble powder, anhydrous zinc chloride, and anhydrous manganese chloride, (b) ciprofloxacin or ciprofloxacin lactate original drug, 14% methyl chloride isothiazolinone agent, and copper quinoline original drug, (c) motilin, 5-nitroguaiacol sodium salt original drug, and alpha -naphthylacetate original drug, and (d) molasses fermentation concentrate, sodium polyacrylate powder, and liquid fertilizer.    USE - The method is useful for preparing agent for controlling kiwifruit canker, and treating bacterial disease (all claimed) and fungal disease.    ADVANTAGE - The method prepares agent with long-acting slow release function.    DETAILED DESCRIPTION - Method for preparing agent for controlling kiwifruit canker, involves using (a) 200 pts. wt. amino acid soluble powder, 40-50 pts. wt. anhydrous zinc chloride, and 45-65 pts. wt. anhydrous manganese chloride (nutrient raw material), (b) 40-80 pts. wt. ciprofloxacin or ciprofloxacin lactate original drug, 100-200 pts. wt. 14% methyl chloride isothiazolinone agent, and 100-150 pts. wt. copper quinoline original drug (components for killing bacteria), (c) 0.1 pt. wt. motilin, 0.1 pt. wt. 5-nitroguaiacol sodium salt original drug, and 0.5 pt. wt. alpha -naphthylacetate original drug (promoting plant tissue cell), and (d) 350-450 pts. wt. molasses fermentation concentrate, 0.2-0.25 pt. wt. sodium polyacrylate powder, and 50-60 pts. wt. liquid fertilizer (liquid fertilizer auxiliary raw material).
NOVELTY - Method for preparing modified biological microrganism carrier support involves (a) uniformly mixing the mixture containing 0.5-1 kg biological residues and 1 L mixed liquid, (b) aging the mixture at room temperature for 12-24 hours, and filtering mixture containing biological residues to obtain filtrate, (c) drying the filtrate to obtain modified biological residue support, and pulverizing the biological residue into coal powder and (d) mixing biomass and mixed liquid containing 12.5-20% inorganic acid, 0.01-1 mol/l organic material, and remainder of water.    USE - The method is useful for preparing modified biological support (claimed) used in wastewater treatment.    ADVANTAGE - The method is simple, cost-effective and environmentally-friendly, and reduces the usage of external carbon source.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for modified biological support, which is prepared by the above-mentioned method.
NOVELTY - Starch wastewater treatment comprises discharging starch wastewater through pipe into regulating pool, regulating pH; pumping to reflux well, heating; flowing to anaerobic tank, performing anaerobic fermentation to obtain marsh gas and first stage sewage; discharging first-stage sewage, and carrying out follow-up process; and storing marsh gas storage to temporary storage tank for further processing.    USE - Method for treating starch wastewater (claimed).    ADVANTAGE - The method yields biogas which can be used as energy source, greatly reduces sewage effluent COD concentration, and has good energy saving effect. The treated wastewater discharge meets standards.
NOVELTY - Starch wastewater processing method comprises discharging starch wastewater into regulating pool, regulating wastewater acid value; pumping to reflux well, heating; flowing to anaerobic tank, fermenting to obtain marsh gas and first-stage sewage, storing marsh gas into temporary storage tank; taking first-stage sewage discharge to first-stage aerobic tank, performing aerobic degradation with activated sludge; sedimenting, taking supernatant as second-stage sewage; discharging to second stage aerobic pool, performing aerobic degradation using active sludge; and settling.    USE - Method for processing starch wastewater (claimed).    ADVANTAGE - The method yields biogas which can be used as energy source, greatly reduces sewage effluent COD concentration, and has good energy saving effect. The treated wastewater discharge meets standards.    DETAILED DESCRIPTION - Starch wastewater processing method comprises discharging starch wastewater into regulating pool through pipe, regulating wastewater acid value; pumping to reflux well, heating; flowing to anaerobic tank, performing anaerobic fermentation to obtain marsh gas and first-stage sewage, storing marsh gas into temporary storage tank; taking first-stage sewage discharge to first-stage aerobic tank, performing aerobic degradation with activated sludge; sedimenting, taking supernatant as second-stage sewage; discharging to second stage aerobic pool, performing aerobic degradation using active sludge; sending to final settling tank, and taking supernatant as final sewage discharge.
NOVELTY - Biodiesel production involves mixing anhydrous methanol, potassium removal agent, and liquid basic catalyst in a mixer uniformly. The formed mixture is transferred into tubular plug flow reactor under ultrasonic treatment for performing transesterification reaction to form crude biodiesel and glycerol. The formed crude biodiesel is separated, and then washed to form the finished biodiesel.    USE - Method for producing biodiesel.
NOVELTY - Preparation of biomass curing-forming fuel comprises using Pinus rigida and coal as raw materials and carrying out compression molding at 70-120 degrees C using binder with pressure of 75-120 MPa. The content of Pinus rigida is 80-100 wt.%. The content of coal is 0-20 wt.%. The particle size of Pinus rigida is 0-2.5 mm. The particle size of coal is 0-1.0 mm. The moisture content of Pinus rigida and coal is less than or equal to 15%.    USE - Method for preparing biomass curing-forming fuel (claimed) used for heating and cooking process in homes, factories, power plants, catering and other industries and used as substitute for coal.    ADVANTAGE - The method is environment-friendly. The product has high calorific value, less ash content, large density and high mechanical strength.
NOVELTY - Experimental apparatus comprises first mud pipe (1), reaction chamber (2), Chinese medicine distribution room (3), dosing pipe (4), diversion chamber (5), stirring impeller (6), heating sleeve (7), guide plate (8), separation chamber, first drainage pipe (10), guide tube, oil outlet, drain line, mud pipes, horizontal screw discharging centrifuge, drum, discharging machine inner shell, discharging machine shell, drainage pipe, second mud pipe, lifting pump, mud pipe, pulverized coal blending machine, pulverized coal mixing impeller, coal opening, slime discharge port, wheel and control panel.    USE - Experimental apparatus for coal bearing sludge system (claimed).    ADVANTAGE - The device has simple operation and good treatment effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a structure schematic diagram of experimental apparatus.    First mud pipe (1)    Reaction chamber (2)    Chinese medicine distribution room (3)    Dosing pipe (4)    Diversion chamber (5)    Stirring impeller (6)    Heating sleeve (7)    Guide plate (8)    Separation chamber (9)    First drainage pipe (10)
NOVELTY - A diesel oil is circularly prepared by mixing glycerol and free fatty acid at ratio of 1:3-2:1 at 200-275 degrees C at pressure of 40-760 mmHg, esterifying to obtain ester mixture, adding alkali catalyst and low carbon alcohol, mixing, rotary esterifying, phase separating to obtain biodiesel oil solution and glycerol solution, mixing acid solution and glycerol solution, regulating pH to 3.5-5.5, generating salt precipitate, filtering to remove salt precipitate, and heating to remove low carbon alcohol and water.    USE - Method for circularly preparing diesel oil (claimed).    ADVANTAGE - The method does not need to add acid catalyst, and reduces production cost.
NOVELTY - Generating biogas involves taking fermentation raw material and then pouring it into a feedstock tube (44) laid with an inner annular pipe (30) of multi-zone pressure generating device (40). The amount of fermentation raw material is passed into the feedstock tube, which is equipped with a one-way check valve (40). The fermentation area promotes the flow of fermentation raw material through micro-organism containing duct (52). The fermentation raw material is processed into large fermentation area under high air pressure to generate biogas, which is then collected by a drain outlet pipe (42).    USE - Method for generating biogas using multi-zone pressure generating device (claimed).    ADVANTAGE - The method enables to generate biogas using multi-zone pressure generating device containing balanced amount of biogas promoting microbial strains, in an efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biogas generating multi-zone pressure generating device.    Inner annular pipe (30)    Multi-zone pressure generating device (40)    One-way check valve (40)    Drain outlet pipe (42)    Feedstock tube (44)    Micro-organism containing duct (52)
NOVELTY - Producing biogas involves taking fermentation raw material and then pouring it into a feedstock tube (44) laid with an inner annular pipe (30) of multi-zone pressure generating device. The amount of fermentation raw material is passed into the feedstock tube, which is equipped with a one-way check valve (40). The fermentation area promotes the flow of fermentation raw material through micro-organism containing duct (52). The fermentation raw material is processed into large fermentation area under high air pressure to generate biogas, which is then collected by a drain outlet pipe (42).    USE - Method for producing biogas (claimed).    ADVANTAGE - The method enables to generate biogas using multi-zone pressure generating device containing balanced amount of biogas promoting microbial strains, in an efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biogas generating multi-zone pressure generating device.    An inner annular pipe (30)    One-way check valve (40)    Drain outlet pipe (42)    Feedstock tube (44)    Micro-organism containing duct (52)
NOVELTY - Producing biogas involves taking fermentation raw material and then pouring it into a feedstock tube (10), which then guided by a feedstock pipe (12) of U-shaped fermentation system. The amount of fermentation raw material is passed into the feedstock tube, which is equipped with a one-way check valve (40). The fermentation area promotes the flow of fermentation raw material through a fermentation pipe (30) into micro-organism containing duct (50). The fermentation raw material is processed into fermentation area under pressure to generate biogas, which is then collected by a drain pipe (20).    USE - Method for producing biogas by U-shaped fermentation system (claimed).    ADVANTAGE - The method enables to produce biogas by U-shaped fermentation system, in an efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biogas U-shaped fermentation system.    Feedstock tube (10)    Feedstock pipe (12)    Drain pipe (20)    Fermentation pipe (30)    One-way check valve (40)    Micro-organism containing duct (50)
NOVELTY - Producing biogas involves taking fermentation raw material and then pouring it into a feedstock tube (44) laid with an inner annular pipe (30) of highly efficient multi-zone pressure generating device. The amount of fermentation raw material is passed into the feedstock tube, which is equipped with a one-way check valve (40). The fermentation area promotes flow of fermentation raw material through micro-organism containing duct (52). The fermentation raw material is processed into large fermentation area under high air pressure to generate biogas, which is then collected by a drain pipe (42).    USE - Method for producing biogas using highly efficient multi-zone pressure generating device (claimed).    ADVANTAGE - The method enables to produce biogas using highly efficient multi-zone pressure generating device, in a productive manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biogas generating multi-zone pressure generating device.    An inner annular pipe (30)    One-way check valve (40)    Drain pipe (42)    Feedstock tube (44)    Micro-organism containing duct (52)
NOVELTY - Phlorizin extraction involves mixing slurry in aqueous solution of ethyl alcohol with stirring to obtain extracting liquid, and then filtering the formed mixture by centrifugation or decompression for carrying out solid-liquid separation to get supernatant. The obtained supernatant is added in aqueous solution of inorganic salt for forming double water phase system, which is extracted with stirring. The extracted mixture is kept for a predetermined time to form a layer, which is decompressed to obtain phlorizin.    USE - Method for extracting phlorizin (claimed).    ADVANTAGE - The method extracts the phlorizin in a simple, cost-effective and eco-friendly manner by using non-toxic organic solvent.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation depicting two-phase system phase diagram. (Drawing includes non-English language text).
NOVELTY - Brick-concrete anaerobic power generation gas station has anaerobic tank, purification tower, anaerobic tank heating system and generating units. The anaerobic tank construction materials are essentially comprises brick and reinforced concrete.    USE - Brick-concrete anaerobic power generation gas station in sewage farms for producing biogas (claimed).    ADVANTAGE - The brick-concrete anaerobic power generation gas station efficiently and economically produces biogas with high production efficiency, without affecting the environment.
NOVELTY - Chemiluminescence enhancement solution comprises chemiluminescence substrate made of mannosamine derivative (I).    USE - Chemiluminescence enhancement solution used for improving immunoassay detection sensitivity.    ADVANTAGE - The environmental-friendly chemiluminescence enhancement solution has improved immunoassay detection sensitivity, and is thus capable of generating linear range. The chemiluminescence enhancement solution solves the reagent dependence on imports, and is thus prepared in a cost-effective manner.    DETAILED DESCRIPTION - Chemiluminescence enhancement solution comprises chemiluminescence substrate made of mannosamine derivative of formula (I).    R=8-40C group; and    Y'=negative ions.    An INDEPENDENT CLAIM is included for a method for preparing chemiluminescence enhancement solution, which involves:    (A) dissolving mannosamine in water, followed by addition of acridine orange, bovine serum albumin, glycine, mannosamine, amino acid analyzer and ammonium chloride-ammonia buffers; and    (B) stirring the prepared mixture uniformly to obtain solution, followed by addition of magnesium chloride and hexanolamine solution under stirring condition to obtain the finished product, which is then diluted by adding balanced amount of water.
NOVELTY - Method for producing saccharides from biomass using immobilized enzyme, involves (a) performing physical pretreatment of biomass by pulverizing the biomass, and (b) saccharifying product obtained in step (a) using immobilized enzyme.    USE - The method is useful for producing saccharides from biomass using immobilized enzyme (claimed).    ADVANTAGE - The method is cost-effective to perform, and environmentally-friendly, reduces loss of biomass, avoids generation of toxic byproducts, and improves yield of saccharides and recovery rate of enzyme.
NOVELTY - Selenium-enriched plant nutrient agent comprises 25.30 wt.% dry dairy manure, 25-30 wt.% dry straw, 30-38 wt.% attapulgite, 5-7 wt.% selenium source, 2-3 wt.% potassium phosphate, 2-3 wt.% calcium superphosphate, and 2-3 wt.% plant ash.    USE - Used as a selenium-enriched plant nutrient agent.    ADVANTAGE - The plant nutrient agent: has good slow-release effect; and is convenient for long-term preservation. The mixing device: can achieve the automatic addition of different powders in batches at intervals; avoids the trouble and cost of manual operation; reduces powders adhered on the inner wall of a tank body through vibration; and is low in noise during operation, simple in structure and convenient to dismount and replace.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for mixing device for mixing the selenium-enriched plant nutrient agent, comprising a tank body and a stirring stick (4). The tank body is set with a feedstock inlet, a discharging port (16) and a stirring pole insertion port. The feedstock inlet is divided into a first feeding port (11) and a second feeding port (12). The stirring stick is set with a rotatable clapboard. The clapboard is set with at least one through-hole. The clapboard is located in the tank body at the lower edge of the internal feedstock inlet. The clapboard can be rotated. The position of the through-hole and feedstock inlet is aligned or staggered. The stirring stick is mounted with a regulating mechanism (7) for regulating stirring blades.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the mixing device for mixing the selenium-enriched plant nutrient agent.    Stirring stick (4)    Regulating mechanism (7)    First feeding port (11)    Second feeding port (12)    Discharging port (16)
NOVELTY - Production of high-quality fuel involves mixing biomass feedstock, additive and acidic solution, carrying out microwave hydrolysis treatment, then subjecting to microwave dehydration treatment, condensing generated pyrolysis volatiles, performing solid-liquid separation, and etherifying.    USE - Production of high-quality fuel used as gasoline and diesel.    ADVANTAGE - The method enables simple production of high-quality fuel having excellent storage stability, with high yield.
NOVELTY - Recovering 3-( alpha -methoxy)-methylene-benzofuran-2(3-hydrogen)-one comprises introducing hydrogen chloride (HCl) exhaust gas generated from salicylaldehyde nitrile synthesis to azoxystrobin product containing 3-hydroxy methylene-benzofuran-2(3-hydrogen)-one and potassium salt washing liquid for neutralizing, regulating pH to 2-3, stirring, filtering, water washing, drying to obtain 3-hydroxy methylene-bonzofuran-2(3-hydrogen)-one (I) solid; introducing HCl exhaust gas to methanol to obtain 3-8% HCl-methanol solution; mixing with compound (I), and carrying out multistage etherification reaction.    USE - Method for recovering 3-( alpha -methoxy)-methylene-benzofuran-2(3-hydrogen)-one (claimed).    ADVANTAGE - The method achieves comprehensive utilization of production waste, and reduces production cost and environmental pollution.
NOVELTY - A process of fermentation system of one-way circulation flow stirring promoting fungus involves fermenting raw material in cell producing marsh gas, collecting adjacent blocking plate (32) between formation, pushing flow biogas feedstock tube (10), discharging tube (46), cloth device in pipe (30), drain pipe and cloth bacteria hydraulic one-way input to biogas at pressure level of slurry liquid and discharging pipe (44) drain reaching lowest position, and finishing circulation of slurry in descending area of feedstock tube drain one-way reflux pipe using the marsh gas in other cell.    USE - A process of fermentation system of one-way circulation flow stirring promoting fungus for producing methane.    ADVANTAGE - Gas production is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the process of fermentation system of one-way circulation flow stirring promoting fungus.    Feedstock tube (10)    Pipe (30)    Blocking plate (32)    Discharging pipe (44)    Discharging tube (46)
NOVELTY - A methane generating system comprises feedstock tube (10), discharging tube (20), straight pipe (30) which is mounted between top of feedstock tube between hydraulic pressure level with feedstock tube and drain pipe, pipeline which is connected with feedstock tube and discharge tube with two end sides, water pressure discharge tube (40) which is connected with horizontal discharging pipe and drain pipe (42), feedstock tube plate, discharging pipe blocking plate which connects pipe and discharge pipe, cloth device, cloth bacteria of drain pipe, and cloth bacteria pipe which is straight pipe.    USE - A methane generating system.    ADVANTAGE - Gas production is increased.    DETAILED DESCRIPTION - A methane generating system comprises feedstock tube (10), discharging tube (20), straight pipe (30) which is mounted between top of feedstock tube between hydraulic pressure level with feedstock tube and drain pipe, pipeline which is connected with feedstock tube and discharge tube with two end sides, water pressure discharge tube (40) which is connected with horizontal discharging pipe and drain pipe (42), feedstock tube plate, discharging pipe blocking plate which connects pipe and discharge pipe, cloth device, cloth bacteria of drain pipe, cloth bacteria pipe which is straight pipe, feedstock pipe discharging water pipe wet with control water pressure and marsh liquid one-way flow, and cloth bacteria which extends to water pressure in lowest point of one side and horizontal plane.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the methane generating system.    Feedstock tube (10)    Discharging tube (20)    Pipe (30)    Water pressure discharge tube (40)    Drain pipe (42)
NOVELTY - A process of generating methane involves using super-efficient biogas liquid turbulent flow type generating system, fermenting raw material in cell producing marsh gas, collecting adjacent blocking plate (32, 34) between the formation, increasing pressure in cell in slurry flow of feedstock tube (10), discharging tube (20), cloth device in pipeline and flow into water in pressure in discharge pipe water way and cloth device flow, and finishing circulation of slurry using marsh gas in other cell.    USE - A process of generating methane.    ADVANTAGE - Biogas slurry circulation flow stirring performance, and gas production are increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the super-efficient biogas liquid turbulent flow type generating system.    Feedstock tube (10)    Discharging tube (20)    Pipe (30)    Air guide pipe (31)    Blocking plate (32, 34)
NOVELTY - A Trametes versicolor T4 (CGMCC No. 9582) is new.    USE - New Trametes versicolor T4 (CGMCC No. 9582) for pre-processing lignin raw material under alkaline condition (claimed).    ADVANTAGE - Pre-processing efficiency of lignocellulose raw material is high, and cost is low.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of Trametes versicolor in pre-processing lignin raw material under alkaline condition.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the detection of Trametes versicolor and T4 development tree.
NOVELTY - A synergist comprises main active ingredient consisting of phosphoric acid diglyceride, glucose, and EDTA tetrasodium salt.    USE - A synergist for increasing biogas production.    ADVANTAGE - The synergist improves efficiency of methane fermentation and increases biogas production. Biomass recycling can be promoted, and environment can be protected.
NOVELTY - Method of using high pressure methane generation system to promote uniform distribution of methane producing bacteria involves fermenting raw material in fermentation system to produce biogas, accumulating biogas in fermentation zone formed between adjacent blocking plates (36, 38), allowing pressure in methane fermentation zone to increase, allowing biogas to flow in pipeline feeding tube (10), discharge tube (20), cloth device, and hydraulic discharge pipe (44), using fermentation zone biogas, lowering biogas pressure in fermentation area, and circulating biogas slurry.    USE - Method of using high pressure methane generation system to promote uniform distribution of methane producing bacteria.    ADVANTAGE - Problems relating to poor slurry mixing performance, uneven distribution of species, and low efficiency of gas production can be solved.    DETAILED DESCRIPTION - Method of using high pressure methane generation system to promote uniform distribution of methane producing bacteria involves fermenting raw material in fermentation system to produce biogas, accumulating biogas in fermentation zone formed between adjacent blocking plates (36, 38), allowing pressure in methane fermentation zone to increase, allowing biogas to flow in pipeline feeding tube (10), discharge tube (20), cloth device, and hydraulic discharge pipe (44), using fermentation zone biogas, lowering biogas pressure in fermentation area, circulating biogas slurry in pipeline feeding tube and cloth pipeline, completing circulation of biogas slurry, and using other biogas in fermentation zone.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a methane generation system.    Pipeline feeding tube (10)    Discharge tube (20)    Blocking plates (36, 38)    Hydraulic discharge pipe (44)
NOVELTY - Use of excess activated sludge is claimed for preparation of long-chain polyhydroxyalkanoate by adding sodium laurate as carbon source substrate to original household sludge to obtain 1 g sludge mixed liquid containing 1 g laurate, 0.6 g magnesium sulfate heptahydrate (MgSO47H2O), 0.016 g ammonium chloride (NH4Cl), 0.1 g EDTA, 0.092 g dipotassium phosphate (K2HPO4), 0.045 g monopotassium phosphate (KH2PO4), 0.07 g calcium chloride dihydrate (CaCl2.2H2O), 0.334 g peptone, 0.124 g yeast extract, and 2 ml trace elements and producing poly-3-hydroxybutyrate-3-hydroxy caproate.    USE - Use of excess activated sludge for preparation of long-chain polyhydroxyalkanoate (claimed).    ADVANTAGE - The method is simple and operation is easy, without the need for sterile working condition and expensive raw material sources.    DETAILED DESCRIPTION - Use of excess activated sludge is claimed for preparation of long-chain polyhydroxyalkanoate by adding sodium laurate as carbon source substrate to original household sludge to obtain 1 g sludge mixed liquid containing 1 g laurate, 0.6 g magnesium sulfate heptahydrate (MgSO47H2O), 0.016 g ammonium chloride (NH4Cl), 0.1 g EDTA, 0.092 g dipotassium phosphate (K2HPO4), 0.045 g monopotassium phosphate (KH2PO4), 0.07 g calcium chloride dihydrate (CaCl2.2H2O), 0.334 g peptone, 0.124 g yeast extract, and 2 ml trace elements and adding sodium laurate as carbon source substrate to activated household sludge to produce poly-3-hydroxybutyrate-3-hydroxy caproate in which amount of mixed liquor suspended solid (MLSS) is 2 g/L, and amount of sodium laurate is 0.5-1.5 g/L, NH4Cl is 0-0.16 g, and K2HPO4 is 0-0.092 g/L. An INDEPENDENT CLAIM is included for preparation of long-chain polyhydroxyalkanoate which involves adding sodium laurate as the only carbon source once or twice in a reactor with the household sludge at each time interval of 4 hours at 25-30 degrees C for 12-16 hours.
NOVELTY - Method for preparing a fermented lysine involves culturing fermentation bacterium in a medium, feeding carbon and nitrogen sources to the medium, and performing fermentation. The fermentation process includes fermenting bacteria in growth phase at a temperature of 30-38 degrees C, and fermenting acidogenic bacteria at a temperature of 32-42 degrees C, where fermentation temperature of bacteria in growth phase is lower than acidogenic bacteria.    USE - The method is useful for preparing fermented lysine (claimed).    ADVANTAGE - The method effectively improves production of lysine concentration and fermentation conversion rate, and shortens fermentation cycle, and reduces energy consumption.
NOVELTY - Silybin is synthesized by using peroxidase as catalyst, taking taxifolin, coniferyl-alcohol as substrate, and taking hydrogen peroxide as receptor.    USE - Enzyme-catalyzed synthesis of silybin.    ADVANTAGE - The method is safe because it avoids use of organic solvent and has high reaction efficiency, resulting in conversion rate of 85.31%.
NOVELTY - A specific primer pair for detecting recurrent respiratory papilloma caused by human papillomavirus type 6 (HPV6) is new.    USE - The specific primer pair and kit are useful for detecting recurrent respiratory papilloma caused by HPV6 (claimed).    ADVANTAGE - The specific primer pair and kit are useful for environment-friendly, simple and rapid recurrent respiratory papilloma detection with high accuracy.    DETAILED DESCRIPTION - A specific primer pair for detecting recurrent respiratory papilloma caused by HPV6, comprises aaccctgtatccaaagttg and ccaccttaaataccctgta (SEQ ID NO. 1 and 2), given in the specification. An INDEPENDENT CLAIM is a kit for detecting recurrent respiratory papilloma caused by HPV6, comprises a specific primer pair comprising SEQ ID NO. 1 and 2, and a probe comprising ccacggatgcttatgttactcgct (SEQ ID No. 3), given in the specification.
NOVELTY - Recovery of catalyst, involves washing the ruthenium catalyst by adding washing solvent to ruthenium catalyst in a mass ratio of 1-4:1, preferably 2:1, adjusting pH to 9-14, stirring for 2 hours, reflux-washing at 20-80 degrees C for 1-24 hours, leaving still, settling, and filtering catalyst.    USE - Method for recovering catalyst used in metribuzin intermediate oxidation reaction (claimed).    ADVANTAGE - The catalyst recovery process is simple, environmentally-friendly, economical, and suitable for industrial application.
NOVELTY - Method for cultivating Agaricus mushroom in northeast region involves culturing mycelium in potato dextrose agar culture medium to obtain mother mycelium, culturing mother mycelium in wheat grain culture medium to obtain elite mycelium, adding water to fermentation feedstock including 50-70 %mass corn core and 15-30 %mass cow dung as main material and having moisture content of 50-60%, fermenting, heating, sterilizing, adding elite mycelium and culturing.    USE - Method for cultivating Agaricus mushroom in northeast region (claimed).    ADVANTAGE - The method enables cultivation of Agaricus mushroom in northeast region by environmentally-friendly process.    DETAILED DESCRIPTION - Method for cultivating Agaricus mushroom in northeast region involves culturing mycelium in potato dextrose agar culture medium at 25 degrees C for 13-15 days to obtain mother mycelium, culturing mother mycelium in wheat grain culture medium at 25 degrees C for 15-20 days to obtain elite mycelium, adding water to fermentation feedstock including 50-70 %mass corn core and 15-30 %mass cow dung as main material and having moisture content of 50-60%, fermenting in an incubator at 37 degrees C for 2 days, heating fermented material at 57 degrees C for 3 days, sterilizing, adding elite mycelium and culturing at 20-25 degrees C for 13-17 days in dark. The fermentation feedstock comprises 97% main material and 3% additive. The moisture content of the fermentation feedstock is less than 40%, after fermentation process. The additive comprises 0.5-1.5 %mass lime, 0.5-1.5 %mass stone bone, 0.5-1.5 %mass superphosphoric acid and 15-30 %mass bran. The wheat grain culture medium is prepared by mixing 98 %mass wheat grains, 1 %mass lime and 1 %mass gypsum and sterilizing at 121 degrees C for 2 hours.
NOVELTY - Cultivating orange, by taking orange seedlings, planting the orange seedlings in sandy soil, applying potassium fertilizer, nitrogen fertilizer, organic fertilizer, rapeseed cake and fermentation agent, where the organic fertilizer comprises one or more of manure, straw powder, leaf powder, plant ash and organic waste, applying potassium fertilizer, nitrogen fertilizer, organic fertilizer, rapeseed cake and fermentation agent, applying fertilizer once during March-April and autumn, and twice during summer season, and stopping fertilization after October.    USE - The method is used for cultivating orange (claimed).    ADVANTAGE - The method improves fruit quality.    DETAILED DESCRIPTION - Method for cultivating orange, involves taking orange seedlings, planting the orange seedlings in sandy soil having pH of 6-7, applying 12-25 %mass potassium fertilizer, 14-23 %mass nitrogen fertilizer, 50-65 %mass organic fertilizer, 8-15 %mass rapeseed cake and 0.2-0.7 %mass fermentation agent within radius of 70-89 cm, where the organic fertilizer comprises one or more of manure, straw powder, leaf powder, plant ash and organic waste, applying potassium fertilizer, nitrogen fertilizer, organic fertilizer, rapeseed cake and fermentation agent, applying 40-65 kg/acre fertilizer once during March-April and autumn, and twice during summer season, and stopping fertilization after October.
NOVELTY - Decoloring of dyed soft gelatin capsule shell waste material involves adding water to polyacrylamide, stirring, obtaining polyacrylamide aqueous solution (A), adding water to dyed soft gelatin capsule shell waste material, aging to expand the waste material, heating resultant mixture at 35-85 degrees C until the waste material is completely dissolved, obtaining dyed soft gelatin capsule shell waste aqueous solution (B), mixing solution (A) and solution (B), flocculating more than 2 times, separating supernatant, and obtaining bright yellow clarified liquid.    USE - Decoloring of dyed soft gelatin capsule shell waste material (claimed).    ADVANTAGE - The method enables economical decoloring of dyed soft gelatin capsule shell waste material with stable quality and high recovery rate of gelatin, by simple and environmentally-friendly process.    DETAILED DESCRIPTION - Decoloring of dyed soft gelatin capsule shell waste material involves weighing polyacrylamide, adding water to polyacrylamide, stirring until polyacrylamide is completely dissolved, obtaining polyacrylamide aqueous solution (A), weighing dyed soft gelatin capsule shell waste material, adding water to dyed soft gelatin capsule shell waste material, aging to expand the waste material, heating resultant mixture at 35-85 degrees C until the waste material is completely dissolved, obtaining dyed soft gelatin capsule shell waste aqueous solution (B), mixing solution (A) and solution (B), flocculating more than 2 times, separating supernatant until the supernatant is bright yellow clear liquid, and obtaining bright yellow clarified liquid. The concentration of dyed soft gelatin capsule shell waste aqueous solution is 1-25%.
NOVELTY - Method for performing circular treatment for processing agricultural organic solid waste, involves subjecting portion of agricultural organic solid waste to ensilage, hydrolysis, first-stage fermentation and second-stage fermentation to produce biogas, purifying the obtained biogas, subjecting the other portion of the agricultural organic solid waste to rice straw silage fermentation, crushing the fermented mixture, subjecting obtained product to solid-liquid separation, adding microbial complex, and preparing high-grade solid and liquid organic fertilizers.    USE - The method is useful for performing circular treatment for processing agricultural organic solid waste which is useful for producing biogas and preparing high-grade solid and liquid organic fertilizers (claimed).    ADVANTAGE - The method is rapid, performed in controlled manner, and environmentally-friendly.    DETAILED DESCRIPTION - Method for performing circular treatment for processing agricultural organic solid waste, involves subjecting portion of agricultural organic solid waste to ensilage, hydrolysis, first-stage fermentation and second-stage fermentation to produce biogas, purifying the obtained biogas, where portion of the biogas is directly used, and the other portion of the biogas produces high-temperature and high-pressure steam through steam generator to supply heat for HPS reaction kettle, subjecting the other portion of the agricultural organic solid waste to rice straw silage fermentation, crushing the fermented mixture, subjecting the obtained product to solid-liquid separation, adding microbial complex, and preparing high-grade solid and liquid organic fertilizers. An INDEPENDENT CLAIM is included for apparatus for performing the above-mentioned method, which comprises stirring unit, anaerobic fermentation tank equipped with the stirring unit, hot water heating equipment, and dual membrane gas holder.
NOVELTY - Bioorganic fertilizer is prepared by mixing fresh dairy manure, fresh sheep manure, fresh chicken manure, and fine powder of dry plant straw, and adding trace elements, and performing fermentation process.    USE - As bioorganic fertilizer.    ADVANTAGE - The bioorganic fertilizer promotes growth of crop, restrains soil-borne disease, and promotes nutrients of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing bioorganic fertilizer, which involves mixing the 30-50% fresh dairy manure, 20-25% fresh sheep manure, 10-30% fresh chicken manure, and fine powder of dry plant straw for 10-13 minutes, and adding Bacillus subtilis, ammonium sulfate, potassium sulfate, monoammonium phosphate, manganese sulfate, and sodium selenite, uniformly mixing mixture for 10-15 minutes, fermenting mixture at 35-40 degrees C for 24 hours, and 38-43 degrees C for 12 hours, and crushing fermented product.
NOVELTY - Synthesis of dapoxetine hydrochloride (1) involves subjecting 3-chloro-1-phenylpropan-1-one (9) and (-)- beta -chlorodiisopinocampheylborane to reduction reaction, obtaining (1R)-3-chloro-1-phenylpropan-1-ol (12), reacting naphthalen-1-ol (8) and alkali, adding the compound (12), alkylating, obtaining (1R)-3-(naphthalen-1-yloxy)-1-phenylpropan-1-ol (13), reacting the compound (13) and thionyl chloride, obtaining 1-((3R)-3-chloro-3-phenylpropoxy)naphthalene (14), reacting the compound (14) and dimethylamine, and reacting obtained product with ethanol solution of hydrogen chloride.    USE - Synthesis of dapoxetine hydrochloride (claimed).    ADVANTAGE - The method enables synthesis of high-purity dapoxetine hydrochloride with high yield.    DETAILED DESCRIPTION - Synthesis of dapoxetine hydrochloride of formula (1) involves subjecting 3-chloro-1-phenylpropan-1-one of formula (9) and (-)- beta -chlorodiisopinocampheylborane to reduction reaction in organic solvent (s1) at 10-80 degrees C, obtaining (1R)-3-chloro-1-phenylpropan-1-ol of formula (12), reacting naphthalen-1-ol of formula (8) and alkali in an organic solvent (s2) at 0-10 degrees C for 2-14 hours, adding the compound (12), performing alkylation reaction at 0-10 degrees C for 15-40 hours, obtaining (1R)-3-(naphthalen-1-yloxy)-1-phenylpropan-1-ol of formula (13), reacting the compound (13) and thionyl chloride in an organic solvent (s3) at -10 degrees C to 0 degrees C, obtaining 1-((3R)-3-chloro-3-phenylpropoxy)naphthalene of formula (14), reacting the compound (14) and dimethylamine in an organic solvent (s4) at 20-30 degrees C, obtaining dapoxetine free amine, and reacting obtained product with ethanol solution of hydrogen chloride.
NOVELTY - Preparation of 2-acetyl-phenothiazine involves mixing phenothiazine, diphenylamine and sulfur with catalyst, stirring and heating at 185-190 degrees C in inert gas, heating at 200-205 degrees C, cooling, and reacting acetic acid and dimethylaniline with the obtained phenothiazine compound. The molar ratio of diphenylamine and sulfur is 1-1.5:1.    USE - Preparation of 2-acetyl-phenothiazine (claimed).    ADVANTAGE - 2-Acetyl-phenothiazine is prepared with high purity and yield with reduced environmental pollution.
NOVELTY - Curved type methane fermentation and generation device comprises feed tube for introducing raw material for fermentation process, collecting pipe, discharge pipe, adjacent blocking plate for extruding biogas slurry, fermentation chamber for performing fermentation process and storing fermented product, feeding pipe, water pressure chamber, and drainage pipe.    USE - The curved type device is for methane fermentation and generating methane (claimed).
NOVELTY - Method for culturing Rhodospirillum rubrum, involves (a) inoculating R.rubrum into culture medium comprising seawater, ammonium chloride, sodium dihydrogen phosphate, yeast extract, sodium acetate, ammonium sulfate, sodium molybdate and boric acid, and culturing strains, (b) nurturing culture, and serially passaging the strains to 3-6 generations, and (c) culturing the strains obtained in step (b) at 25-35 degrees C under light intensity of 10000-70000 lx for 9-15 days, in natural medium.    USE - The method is useful for culturing R.rubrum for degrading organic contaminations of aquiculture (claimed) of crab, shrimp or fish.    DETAILED DESCRIPTION - Method for culturing Rhodospirillum rubrum, involves (a) inoculating R.rubrum into culture medium comprising 1 l seawater, 0.1-1.5 g ammonium chloride, 0.2-2.7 g sodium dihydrogen phosphate, 2.5-9.6 g yeast extract, 2.7-6.8 g sodium acetate, 0.1-1.5 g ammonium sulfate, 0.05-0.15 g sodium molybdate and 0.05-0.15 g boric acid, and culturing strains for 3-10 days, where pH of the culture medium is 6.5-7.8, (b) nurturing culture obtained in step (a), and serially passaging the strains to 3-6 generations, and (c) culturing the strains obtained in step (b) at 25-35 degrees C under light intensity of 10000-70000 lx for 9-15 days, in natural medium comprising 0.5 l aquaculture water sludge, 0.1-1.5 g ammonium chloride, 1.5-3.5 g magnesium sulfate, 0.15-0.56 g glutamate, 0.25-0.75 g ferrous sulfate and 0.5 l seawater, where pH of the natural medium is 7-8.
NOVELTY - Preparing rhamnolipids by semi-solid state fermentation, by adding potassium dihydrogen phosphate, magnesium sulfate, sodium nitrate, and glycerol to agricultural wastes, adding water upto 1 l, sterilizing to obtain semi-solid state fermentation medium, inoculating 6% Pseudomonas aeruginosa (CCTCC AB93066) in the medium, fermenting the mixture at 37 degrees C and 100-150 revolutions per minute (rpm) for 12 days, and subjecting the fermented product to pasteurization at 80 degrees C for 30 minutes, or steam sterilization at 80 degrees C for 15 minutes.    USE - The method is used for preparing rhamnolipids for repairing heavy metal contaminated soil. The heavy metal is lead, cadmium, arsenic, copper or chromium (all claimed).    ADVANTAGE - The prepared rhamnolipids have effect of inhibiting pathogenic bacteria.    DETAILED DESCRIPTION - Method for preparing rhamnolipids by semi-solid state fermentation, involves adding 5-10 g/l potassium dihydrogen phosphate, 0.1-1 g/l magnesium sulfate, 2-10 g/l sodium nitrate, and 10-60 g/l glycerol to 150-160 g/l agricultural wastes, adding suitable amount of water upto 1 l, sterilizing at 121 degrees C for 15 minutes to obtain semi-solid state fermentation medium, inoculating 6% Pseudomonas aeruginosa (CCTCC AB93066) in the medium, fermenting the mixture at 37 degrees C and 100-150 revolutions per minute (rpm) for 12 days, and subjecting the fermented product to pasteurization at 80 degrees C for 30 minutes, or steam sterilization at 80 degrees C for 15 minutes. An INDEPENDENT CLAIM is included for use of the rhamnolipids for repairing heavy metal contaminated soil.
NOVELTY - Intercropping cassava and Dictyophora involves taking bamboo, straw and weeds, taking biogas, biogas residue, urea and livestock poultry manure, drying mixture, stacking, fermenting, turning every 15 days to obtain fermentation culture material, digging 8-10 cm deep hole in sandy loam, sowing Dictyophora fungus culture in late March with seeding rate of 0.5-1 kg/m2, covering with straw, taking cassava seedlings, sowing in late February, transplanting cassava using in-line method with 70-90 cm spacing, controlling growing conditions and performing water management.    USE - Method for intercropping cassava and Dictyophora (claimed).    ADVANTAGE - The method reduces pests, and increases land utilization rate.
NOVELTY - Composting waste gas treatment apparatus comprises primary gas filter tank (5), secondary gas filter tank (14) and biological bed (15). The primary gas filtering tank is connected by air inlet pipe (1), discharge pipe (6), liquid inlet pipe (2), liquid discharging pipe (7), hole (3) and sampling hole. The biological bed is a rectangular pool comprising distributing pipeline (19), wood (18), ripe compost layer (17) and humidifying pipe (16). The composting waste gas treatment apparatus also comprises ammonia furnace (12) comprising heater (10) and temperature sensor (11).    USE - Composting waste gas treatment apparatus used for removing odor, paticularly hydrogen sulfide, sulfur dioxide, mercaptans, amines and other malodorous gases generated during composting, from waste gas (claimed).    ADVANTAGE - Ammonia produced by the composting is used.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of composting waste gas treatment apparatus.    Air inlet pipe (1)    Liquid inlet pipe (2)    Hole (3)    Primary gas filter tank (5)    Discharge pipe (6)    Liquid discharging pipe (7)    Temperature sensor (11)    Ammonia furnace (12)    Secondary gas filter tank (14)    Biological bed (15)    Humidifying pipe (16)    Ripe compost layer (17)    Wood (18)    Distributing pipeline (19)
NOVELTY - Preparing fertilizer comprises screening an algae species, breaking the cell wall to release the contents and forming an algae concentrate, controlling the moisture content of pond sludge to 30-40% by sun exposure, mixing the algae, dried sludge and straw cut into 1.5 cm lengths, placing in parallel rows in a field, turning while adding Bacillus subtilis, spraying with 2 kg probitoic liquid formulation for 7 days at 20 degrees C and humidity of 40%, dehydrating, crushing, stacking, adding 0.4 kg humic acid, adding 2 kg phosphate powder, adding 0.3 kg ash, stirring, granulating, drying, cooling and packaging the obtained organic fertilizer.    USE - Method for preparing fertilizer (claimed).    ADVANTAGE - Environmental pollution can be eliminated while reducing river bed height.    DETAILED DESCRIPTION - Preparing fertilizer comprises screening an algae species, breaking the cell wall to release the contents and forming an algae concentrate, controlling the moisture content of pond sludge to 30-40% by sun exposure, mixing the algae, dried sludge and straw cut into 1.5 cm lengths, placing in parallel rows in a field, turning while adding Bacillus subtilis, spraying with 2 kg probitoic liquid formulation for 7 days at 20 degrees C and humidity of 40%, dehydrating, crushing, stacking, adding 0.4 kg humic acid, adding 2 kg phosphate powder, adding 0.3 kg ash, stirring, granulating, drying, cooling and packaging the obtained organic fertilizer.
NOVELTY - Method for detecting Helicobacter pylori (Hp) involves carrying out in vitro diagnosis on concentration of Hp in stomach by taking a wavelength scanned-cavity ring down spectroscopy (WS-CRDS) as a detection technology and taking urea marked by carbon-13 isotope as a tracer agent, and detecting change of carbon dioxide concentration in breathing air of a patient.    USE - The method and device are useful for detecting Hp in breathing air of a patient (all claimed).    ADVANTAGE - The method is accurate, flexible, environmentally-friendly and economical, and suitable for large-scale application.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device useful for detecting Hp.
NOVELTY - The composting method of organic fertilizer involves: (1) pretreating feedstock with degrading bacteria; (2) adding pretreated feedstock to organic fertilizer in aging equipment, spraying fermentation broth and fermenting; (3) aging the material at a temperature of 95-100 degrees C for 2-4 hours and controlling the temperature at 70 degrees C, cooling and stirring for 8 hours; and (4) crushing the material for 8 hours, stacking the crushed material as a heap to a height of 2-3 m with a long wooden stick in piles for 3-6 days and fermenting into stable humus.    USE - Method is useful for composting organic fertilizer (claimed).    ADVANTAGE - The method enables preparation of fertilizer that supplies comprehensive nutrition, has excellent fertilizer efficiency, increases soil organic matter, promotes microorganism breeding, and improves physical and chemical properties and biological activity of soil.
NOVELTY - Refined biogas fermentation feedstock and preparation method of biogas are claimed. The feedstock comprises wheat bran, corncob powder, peanut shell powder, sweet potato powder, limestone powder, crop straw, human waste, biogas slurry and water. The preparation involves crushing and filling crop straw in dry fermenter containing wheat bran, corncob powder, peanut shell powder and sweet potato powder, stirring the mixture with water, adding the contents into a biogas tank, adding remaining raw materials and closing the tank.    USE - Refined biogas fermentation feedstock and preparation method of biogas (claimed).    DETAILED DESCRIPTION - Refined biogas fermentation feedstock and preparation method of biogas are claimed. The feedstock comprises 3-10 pts. wt. wheat bran, 2-10 pts. wt. corncob powder, 2-10 pts. wt. peanut shell powder, 2-10 pts. wt. sweet potato powder, 5-10 pts. wt. limestone powder, 300-800 pts. wt. crop straw, 200-500 pts. wt. human waste, 300-500 pts. wt. biogas slurry and 300-600 pts. wt. water. The preparation involves crushing and filling 1-3 cm crop straw in dry fermenter containing wheat bran, corncob powder, peanut shell powder and sweet potato powder, stirring the mixture with water of 70-100 degrees C for 0.5-1 hour until the mixture turns into paste, adding the contents into a biogas tank, adding remaining water along with human waste and biogas slurry, and closing the tank.
NOVELTY - Performing sewage purification treatment involves discharging pig manure and sewage into a tank, and then subjecting the obtained mixture into a fermenter for 15 days to a month to obtain biogas solution, which is used as fuel for electricity generation. The resulting biogas solution, is then discharged to an artificial farmland, lake or reservoir for planting rice or vegetables such as lettuce, spinach, water chestnut or taro, and for breeding of aquatic fish such as grass carp, carp and herring, fish or turtles.    USE - Method for performing sewage purification treatment for planting vegetable (claimed).    ADVANTAGE - The method enables to perform sewage purification treatment by effectively eliminating any chemical fertilizers and pesticides, and also reducing total nitrogen content by 40-75%, total phosphorus content by 30-60%, sodium content by 8-12%, and potassium content by 30-40%. The purified sewage is then introduced to the lakes, rivers and ponds for growing vegetables.    DETAILED DESCRIPTION - Performing sewage purification treatment involves discharging pig manure and sewage into a tank, and then subjecting the obtained mixture into a fermenter for 15 days to a month to obtain biogas solution, which is used as fuel for electricity generation. The resulting biogas solution, is then discharged to an artificial farmland, lake or reservoir for planting rice or vegetables such as lettuce, spinach, water chestnut or taro, and for breeding of aquatic fish such as grass carp, carp and herring, fish or turtles. The obtained biogas solution is dried, and then mixed with clay to grow vegetable on the growth substrate.
NOVELTY - The equipment has rotary sieves that are connected to a mobile tank. A conveyor pipe separator is arranged inside of a rotary drum. A biodigester for biogas performs the combustion of the biogas, where the rate of rotation and increment of temperature is adjustable and the hot gases of pyrolysis are produced in processed cyclone and distiller condensers. A catalyst is exhausted for the security of air.    USE - Equipment for separating and converting solid phase of effluents for conditioning the fertilizer of soil.    ADVANTAGE - The biodigester for biogas performs the combustion of the biogas, where the rate of rotation and increment of temperature is adjustable and the hot gases of pyrolysis are produced in processed cyclone and distiller condensers, and thus enables to recover the degraded areas in urban gardening.
NOVELTY - Preparation of bacterial cellulose using bean curd yellow slurry water involves selecting bean curd yellow slurry water as raw liquid and then centrifuging at 5000 rpm for 10 minutes, adding solid culture medium comprising glucose, yeast leaching powder, agar and distilled water to the raw liquid, adjusting pH value to 4.5 and then sterilizing at 121 degrees C for 15 minutes, adding liquid culture medium comprising glucose, yeast leaching powder and distilled water to the mixture and then sterilizing, adding glucose to the mixture and fermenting, and adjusting pH value to 5.    USE - The method is useful for preparation of bacterial cellulose using bean curd yellow slurry water (claimed).    ADVANTAGE - The method enables simple and economical preparation of bacterial cellulose with high yield of 1.40 g/100 ml and excellent glucose utilization rate of 97.5% in an environmentally-friendly manner.    DETAILED DESCRIPTION - Preparation of bacterial cellulose using bean curd yellow slurry water involves selecting bean curd yellow slurry water as raw liquid and then centrifuging at 5000 rpm for 10 minutes, removing impurities and then purifying, adding solid culture medium comprising 40 g glucose, 10 g yeast leaching powder, 15 g agar and 1 l distilled water to the raw liquid, uniformly mixing, adjusting pH value to 4.5 and then sterilizing at 121 degrees C for 15 minutes, adding liquid culture medium comprising 40 g glucose, 10 g yeast leaching powder and 1 l distilled water to the mixture and then adjusting pH value to 4.5, sterilizing the mixture at 121 degrees C for 15 minutes and then fermenting, sterilizing the mixture at 121 degrees C for 15 minutes, adding 8% glucose to the mixture with an inoculum size of 6% and then fermenting at 30 degrees C for 7 minutes, and adjusting pH value to 5.
NOVELTY - Bamboo tube fuel (1) is formed by filling inner side of bamboo tube (10) with biomass (12) of grass and tree.    USE - Bamboo tube fuel used as alternative fuel of firewood.    ADVANTAGE - Bamboo tube fuel can be easily manufactured at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for manufacturing bamboo tube fuel which comprises hopper area for injecting biomass of grass and tree, stirring part for installing in hopper area and for stirring biomass of grass and tree, fuel filling part which is equipped with guide pipe provided with spiral screw for connecting with hopper area and conveying biomass of grass and tree from hopper area, and control part for controlling motive power of stirring part and spiral screw.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional diagram of the bamboo tube fuel.    Bamboo tube fuel (1)    Bamboo tube (10)    Biomass of grass and tree (12)    Opening part (14)    Stopper (16)
NOVELTY - The apparatus (15) has power supply (5) for self-supporting starting which supplies electric power to material supply device (2) and combustion-air supply device (4). An electric power supply is carried out to the auxiliary machine containing material supply device and combustion-air supply device. The electric power supply is carried out to auxiliary machine only from the power supply for self-supporting starting. A controller (6) is provided so that first heating amount became larger than second heating amount burns with combustor (3) during normal starting.    USE - Hydrogen generating apparatus of fuel cell system (claimed) used for domestic purpose.    ADVANTAGE - The temperature of a catalyst is heated up at an early stage, and starting time is shortened, when starting by the electric power supply from the power supply for self-supporting starting. Thus, the electric energy consumed by an auxiliary machine is reduced, and the power supply for self-supporting starting is reduced in size.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a fuel cell system; and    (2) a method for operating hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus.(Drawing includes non-English language text)    Material supply device (2)    Combustor (3)    Combustion-air supply device (4)    Power supply for self-supporting starting (5)    Controller (6)    Hydrogen generating apparatus (15)
NOVELTY - Method for controlling fume in organic waste process by fermentation using microorganisms, involves heating organic waste by supplying 200 degrees C or less air to tank from upper direction, discharging from discharge port provided in other upper direction, heat-drying the organic waste in stirring state, and controlling absolute humidity of air to 80 g/kgDA or more when temperature of air inside the tank is 60-80 degrees C.    USE - The method is used for controlling fume in organic waste process by fermentation using microorganisms (claimed).
NOVELTY - A composite membrane comprises greater than or equal to 1 dense polymeric membrane having permeability for 1st gas of greater than or equal to 7.5x 10-11cm3/cm2.s.kPa and greater than or equal to 1 layer of perforated two-dimensional material in which composite membrane is arranged to provide preferential transport of 1st gas relative to 2nd gas through dense polymer membrane and layer of perforated two-dimensional material.    USE - A composite membrane for separation of 1st gas from 2nd gas (claimed).    ADVANTAGE - Gas separation process is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a separation of 1st gas from 2nd gas which involves providing composite membrane, and contacting external surface of composite membrane with 1st gas and 2nd gas in which composite membrane provides preferential transport of 1st gas relative to 2nd gas through greater than or equal to 1 dense polymer membrane and greater than or equal to 1 layer of perforated two-dimensional material.
NOVELTY - Device comprises an apparatus disposed in these regions for generating solar energy and/or wind turbines and water electrolysis systems for generating hydrogen, and double pipes or double pipelines are arranged for hydrogen transport and outward transportation of water from water sources used for water electrolysis.    USE - The device is useful for power-to-gas technology in desert regions or other little populated or agriculturally unused regions (claimed).    ADVANTAGE - The device: reduces the cost of necessary transport capacities, thus it is cost efficient; and provides protection against electromagnetic pulses, and thus it has increased safety.
NOVELTY - A conversion of biomass-based char into water-soluble products involves subjecting biomass-based char to an oxidant to provide a mixture, and converting the biomass-based char of the mixture into water-soluble products.    USE - Conversion of biomass-based char into water-soluble products e.g. levulinic acid, acetic acid, succinic acid and/or formic acid (claimed) used for producing resins, plasticizers, specialty chemicals, herbicides and as flavor substance. Levulinic acid is useful as solvent, and as starting material in preparation of variety of industrial and pharmaceutical compounds such as diphenolic acid, and calcium levulinate.    ADVANTAGE - The method to convert biomass-based char into water-soluble products is flexible and increases yield.
NOVELTY - The method involves removing hot pressed transfer film which contains catalyst layer containing a platinum-based catalyst. The catalyst layer is transferred on the transfer film. A catalyst solution is coated at the upper part of the catalyst layer of the transmitted film in which the catalyst layer is transferred to form another catalyst layer containing the platinum-based catalyst.    USE - Method for manufacturing a film (Claimed) for fuel cell-electrode assembly.    ADVANTAGE - The method involves removing hot pressed transfer film which contains catalyst layer containing a platinum-based catalyst, where the catalyst layer is transferred on the transfer film, and hence ensures an improved fuel cell-electrode assembly film manufacturing method that increases the economical efficiency and durability of the film.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation of current-voltage performance of membrane electrode assembly.
NOVELTY - The new type utility claims have one kind novel biological fuel granulator, make up of main box, a large belt wheel, a chassis, a cutter, a main shaft, a compression roller, hopper for, a drive plate, mould, bearing, motor and small belt wheel, and the right side upper part set with motor case, motor provided with upper small belt wheel, in case left side set with bearing, upper bearing set with large belt wheel, the bearing, the main shaft top end in inner upper case set with left box, a material box set with main shaft, main shaft connected with machine box set with plate, lower plate main shaft double side provided with compression roller, compression roller set with die, lower die set with cutter. The utility model is new type for construction of traditional horizontal granulating machine designed as a vertical structure, reducing have small square meter, increase have pelletizing effect, increase production efficiency, is convenient to change, suitable maintenance, reducing have production cost, the granulator with scientific design, small square meter small, pelletizing effect is good, the spiral blade and a long service life.
NOVELTY - A nano-polycrystalline silicoaluminophosphate (SAPO) molecular sieve comprises CHA-structure type (SAPO-34) molecular sieve, RHO-structure type (SAPO-RHO) molecular sieve or eutectic molecular sieve, and has crystal size of less than 100 nm and polycrystalline aggregate size of 1.5-2.5 microns, pore volume of 0.14-0.17 ml/g and specific surface area of 650-730 m2/g.    USE - The nano-polycrystalline silicoaluminophosphate (SAPO) molecular sieve is useful as catalyst for dehydration of methanol to lower olefins and adsorbent for adsorbing and separating small molecules from gas (claimed).    ADVANTAGE - The nano-polycrystalline silicoaluminophosphate (SAPO) molecular sieve has large specific surface area.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing nano-polycrystalline silicoaluminophosphate (SAPO) molecular sieve.
NOVELTY - The new type utility claims have one kind of biomass gasification furnace, comprising a furnace body, a feedstock device and gas treatment device, in the furnace body and lower part is set with grate, furnace grate for the furnace body internal is divided into the following two at one part, the upper part is reaction room, in the lower part is collected sum room, the biomass raw material reaction room, collected sum room lower end for collecting hopper, collected sum room upper part connected with the air outlet pipe, feedstock right side device and the furnace body of the upper part left side set with feedstock device, connected with the furnace feedstock and wherein, in said feedstock device provided with heat load sum and mixing room inlet and cone shape, the heat load sum air inlet pipe comprises heat load sum inlet end and heat load sum air inlet pipe. The utility model is new type equipped with the feedstock device can make high temperature catalyst and biomass raw material full mixing, further increase have catalytic effect of catalyst, the gas treatment device can be formed for gas from gasification furnace and from the cooling process, and the gas for processing waste liquid and separating the dust.
NOVELTY - The new type utility claims have one kind methanol gasoline continuous production device, belonging to methanol gasoline manufacture technology field. The device comprises preparation device and preparation device of methanol gasoline double part of modified methyl alcohol. The modified methanol in the preparation device, modified methyl alcohol reaction kettle in turn connected with feeding pump I and I the feedstock wherein cyclone, discharging mouth and swirl nozzle (I) by pipeline connected with the modified methanol storing kettle, in device of methanol gasoline in the gasoline reaction kettle and modified methyl alcohol storage kettle respectively connected with methanol gasoline reaction kettle, methanol gasoline reaction kettle in turn connected with the feeding pump II and feedstock and wherein the nozzle II, a discharging mouth of nozzle II through pipe connected with the methanol gasoline storage kettle. The utility model is new type by two segment closed-circuit circulation device, the impurity of methanol gasoline production process by the condenser can be separated out, at last to obtain the product is qualified and methanol gasoline, can make methanol gasoline production process continuously.
NOVELTY - Extracted oil from laurel seeds which can be used in producing biodiesel according to the standard SNI 04-7182-2006.    USE - The extracted oil from laurel seeds is useful in producing biodiesel used in producing automobile fuel (claimed).    ADVANTAGE - The extracted oil can be efficiently used in producing biodiesel which can be used in automotive purely 100% without any mixture of other diesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process of making biodiesel from oil laurel with esterification- transesterification process for use in producing good automotive fuel, which involves: (a) degumming process: addition of phosphoric acid in an amount of 0.5% (w/w), reaction is carried out at 60 degrees C for 30 minutes; furthermore, oil degumming results in separating impurities by settling the dirt on the bottom of the oil; (b) esterification: reacting the oil with methanol, where methanol is added according to the ratio of 20:1 according to free fatty acid (FFA) content, the catalyst used in this process is 1% (w / w) hydrochloride (HC1) or using zeolite in an amount of 3% (w/w), and where the process is carried out at 60 degrees C for 1 hour, and further washing using warm distilled water and weak alkaline solution of 0.01% sodium bicarbonate (NaHCO3), washing with water until pH is neutral; (c) transesterification: reacting the oil with esterified methanol having an amount in a ratio of 6:1 in relation to oil and esterification which is aided using sodium hydroxide (NaOH) catalyst in an amount of 0.5% (w/w), the reaction is conducted at a temperature of 60 degrees C for 0.5 hour, at this stage the obtained methyl esters (biodiesel) are still mixed with the residual methanol, glycerol and residual catalyst; thus, to obtain pure biodiesel, further washing and purification process is executed.
NOVELTY - Catalytic method for processing natural gasoline comprising more than five carbon comprises continuous process of natural gasoline comprising more than five carbon in a fixed bed reactor at 350-550 degrees C and at an atmospheric pressure using nitrogen as a carrier gas in the gas-solid phase.    USE - The catalytic method is useful for processing natural gasoline comprising more than five carbon which is useful in hydrocarbon cracking processes, where the hydrocarbon is more than five carbon preferably a mixture of pentane, 2-methyl-butane and hexane (all claimed).
NOVELTY - A catalyst comprises a support, and a transition metal which shows a catalytic activity, supported by the support. The support is two-dimensional electride or its precursor.    USE - Catalyst is used in synthesis of ammonia (claimed).    ADVANTAGE - The catalyst has high catalytic activity and excellent chemical stability and thermal stability. Ammonia can be efficiently synthesized using the catalyst by economical and simple process with reduced energy consumption.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of catalyst, which involves supporting the transition metal using a compound powder comprising support by impregnation method, physical mixing method, thermal decomposition method, liquid-phase process or vapor deposition method; and    (2) synthesis of ammonia, which involves reacting nitrogen and hydrogen at 100-600 degrees C under pressure of 10-20 MPa in presence of catalyst within ammonia synthesis reaction apparatus reaction.
NOVELTY - Waste fermentation treatment system comprises roller (101), air duct (102), feeding device (103), fan (104), discharging groove (105), bearing bracket device (106), base (107), driving device (108), water outlet, inlet, first door, outlet, air pipe connecting frame, bearings, support rods, feed hopper, feeding pipe, brackets, connecting motor, driving gear, passive gear ring, hopper, auger, connecting shaft, cutter drive motor, crushing gear, discharge ports and cylinder body.    USE - Waste fermentation treatment system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic structure diagram of waste fermentation treatment system.    Roller (101)    Air duct (102)    Feeding device (103)    Fan (104)    Discharging groove (105)    Bearing bracket device (106)    Base (107)    Driving device (108)
NOVELTY - The utility model claims a propulsion stirring relux anaerobic fermentation tank, fermentation device belonging to the field of the propulsion stirring relux Anaerobic fermentation tank comprises tank body, driving device, spray device, relux device, stirring device, an exhaust port, using mechanical stirring is paddle stirring leaves forming the radial force, with strong cutting effect, large particle diameter of solid object and dispersing a liquid full mixing, which avoids material generate crusting; biogas extraction tank bottom tube and tank body to force the liquid product flow of internal circle direction following extraction function and a screw pump, forming liquid circulation stirring, using push-type stirring leaf form axial force cutting effect is small, which avoids the damage to methane fungus have mechanical and biogas slurry and stirring paddle stirring leaf extract pipe extraction liquid form the liquid relux stirring effect together, forming full mixing stirring, increase have stirring effect, reducing stirring consume active power, the utility model is new type structure is simple, suitable operation, which is good for popularization.
NOVELTY - The utility model claims a relux mixture, push type stirring and filtering Anaerobic fermentation tank , belonging to fermentation equipment field, said device comprises tank body, driving device, stirring device, a screw pump, a filter device, a relux device, the utility model is new type using a fermentation tank internal equipped with paddle stirring leaf, using the product with strong cutting action of the radial force, and a dispersing of biogas straw raw material is full mix, which avoids material generate crusting; use push-type stirring leaf form axial force cutting effect is small, which avoids the damage to methane fungus, using screw pump using biogas slurry circulation tank body of internal flow, forming liquid stirring, machine stirring and liquid stirring using a common function, increase have stirring effect, using for the reaction is more complete, reduce stirring consume active power, equipped with a discharging port, a can of the biogas and slag discharge in fermentation tank, increase efficiency of fermentation, filter device can save the fermentation raw material, further reducing cost.
NOVELTY - The utility model claims a municipal domestic garbage sorting organic matter water high speed fermentation device, comprising, water power sorting device, a sorting device, sewage purification device, crushing dispensing device, pressure hydro-thermal treatment equipment, methane fermentation device and fermentation residue pool and a biological tank; the garbage chamber one end set with garbage entering into mouth, the garbage chamber another one end connection and then the water power sorting device on a one channel process, water power sorting device another one end respectively and then sorting device, sewage purification device and dispensing device connected crushing, the crushing device and respectively adjusting a pressure hydro-thermal processing device and sewage purification device connected, said pressure hydro-thermal processing device another terminal connected with methane fermentation equipment, methane fermentation device respectively connected and a biological tank and fermentation residue pool. With automatic degree high, working personnel, using suitable, reducing production cost, energy saving environment-friendly equal.
NOVELTY - The utility model claims a relux mixture and propulsion stirring anaerobic fermentation tank , belonging to the field of fermentation equipment; the relux mixture and propulsion stirring Anaerobic fermentation tank using mechanical stirring is a paddle stirring leaves forming the radial force, with strong cutting effect, large particle diameter of solid object and dispersing additive and liquid full mixing, which avoids material crust, and biogas tank body bottom in extraction under effect of screw pump, wherein the tank body internal circulation flow, forming liquid stirring, push type stirring leaf form axial force cutting effect small, which avoids the damage to methane fungus, circulation flow of machine stirring and liquid extract pipe, biogas liquid to common effect, full mixing stirring, increase stirring effect, reducing stirring consume active power, the tank body set with longer diameter than large, which is good for further reducing stirring consume power, using stirring more uniform additive tank in storage by the precise metering pump added with fermentation tank, used for regulating material composed of, increase fermentation effect.
NOVELTY - Straw feed is prepared by selecting crop straw, passing crop straw through pulverizer and cutting to specific length. The water content in the crop straw is controlled to 60-70% during the drying process. The cut straw is fermented using microorganisms in a storage cellar for 9-16 days, and finally packaged using nylon bag. Also claimed is the preparation of the straw feed.    USE - Straw feed for livestock and poultry.    ADVANTAGE - The degradation of straw cellulose using microbial fermentation fully converts the nutrients in the straw for livestock feed absorption, and improves the utilization of crop straw.
NOVELTY - Preparing composite solid fuel biomass involves preprocessing crop straw, wood and forestry waste shoulder containing wood cellulose biomass raw material and then removing impurities from the preprocessed material. The preprocessed biomass raw material is crushed and then the crushed material is subjected to hydro-thermal treatment to obtain modified biomass solid product and liquid product. The obtained product is added with heat improving agent, dried, pulverized and mixed to reduced water content to 12-18%.    USE - Method for preparing composite solid fuel biomass (claimed).    ADVANTAGE - The method enables to prepare composite solid fuel biomass in simple, energy-saving and cost-effective manner.
NOVELTY - Fuel composition comprises 23-40 wt.% biomass alcohol, 30-46 wt.% rapeseed straw powder, 19-26 wt.% green vine straw stick powder, 10-15 wt.% wheat straw powder, 20-30 wt.% sunflower straw powder, 35-45 wt.% castor straw stick, 16-25 wt.% rice hull powder, 30-45 wt.% peat grass, 40-65 wt.% fly ash, 55-60 wt.% mulberry branch, 6-13 wt.% pine oil and 7-10 wt.% dry pine branch.    USE - Fuel composition used in chemical plants, fertilizer plants, breweries, pharmaceutical factory and sugar factory.    ADVANTAGE - The fuel composition is safe and cost-effective, and replaces diesel or heavy oil used in the collective canteens, restaurants, hotels, stove and boiler.
NOVELTY - Decoloring catering waste biodiesel oil involves adding crude waste biodiesel oil in decoloring vessel and then illuminating the obtained material at room temperature for 6-16 hours for decoloring. The decolored material is observed to compare the color with good decolor biodiesel oil. The illumination is stopped after observing qualified product and then the qualified product is transported to storage tank.    USE - Method for decoloring catering waste biodiesel oil (claimed). .    ADVANTAGE - The method enables to decolor catering waste biodiesel oil in cost-effective and energy-saving manner and without solid waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for decoloring catering waste biodiesel oil, which comprises a vessel body, a vessel cover, an ultraviolet lamp, an ultraviolet lamp tube, the ultraviolet working indicator lamp, valve and pipe, and vessel cover is on the vessel body through a bolt.
NOVELTY - The system has a wind and solar heat generating unit (10), biogas generating unit (20), a slurry heating unit (30), and power storage unit (40). The wind and solar heat generating unit is connected with power storage unit and slurry heating unit which is connected with biogas generating unit. The biogas generating unit is connected with greenhouse (50). The human and animal excreta are transmitted as raw material to biogas generating unit, and then the biogas residue and liquid of biogas generating unit are conveyed to the greenhouse for utilization of energy.    USE - Biogas, wind energy, solar energy integrated eco-cycle system for greenhouse.    ADVANTAGE - The quality of life of pastoral herders is improved, and the grassland and forest ecological environment in pasturing area is protected effectively. The air pollution emission is reduced, and the continual use of energy is ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biogas, wind energy, solar energy integrated eco-cycle system. (Drawing includes non-English language text)    Wind and solar heat generating unit (10)    Biogas generating unit (20)    Slurry heating unit (30)    Power storage unit (40)    Greenhouse (50)
NOVELTY - An eco-friendly carpet deodorant preparing method involves inoculating composite strain such as inoculating composite strain composed of Saccharomyces cerevisiae, Lactobacillus, Streptococcus and Rhodopseudomonas palustris in culture medium to carry out culturing for 48 hours to obtain microbial inoculum raw liquid, sterilizing a molasses at 110 degrees C, sterilizing a vitamin solution at 121 degrees C, followed by stirring microbial inoculum raw liquid, molasses, vitamin solution and rest water in a tank to carry out fermentation process to obtain deodorant.    USE - Method for preparing eco-friendly carpet deodorant.    DETAILED DESCRIPTION - An eco-friendly carpet deodorant preparing method involves inoculating composite strain such as inoculating composite strain composed of 25-30 wt.% Saccharomyces cerevisiae, 20-30 wt.% Lactobacillus, 20-30 wt.% Streptococcus and 10-20 wt.% Rhodopseudomonas palustris in culture medium to carry out culturing at 30 degrees C for 48 hours to obtain microbial inoculum raw liquid, sterilizing a molasses at 110 degrees C for 20 minutes, sterilizing a vitamin solution at 121 degrees C for 20 minutes, followed by stirring microbial inoculum raw liquid, molasses, vitamin solution and rest water in a fermentation tank to carry out fermentation process at 30 degrees C for 15 days to obtain deodorant, where the culture medium comprises 0.3 wt.% peptone, 0.8 wt.% maltose, 1 wt.% glucose, 0.1 wt.% sodium dihydrogen phosphate, 0.08 wt.% preservative, 0.1 wt.% stablizing agent and rest water to pH value of 6.8.
NOVELTY - Organic fertilizer processing device comprises fermentation tank, belt transport machine, raw material sieving and stirring mechanism, spiral transport machine and weighing mechanism, where fermentation tank entrance and material separation machine are connected to fermentation tank outlet that is set with belt transport mechanism. The belt transport mechanism comprises pit (A1) that is provided with transport frame (A2). The transport frame is fixed with bottom leg (A3). The transport frame is fixed with shaft (A4) that is mounted with strip transport roller (A5).    USE - Organic fertilizer processing device.    ADVANTAGE - The organic fertilizer processing device is simple, and has high automatic degree and good effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a organic fertilizer processing device.    Pit (A1)    Transport frame (A2)    Bottom leg (A3)    Shaft (A4)    Transport roller (A5)
NOVELTY - High-performance diesel methanol comprises 55-75 wt.% diesel oil, 10-30 wt.% methanol and 5-15 wt.% additive.    USE - The method is useful for preparing high-performance diesel methanol (claimed).    ADVANTAGE - The diesel methanol: has good stability; is economical; exhibits good lipophilicity and water resistance; has physical and chemical indicators that reach the indicators of vehicle diesel. The method is easy to operate; and carried out under low temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the high-performance diesel methanol, comprising at room temperature and atmospheric pressure, adding additive, methanol and diesel oil into the reaction tank and uniformly mixing.
NOVELTY - The new type utility claims have one plant fertilizer fermentation device, comprising: tube, mounted on the bracket on the tube top part is set with feeding opening and a cylindrical cavity body, cylinder body mounting bottom has cone funnel, the funnel cone bottom is provided with a discharging mouth, the cylinder wall of the tube for inner layer and double-layer structure comprises the outside layer, double layer between is connected one the cavity, the outside upper layer side and lower side respectively set with one water out mouth and one water inlet, stirring device, ventilation device. The utility model is new type can for fertilizer for large stirring range, effective to prevent compost temperature over-high to avoid the high temperature bacteria cause death, and using sum flow distribution plate to tube in the air, the fertilizer can make more effective the large square meter contact air so as to further promote the fermented fertilizer, also can use fertilizer fermentation process of producing heat to water for heating, has heat preservation function or the circulating cooling water to control temperature function, increase fertilizer fermentation efficiency, with good practical value.
NOVELTY - The utility model is new type relates to one plant three-dimensional planting structure, especially one kind of building and is suitable for family kitchen is to solve three-dimensional planting structure. A plant solves building three-dimensional planting structure, the three-dimensional planting structure of family kitchen set at outside of building up terrace, comprising poultry breeding area, vigetable, flower and fruit planting area, fertilizer fermentation area and storage pool area, terrace upper set with bracket, three-dimensional planting structure is set on bracket, the poultry breeding area used for feeding poultry, fertilizer fermentation area for taking excrement fermentation of poultry. The utility model is new type and limited technology, comprises following advantages: 1, the structure is simple. 2, have family kitchen using, at the same time also beautify have environment.
NOVELTY - Coal-based natural gas catalyst comprises 10-35 wt.% active substance nickel oxide, 20-47 wt.% carrier aluminum oxide, 8-40 wt.% auxiliary agent, 15-30 wt.% adhesive, 3-6 wt.% graphite, and 8-13 wt.% water. The auxiliary agent is lanthanum oxide, manganese oxide or zirconium oxide.    USE - Used as coal-based natural gas catalyst.    ADVANTAGE - The catalyst has high strength, good activity, thermal stability, anti-carbon function, and high temperature resistance performance, is prepared by simple and economical method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing coal-based natural gas catalyst comprising (i) taking 50.8-83.15 g/l aluminum trinitrate nonahydrate, 15.43-39.62 g/l nickel nitrate hexahydrate, and 14.52-25.64 g/l auxiliary agent, mixing to obtain mixture, heating mixture to 50-70 degrees C, adding into constant-temperature tank I, (ii) taking 8-12% potassium carbonate, heating to 50-70 degrees C, and loading in constant temperature tank II, (iii) adding constant temperature tank I and II reaction liquid in centrifugal reactor, controlling relative flow speed in reactor and pH at 7-8.5, where the reaction time is 20-30 minutes, (iv) taking step (iii) reaction liquid and filtering to obtain precipitate, aging for 8-24 hours, washing filtering again to obtain catalyst product, (v) taking semi-finished product catalyst, drying at 80-120 degrees C for 4-12 hours, and (vi) drying the catalyst semi-finished product, sintering for 5-6 hours at low temperature in a muffle furnace at 480-550 degrees C, after sintering the material, grinding, sieving, adding 15-30% adhesive, 3-6% graphite, and 8-13% water, mixing uniformly and pressing to obtain the product.
NOVELTY - Treatment of acidic metal sulfate industrial wastewater with sulfate-reducing bacteria by taking soybean meal or corn germ meal, placing into closed vessel, naturally fermenting, adding domestic sewage, grinding, adding acidic metal sulfate wastewater, mixing, measuring sulfate concentration, metal ion content and pH, placing into anaerobic moving bed reactor, water circulating, placing into anaerobic moving bed reactor, sedimenting metal sulfide, reducing sulfate ion concentration, and neutralizing water.    USE - Method for treating acidic metal sulfate industrial wastewater with sulfate-reducing bacteria (claimed).    ADVANTAGE - The method uses domestic sewage with wide source and rich in nitrogen, sulfur and phosphorus, solves sulfate-reducing bacteria application condition requirement and processing cost and high problems, and provides convenient sulfate wastewater and metal recovery condition. It ensures enterprise normal operation, saves cost, and increases enterprise benefit.    DETAILED DESCRIPTION - Treatment of acidic metal sulfate industrial wastewater with sulfate-reducing bacteria by taking soybean meal or corn germ meal, placing into closed vessel, naturally fermenting for 3-5 days, taking at solid-liquid ratio of 1:20-1:40, adding domestic sewage, grinding through 180 mesh, adding acidic metal sulfate wastewater, mixing, measuring sulfate concentration, metal ion content and pH, placing into anaerobic moving bed reactor at flow speed of 0.2-0.5 L/hour, water circulating, placing into anaerobic moving bed reactor at flow speed to 0.2-0.5 L/hour, sedimenting metal sulfide, reducing sulfate ion concentration to 500 mg/L, and neutralizing water.
NOVELTY - Boiler biomass fuel, comprises 1000 pts. corn, 800 pts. wooden meal, 600 pts. cotton straw, 500 pts. charcoal and 30 pts. paraffin.    USE - Used as boiler biomass fuel.    ADVANTAGE - The biomass fuel is economical, simple to manufacture, saves energy, and increases industrial income.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the boiler biomass fuel, comprising cutting corn cob and cotton straw to length of 2-3 cm, air-drying; adding wooden meal, charcoal and paraffin into heating vessel, heating to 25-35 degrees C for 30-40 minutes; and finally adding the corn cob and cotton straw, and stirring.
NOVELTY - The utility model is new type supply have one plant for production biological organic fertilizer of fungus liquid bacteria adding device, the device comprises bacteria adding device and fungus material mixing device, the device comprises bacteria adding liquid fungus jar and pressure jar, the fungus material mixing device comprises roller, the bacteria outlet mouth through bacteria adding pipe and the connected expansion cylinder, the expansion cylinder of the second rotary driving mechanism driving movement, on the inner wall of the roller set with atomizer of liquid fungi, using the fungus liquid tank of the lower part set with clean mouth, the upper pipe set with bacteria adding add material pump and the first valve, connected with pipeline clean up in bacteria adding pipeline between the pump and the first valve add material, the clean pipeline and water tank connected, on the clean pipe set with the second valve. Using the utility new type can make probiotic coenobium uniformly and spray up in organic fertilizer, probiotic coenobium organic fertilizer and can be full mixed in on roller, production out of biological fungus organic fertilizer quality is good, the production efficiency high.
NOVELTY - Feed comprises 60-80 pts. wt. wheat, 10-20 pts. wt. soybean meal, 0-3 pts. wt. imported fish meal, 0-3 pts. wt. lipid, 2-4 pts. wt. premix, 0.3-0.1 pt. wt. plant extract sediment and 0.01-0.02 pt. wt. wheat-based special enzyme.    USE - The feed is useful for improving gastrointestinal function and promoting digestion in pig.    ADVANTAGE - The feed is environment-friendly and promotes development of animal husbandry.
NOVELTY - Mouthwash comprises 0.5-1 vol.% lemon juice, 1-5 vol.% tomato juice, 0.1-0.5 vol.% vitamin C, 8-15 vol.% vinegar and 5-14 vol.% traditional Chinese medicine extracting liquid; the traditional Chinese medicine extracting liquid comprises 15-30 pts. bamboo leaves, 1-10 pts. Oldenlandia diffusa, 5-12 pts. radix ampelopsis, 3-10 pts. dyers woad, 8-17 pts. boat-fruited sterculia, 5-15 pts. Juncus effuses, 10-20 pts. rose, 1-8 pts. garlic, 5-12 pts. cottonrose hibiscus leaf, and 7-15 pts. mulberry leaves.    USE - The mouthwash is useful for treating oral ulcer and inflammation (claimed), relieving pain, and cleaning oral cavity.    ADVANTAGE - The mouthwash is green and environment-friendly, and has low production cost.
NOVELTY - Fertilizer comprises organic fertilizer (40-50 pts. wt.), inorganic fertilizer (2.3-5.7 pts. wt.), sodium chloride (0.5-1.5 pts. wt.), microbial inoculum (0.3-0.7 pts. wt.), and mushroom residue (5-10 pts. wt.).    USE - Fertilizer used for areca nut (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) mixing organic fertilizer, sodium chloride, microbial inoculum and mushroom residue with warm water;    (B) retting obntained mixture; and    (C) adding potassium chloride, urea and magnesium sulfate to obtained mixture to obtain the final product.
NOVELTY - Medicinal balance fertilization comprises 1.0-3.0% Trichoderma powder, 1.0-2.5% fungus particle agent, 1.0-1.5% Paecilomyces lilacinus powder, 3.0-5.0% radix stemonae extract, 25.0-35.0% urea, 15.0-25.0% potassium sulfate, 5.0-15.0% calciumsuperphosphate, 0.1-0.3% ferrous sulfate, 0.3-0.5% copper sulfate, 0.3-0.4% magnesium sulfate, 0.3-0.45% zinc sulfate, 5.0-8.0% water retention agent, 5.0-10.0% straw powder, 5.0-10.0% dairy manure and 5.0-8.0% rice bran.    USE - Medicinal balance fertilization used for plant cropping (claimed).    ADVANTAGE - The medicinal balance fertilization is suitable for variety of plants, maintains sustainable use of soil, and prevents root disease.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing medicinal balance fertilization, which involves:    (A) crushing components through 50 items sieve into powder by using ultra-micro pulverizer; and    (B) crushing the powder through 100-200 items sieve, and then mixing to obtain final product.
NOVELTY - The system has air inlet pipe (8) that is connected with marsh gas pump (1) and air outlet pipe that is connected with aeration pipe (9) which is set with stop valve (17). A gas storage pipe (10) is connected with emptying pipe (11) and set with stop valve (18). A liquid drain pipe (14) is connected with water liquid slot (4) and connected with discharging liquid tank (13) through water sealing cylinder.    USE - Floor film cover dry anaerobic compost fermentation system for agricultural organic solid waste.    ADVANTAGE - The simple operation, sealing safety, reliability, good air permeability, high production rate, and strong harmless processing ability of fermentation system are ensured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a using method of floor film cover dry anaerobic compost fermentation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the floor film cover dry anaerobic compost fermentation system.    Marsh gas pump (1)    Water liquid slot (4)    Air inlet pipe (8)    Aeration pipe (9)    Gas storage pipe (10)    Emptying pipe (11)    Discharging liquid tank (13)    Liquid drain pipe (14)    Stop valves (17,18)
NOVELTY - Biodiesel for preparation of biodegradable anti-rust oil, is claimed.    USE - Biodiesel is used for preparation of biodegradable anti-rust oil (claimed).    ADVANTAGE - The biodegradable anti-rust oil formed using the biodiesel has excellent workability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biodegradable anti-rust oil, which involves pumping 20-30 pts. wt. mineral oil and 40-50 pts. wt. biodiesel into vacuum reactor, to obtain base oil, heating base oil at 75 degrees C, pumping additives comprising 0.01-0.05 pt. wt. methyl silicone oil, 0.01-0.05 pt. wt. benzotriazole, 0.48-0.1 pt. wt. 2,6-di-tert-butyl-p-cresol, 2-5 pts. wt. zinc naphthenate, 2-5 pts. wt. alkenyl succinate, 2-5 pts. wt. sorbitan monooleate, 4-8 pts. wt. barium oxide soap stone oil, 5-10 pts. wt. barium dinonylnaphthalene sulfonate, 5-10 pts. wt. barium petroleum sulfonate and 2-5 pts. wt. D-octyl zinc parathion into base oil with circulation pump, stirring, heating mixture at 75 degrees C, maintaining vacuum at -0.096 MPa with open vacuum pump and reacting for 0.5-2 hours.
NOVELTY - Microalgae biodiesel extraction technology comprises large-scale cultivating microalgae in lake and pond; ethanol-hexane co-solvent extraction of high water content algae mud for extracting algae oil; and carrying out transesterification reaction for converting algae oil into biodiesel.    USE - Microalgae biodiesel extraction technology (claimed).
NOVELTY - Preparation of microorganism additive comprises adding Frankia into flask, shake culturing, seed culturing, and collecting Frankia fermentation liquid; adding Bacillus thuringiensis into flask, shake culturing, seed culturing, and collecting Bacillus thuringiensis fermentation liquid; and taking 20-30 wt.% Frankia fermentation liquid, 30-40 wt.% Bacillus thuringiensis fermentation liquid, 1-10 wt.% photosynthetic bacteria, 1-10 wt.% Bacillus mucilaginosus solution, 1-5 wt.% trace element and balance chicken manure and mixing.    USE - Method for preparing microorganism additive used for cultivating strawberry (claimed).    ADVANTAGE - The microorganism additive increases strawberry yield.
NOVELTY - Fertilizer comprises main components comprising potato seedlings and soybean straw fermentation product, and plant ash, potassium sulfate, potash and monoammonium phosphate, in a mass ratio of 40:22:15:8:2.5.    USE - The fertilizer is useful for potatoes (claimed).    ADVANTAGE - The fertilizer has high fertilization effect; can effectively promote the growth of potatoes; not only can achieve recovering of straw, but also can promote soil conditioning effect; enhances soil fertility; is economical; and facilitates rapid absorption of nutrients into the soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing fertilizer, comprising subjecting potato seedlings and soybean straw fermentation product to air-drying process, crushing, and then adding the remaining raw materials, reacting for 2-3 days under closed environmental conditions under room temperature conditions of less than 8-12 degrees C, disinfecting, and processing the material at 35-40 degrees C, to obtain the final product.
NOVELTY - Manufacture of hydrocortisone (VI) involves performing etherification of (14S)-14-hydroxy-2,15-dimethyl-5-oxotetracyclo(8.7.0.02,7.011,15)heptadeca-1(17),6-diene-14-carbonitrile (III), obtaining (14S)-14-(chloromethoxy)-2-methyl-5-oxo-15-(2-silylethyl)tetracyclo(8.7.0.02,7.011,15)heptadeca-1(17),6-diene-14-carbonitrile (IV), rearranging, obtaining (14R)-14-acetyl-14-hydroxy-2,15-dimethyltetracyclo(8.7.0.02,7.011,15)heptadeca-1(17),6-dien-5-one (V) and subjecting resultant compound to displacement reaction.    USE - Manufacture of hydrocortisone (claimed).    ADVANTAGE - The method enables manufacture of hydrocortisone with high yield, by simple, environmentally-friendly and economical process.    DETAILED DESCRIPTION - Manufacture of hydrocortisone of formula (VI) involves reacting (1S)-1-hydroxy-2,15-dimethyltetracyclo(8.7.0.02,7.011,15)heptadec-6-ene-5,14-dione of formula (I) with cyanide, aging, obtaining (1S,14S)-1,14-dihydroxy-2,15-dimethyl-5-oxotetracyclo(8.7.0.02,7.011,15)heptadec-6-ene-14-carbonitrile of formula (II), subjecting resultant compound to elimination, obtaining (14S)-14-hydroxy-2,15-dimethyl-5-oxotetracyclo(8.7.0.02,7.011,15)heptadeca-1(17),6-diene-14-carbonitrile of formula (III), performing etherification of resultant compound, obtaining (14S)-14-(chloromethoxy)-2-methyl-5-oxo-15-(2-silylethyl)tetracyclo(8.7.0.02,7.011,15)heptadeca-1(17),6-diene-14-carbonitrile of formula (IV), rearranging, obtaining (14R)-14-acetyl-14-hydroxy-2,15-dimethyltetracyclo(8.7.0.02,7.011,15)heptadeca-1(17),6-dien-5-one of formula (V) and subjecting resultant compound to displacement reaction.
NOVELTY - Method for improving anaerobic digestion of corn stock involves crushing corn stock, pretreating using potassium hydroxide and metal salt as preprocessing agent, adding water in an amount of 6 times of amount of corn stock, stirring, sealing, subjecting to anaerobic fermentation using activated sludge in reactor at room temperature for 3 days, adding water in amount of 80% of total volume of reactor, filling nitrogen, sealing with a rubber stopper, placing the reactor in a shaker, and shaking at 35 plus minus 2 degrees C.    USE - Method for improving anaerobic digestion of corn stock in production of methane.    ADVANTAGE - The method enables quick improvement of anaerobic digestion of corn stock, and provides methane with high productivity.    DETAILED DESCRIPTION - Method for improving anaerobic digestion of corn stock involves crushing corn stock, pretreating using potassium hydroxide and metal salt as preprocessing agent, adding water in an amount of 6 times of amount of corn stock, stirring, sealing, subjecting to anaerobic fermentation using activated sludge in reactor at room temperature for 3 days, adding water in amount of 80% of total volume of reactor, filling nitrogen, sealing with a rubber stopper, placing the reactor in a shaker, and shaking at 35 plus minus 2 degrees C. The metal salt includes 1-15 wt.% iron chloride(II) tetrahydrate, 0.05-1 wt.% cobalt(II) chloride hexahydrate and 0.05-1 wt.% nickel(II) chloride hexahydrate based on amount of corn stock. The amount of potassium hydroxide is 2 wt.% based on amount of corn stock. The amount of activated sludge and corn stock is 52 g TS and 12 g TS, respectively.
NOVELTY - Preparation of maleic acid salt comprises reacting 3,4-dicarboxylic acid pyridine and acetic anhydride, under catalyst carrying out Friedel-Crafts reaction pyridine-3,4-anhydride and 1,4-difluorophenyl to obtain 4-(2',5'-difluorobenzoyl) nicotinic acid and 3-(2',5'-difluorobenzoyl) isonicotinic acid mixture, processing dehydration cyclization, reacting product with hydrogen, concentrating, adding to aqueous solution of maleic acid, stirring at room temperature overnight, filtering, washing, and drying.    USE - Method of preparation of maleic acid salt (claimed).    ADVANTAGE - The method restrains generation of side reaction, reduces impurity content, is simple, and increases yield.    DETAILED DESCRIPTION - Preparation of maleic acid salt comprises:    (A) reacting 3,4-dicarboxylic acid pyridine and acetic anhydride react, and obtaining pyridine-3,4-anhydride;    (B) under catalyst, carrying out Friedel-Crafts reaction pyridine-3,4-anhydride and 1,4-difluorophenyl to obtain 4-(2',5'-difluorobenzoyl) nicotinic acid and 3-(2',5'-difluorobenzoyl) isonicotinic acid mixture;    (C) processing dehydration cyclization to obtain intermediate 6,9-difluorobenzo(g)isoquinoline-5,10-dione;    (D) under protection of nitrogen, reacting ethylene diamine with R-Cl, with protecting group-containing ethylene diamine; and    (E) under catalyst, reacting product with hydrogen, concentrating, adding to aqueous solution of maleic acid, stirring at room temperature overnight, filtering, washing, and drying.    R=Cbz and Fmoc.
NOVELTY - Methane fermentation system includes primary fermentation system (10) and secondary fermentation system (40). The primary fermentation system is mounted higher than the level of secondary fermentation system and both are connected by a guide pipe (22). The primary fermentation system includes primary fermentation pipeline and barrel (12). The barrel contains inlet, which is provided in the primary fermentation pipeline and an outlet that extends to the bottom of the primary fermentation pipeline.    USE - Methane fermentation system.    ADVANTAGE - The methane fermentation system has large capacity, and promotes effective stirring of slurry and uniform distribution of bacteria, and improves fermentation efficiency.    DETAILED DESCRIPTION - Methane fermentation system includes primary fermentation system and secondary fermentation system. The primary fermentation system is mounted higher than the level of secondary fermentation system and both are connected by a guide pipe. The primary fermentation system includes primary fermentation pipeline and barrel. The barrel contains inlet, which is provided in the primary fermentation pipeline and an outlet that extends to the bottom of the primary fermentation pipeline. The primary fermentation pipeline is separated with partitions and present in cylinder, which is divided into levels. Primary fermentation pipeline from inside is provided with primary fermentation zone, which is provided with air resistance plates. The secondary fermentation system includes secondary fermentation pipeline, feeding tube (42) and discharging tube (44).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane fermentation system.    Primary fermentation system (10)    Barrel (12)    Guide pipe (22)    Secondary fermentation system (40)    Feeding tube (42)    Discharging tube (44)
NOVELTY - Composite microbial inoculant comprises 3. 5-23.5 pts. wt. photosynthetic bacteria, 0.2-3.8 pts. wt. Lactobacillus bulgaricus, 1-10 pts. wt. Bacillus subtilis and 0.4-7 pts. wt. Saccharomyces cerevisiae.    USE - Composite microbial inoculant used for fixing soil damaged by cadmium (claimed).    ADVANTAGE - The composite microbial inoculant reduces the activity of health hazardous cadmium in the soil, in an easy and simple manner. The environmental-friendly composite microbial inoculant decreases heavy metals cadmium content by 20.3% as compared with the control group.
NOVELTY - Recrystallizing gibberellin mother liquid involves mixing gibberellin mother liquid and extracting agent in weight ratio of 1:2-5, uniformly stirring obtained mixture, and adding alkaline solution to mixture for regulating pH to 4.0-7.0. Acid solution is further added to obtained product for regulating pH to 1.5-3.5. The obtained product is dehydrated to remove water. The product is concentrated, and filtered to remove dehydrating agent. The obtained material is crystallized to obtain the desired product.    USE - Method for recrystallizing gibberellin mother liquid (claimed).    ADVANTAGE - The method enables recrystallizing gibberellin mother liquid in an eco-friendly manner.
NOVELTY - A biological carbon comprises 590-600 pts. wt. coal gangue, 390-400 pts. wt. yellow garbage, 2-3 pts. wt. potassium nitrate, 4-4.5 pts. wt. sodium nitrate, 3-3.5 pts. wt. borax, 2-2.1 pts. wt. efficient plant particle, and 200-250 pts. wt. water.    USE - Biological carbon used as industrial and civil fuel.    ADVANTAGE - The carbon has full combustion, reduced fly ash, reduced heat loss, increased heat efficiency of 70-90%, reduced sulfur dioxide content in fume, reduced environment pollution, and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of biological carbon comprising crushing coal gangue and yellow garbage, uniformly stirring, adding the rest of the materials, mixing, cold pressing by forming, and drying to obtain the finished product.
NOVELTY - Selenium-enriched organic fertilizer comprises 12-18 pts. wt. fermentation material, 6-10 pts. wt. mineral substance, 0.5-0.8 pts. wt. Bacillus subtilis strain ATCC 6633, 30-40 pts. wt. selenium-enriched rice bran, 5-10 pts. wt. cassava starch and 15-20 pts. wt. humic acid. Fermentation material comprises 10-20 pts. wt. soybean, 1-3 pts. wt. humic acid, 3-5 pts. wt. molasses, 0.1-0.2 pts. wt. sodium selenite and 0.1-0.2 pts. wt. Bacillus subtilis strain ATCC 6633. Mineral substance comprises 40-60 pts. wt. phosphate, 40-60 pts. wt. maifanite and 1-3 pts. wt. silicon powder.    USE - Selenium-enriched organic fertilizer.    ADVANTAGE - The selenium-enriched organic fertilizer is eco-friendly, and improves soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing selenium-enriched organic fertilizer, which involves mixing components with fermentation material and carrying out natural fermentation in a fermentation pool for 1-2 weeks.
NOVELTY - Method for catalytic hydrothermal conversion of wet biomass to hydrocarbon fuel, involves processing bio-based lipid bi-metal catalyst at high temperature and high pressure in reactor, where the reactor is pressurized to deoxygenation reaction.    USE - The method is useful for catalytic hydrothermal conversion of wet biomass to hydrocarbon fuel (claimed).
NOVELTY - Converting greenhouse gasses into oxygen and biomass involves using photobioreactor. The greenhouse gasses are fed into photobioreactor with saline water and nutrients. The photobioreactor contains algae, which converts greenhouse gasses into biomass and oxygen.    USE - Method for converting greenhouse gasses into oxygen and biomass (claimed).
NOVELTY - Production of syngas involves feeding biomass feedstock to gasification reaction apparatus through feeding device, subjecting to pyrolysis and gasification, reforming in presence of gasification reaction medium, obtaining water, carbon dioxide, and porous solid product, subjecting to high-temperature catalytic gasification in presence of high-temperature catalyst in a reactor, obtaining semi-coke and tar, and subjecting obtained semi-coke and catalyst to microwave reformation under syngas production conditions.    USE - Production of syngas (claimed).    ADVANTAGE - The method enables efficient and simple production of high-quality syngas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for producing syngas.
NOVELTY - A composite acid catalyst comprises composite acid ionic liquid including cesium salt of 12-tungstophoric acid, and 1-methyl-3-propanesulfonic-imidazolium hydrosulfate, in a mass ratio of 1:0.2-1.    USE - Composite acid catalyst is used for preparing biodiesel (claimed).    ADVANTAGE - The composite acid catalyst has high specific surface area, excellent activity and solubility, and is prepared by simple process under mild reaction conditions.    DETAILED DESCRIPTION - A composite acid catalyst comprises composite acid ionic liquid including cesium salt of 12-tungstophoric acid (Cs2.5H0.5PW12O14), and 1-methyl-3-propanesulfonic-imidazolium hydrosulfate, in a mass ratio of 1:0.2-1. INDEPENDENT CLAIMS are included for the following:    (1) preparation of composite acid catalyst; and    (2) usage of composite acid catalyst in preparation of biodiesel, which involves carrying out transesterification reaction of waste oil as raw material, with lower aliphatic alcohol under the action of the composite acid catalyst, filtering, and washing.
NOVELTY - Method for culturing salt-tolerant aerobic activated sludge involves preparing a mixed solution containing salt-tolerant microorganism in high-salt environment, aerating the mixed solution to promote the formation of salt-tolerant microorganisms, dehydrating, and culturing obtained aerobic activated sludge in an open environment. The concentration of inorganic salt in culture system is 1-25%.    USE - Method for culturing salt-tolerant aerobic activated sludge (claimed).
NOVELTY - Domestic environmentally friendly enzyme fermentor comprises a tank body, a separation slag groove placed in the tank body, a pressing plate set in slag groove, a top cover above the tank body and a cylindrical piston. The top cover is provided with a concave edge, where the tank body is tightly fastened to the top cover via the concave edge. The middle of the cover is set with a cylindrical feed tube. The cylindrical piston is set within the cylindrical feed tube. The top of the pressing plate is set with a through hole. The bottom of the tank body is set with a feeding device.    USE - Used as domestic environmentally friendly enzyme fermentor.    ADVANTAGE - The fermentor: has simple construction; and is convenient to use.    DETAILED DESCRIPTION - Domestic environmentally friendly enzyme fermentor comprises a tank body, a separation slag groove, a pressing plate, a top cover and a cylindrical piston. The separation slag groove is placed in the tank body. The pressing plate is placed in the slag groove. The top cover is set above the tank body. The top cover is provided with a concave edge, where the tank body is tightly fastened to the top cover via the concave edge. The middle of the cover is set with a cylindrical feed tube. The cylindrical piston is set within the cylindrical feed tube. The top of the pressing plate is set with a through hole, which is in consistent with the size of the cylindrical feed tube. The bottom of the tank body is set with a feeding device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the domestic environmentally friendly enzyme fermentor.
NOVELTY - High-yield oil Scenedesmus bijuga SDEC-12 deposited under CCTCC No. M2014497 is new.    USE - The new high-yield oil S. bijuga SDEC-12 is useful for treating, preferably for purifying wastewater (including industrial or municipal wastewater) and/or exhaust gas from industrial emissions, and for preparing biodiesel and/or grease (all claimed).    ADVANTAGE - The high-yield oil S. bijuga SDEC-12 has excellent oxidation stability and low-temperature fluidity, and is capable of efficiently treating wastewater thus achieving both economic and environmental benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of high-yield oil S. bijuga SDEC-12.
NOVELTY - Preparation of photoluminescent carbon quantum dots involves uniformly mixing milk and deionized water, pouring the resultant mixture into a reactor placed in an oven, carrying out hydrothermal reaction process, removing the reactor, after completion of the reaction, cooling to room temperature, obtaining brownish yellow aqueous dispersion, maintaining, centrifuging, removing supernatant containing photoluminescent carbon quantum dots, washing using deionized water and obtaining aqueous solution containing uniform dispersion of carbon photoluminescent quantum dots.    USE - Preparation of photoluminescent carbon quantum dots used in nanotechnology, drug delivery, biological detection, photoelectric conversion and catalytic fields.    ADVANTAGE - The method provides photoluminescent carbon quantum dots by simple and environmentally-friendly process.
NOVELTY - Method for producing organic fertilizer, involves mixing 20-23 pts. wt. straw residue, 22-25 pts. wt. seaweed residue, 23-26 pts. wt. livestock manure, 25-28 pts. wt. chelated molasses alcohol fermentation liquid, 0.3-0.6 pt. wt. urea, 0.5-0.8 pt. wt. calcium phosphate, 1-1.3 pts. wt. potassium sulfate and 0.01-0.04 pt. wt. compost, fermenting the mixture at 36-42 degrees C for 6-9 days, turning the mixture once every 2-3 days, drying the fermented product, crushing the dried product, passing through 10-20 mesh sieve, and granulating obtained product.    USE - The method is used for producing organic fertilizer (claimed).    ADVANTAGE - The produced organic fertilizer is rich in organic matter.
NOVELTY - Application of hydrogen donor solvent and surfactant in the methanation reactions involves adding hydrogen donor solvent and 1-12.5 vol.% surfactant to slurry bed reactor, and carrying out methanation reaction in the presence of methanation catalyst. The ratio of catalyst and hydrogen donor solvent is 0.002-0.01 g:1 ml. The hydrogen donor solvent is tetrahydronaphthalene, decahydronaphthalene or ethylene glycol.    USE - Application of hydrogen donor solvent and surfactant in methanation reactions (claimed).    ADVANTAGE - The methanation reaction is carried out efficiently in slurry bed reactor using hydrogen donor solvent and surfactant.
NOVELTY - An L-glufosinate-N-carboxylic anhydride is new.    USE - An L-glufosinate-N-carboxylic anhydride for preparation of highly pure L-glufosinate (claimed).    ADVANTAGE - Product has strong selectivity and high conversion, and preparation process has low energy consumption and low environmental pollution.    DETAILED DESCRIPTION - An L-glufosinate-N-carboxylic anhydride of formula (IV) is new. INDEPENDENT CLAIMS are included for:    (1) preparation of L-glufosinate-N-carboxylic anhydride of formula (IV); and    (2) use of L-glufosinate-N-carboxylic anhydride in obtaining L-glufosinate which involves mixing L-glufosinate-N-carboxylic anhydride and 36-38 mass% concentrated hydrochloric acid, heating to reflux, evaporating to dryness, adding 95 vol.% aqueous ethyl alcohol solution, heating to reflux, adding 95 vol.% of 2 ml aqueous ethyl alcohol solution until solids are completely dissolved, cooling with ice water to 30 degrees C, adding ethylene oxide, standing at 5-10 degrees C for 12 hours, completely crystallizing, filtering, vacuum drying filter cake at room temperature vacuum drying in which ratio of L-glufosinate-N-carboxylic anhydride and ethylene oxide is 1:2-4, volume of concentrated hydrochloric acid with L-glufosinate-N-carboxylic anhydride is 6 L/mol, and amount of 95 vol.% aqueous ethyl alcohol solution alcohol with L-glufosinate-N-carboxylic anhydride is 3 ml/mmol.
NOVELTY - Small and efficient multifunctional device for methane fermentation comprises a fermenter; a seal attached to the top of the fermentation tank cover, disposed on the roof of the gas output tube , provided at a lower portion of the fermenter feed tube, provided on a side wall of the fermenter discharge tube, and disposed in a center of the fermenter biogas tube; a rotatable biogas socket on the sleeve tube; a fermentation tank fastened in socket on sleeve pressure plate; fastening unit interposed in the nip plate cannula; and insulation unit in the outer side of the fermentation tank.    USE - The small and efficient multifunctional device is useful for methane fermentation (claimed). Generally, it can be used in small-scale biogas fermentation process.    ADVANTAGE - Small, compact, versatile and efficient biogas device is provided.
NOVELTY - Stainless steel anaerobic gas power supply station comprises anaerobic tank, purification tower, anaerobic tank heating system, and power generation unit comprising stainless steel anaerobic tank constructed from stainless steel materials.    USE - The stainless steel anaerobic gas power supply station is useful for gas production e.g. biogas production.    ADVANTAGE - The stainless steel anaerobic gas power supply station has improved efficiency for biogas production and gas production; can save investment cost; and has environmental protection effect.
NOVELTY - The station has an anaerobic tanks, a purification tower, an anaerobic tank warming systems, a power generation unit with four large unit formed of the building material of anaerobic tank for carbon steel, and structure for carbon steel welding. The anaerobic tank is sealed, and is divided into the main anaerobic tank, a deputy anaerobic tank, an excretion anaerobic tank and other components. Each anaerobic tank is cylindrical, and top design gas storage cabinet is consistent in the upper and lower side of the design ladder (2) contacting with the ground at the base.    USE - Carbon steel structure anaerobic power supply station.    ADVANTAGE - Increase biogas production efficiency since anaerobic tank group and a purifying tower group, power generation unit, pressure pump and fuel gas boiler complement to each other. Saves raw material, increases efficiency, and protects environment by using sewage farm and straw.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the anaerobic tank stirring tank longitudinal structure.    Ladder (2)    Stirrer (18)    Feeder (19)    Feeder feeding tube (20)    Feeder bracket (21)
NOVELTY - The station has an anaerobic tank with a purifying tower, an anaerobic tank heating system, a power generation unit with four large unit formed of the building material of rubber anaerobic tank, and a rubber and steel structure beam column frame structure. The anaerobic tank is sealed, and is divided into the main anaerobic tank, a deputy anaerobic tank, an excretion anaerobic tank and other components. Each anaerobic tank is cylindrical, and top design gas storage cabinet is consistent in the upper and lower side of the design ladder (2) contacting with the ground at the base.    USE - Rubber steel mixing structure anaerobic power generation gas station.    ADVANTAGE - Increase biogas production efficiency since anaerobic tank group and a purifying tower group, power generation unit, pressure pump and fuel gas boiler complement to each other. Saves raw material, increases efficiency, and protects environment by using sewage farm and straw.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the anaerobic tank stirring tank longitudinal structure.    Ladder (2)    Stirrer (18)    Feeder (19)    Feeder feeding tube (20)    Feeder bracket (21)
NOVELTY - The system has a feed pipe (10), a discharge pipe (20), a fermentation pipe (30), and a pressure pipe (40). The fermentation pipe is connected to both ends of the feed pipe and the discharge pipe. The pressure pipe is mounted at the top of the fermentation pipe. The fermentation pipe is equipped with a feed pipe blocking plate (32), baffle plates (36,38), and a discharge pipe blocking plate (34). A gas-guide pipe (31) is connected on portion of each cell that is formed by the space between adjacent blocking plates in the fermentation pipe, and is set with valve.    USE - Pipeline biogas fermentation system lifting biogas turbulence effect.    ADVANTAGE - The use of biogas flow stirring facilitates uniform distribution of strain, and promotes fermentation of raw materials within the fermentation system. Gas production of the fermentation system is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic sectional view of the pipeline biogas fermentation system.    Feed pipe (10)    Discharge pipe (20)    Fermentation pipe (30)    Gas-guide pipe (31)    Feed pipe blocking plate (32)    Discharge pipe blocking plate (34)    Baffle plates (36,38)    Pressure pipe (40)
NOVELTY - The generating method involves placing the raw material into a fermentation system through a feed tube (10) to produce biogas, and collecting the gas in the feed tube or discharge tube side wall. The fermentation tube (30) is equipped with blocking plates (34-38) which form a cell or space between adjacent plates. The gas pressure in the cell is increased, pushing the flow of fermentation biogas into the discharge tube (20). The biogas in-room pressure is drained back from the discharge tube into the fermentation tube to complete the circulation flow of slurry.    USE - Methane generating method of methane generating device with detachable discharge tube.    ADVANTAGE - Stirring performance of biogas slurry circulation flow is improved. The use of biogas flow stirring promotes uniform distribution of strain, and increases gas production of the fermentation system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic sectional view of the fermentation system.    Feed tube (10)    Discharge tube (20)    Fermentation tube (30)    Blocking plates (34-38)    Pressure pipe (40)
NOVELTY - Micro-RNA comprises 20 nucleobases (SEQ ID NO: 1).    USE - Micro-RNA for preparing medicine for inhibiting tyrosinase activity in plants (claimed).    ADVANTAGE - The micro-RNA is natural plant extract, eco-friendly, can be stored for longer time at low temperature, and enables to prepare drug in simple and cost-effective manner.    DETAILED DESCRIPTION - Micro-RNA comprises 20 nucleobases (SEQ ID NO: 1), that are uuggcauucuguccaccucc.
NOVELTY - Method of improving anaerobic methane production efficiency of high or short-chain fatty acids involves adding graphite as additive to anaerobic fermentation system of short-chain fatty acids, and mixing short-chain fatty acids, anaerobic microorganisms, and graphite to increase number and activity of microorganisms.    USE - Method of improving anaerobic methane production efficiency of high or short-chain fatty acids.    ADVANTAGE - Production efficiency and yield of methane are improved.
NOVELTY - Method of using linear methane generation system to promote uniform distribution of methane producing bacteria involves fermenting raw material in fermentation system to produce biogas, accumulating biogas in fermentation zone formed between adjacent blocking plates (36, 38), allowing pressure in methane fermentation zone to increase, allowing biogas to flow in pipeline feeding tube (10), discharge tube (20), cloth device, and hydraulic discharge pipe (44), using fermentation zone biogas, lowering biogas pressure in fermentation area, and circulating biogas slurry in pipeline feeding tube.    USE - Method of using linear methane generation system to promote uniform distribution of methane producing bacteria.    ADVANTAGE - Problems relating to poor slurry mixing performance, uneven distribution of species, and low efficiency of gas production can be solved.    DETAILED DESCRIPTION - Method of using linear methane generation system to promote uniform distribution of methane producing bacteria involves fermenting raw material in fermentation system to produce biogas, accumulating biogas in fermentation zone formed between adjacent blocking plates (36, 38), allowing pressure in methane fermentation zone to increase, allowing biogas to flow in pipeline feeding tube (10), discharge tube (20), cloth device, and hydraulic discharge pipe (44), using fermentation zone biogas, lowering biogas pressure in fermentation area, circulating biogas slurry in pipeline feeding tube and cloth pipeline, completing circulation of biogas slurry, and using other biogas in fermentation zone.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a linear methane generation system.    Pipeline feeding tube (10)    Discharge tube (20)    Blocking plates (36, 38)    Hydraulic discharge pipe (44)
NOVELTY - Microwave-assisted pre-treatment method of corn stover involves mixing corn stover and ethylenediamine solution in confined conditions and subjecting obtained mixture to microwave treatment and heat treatment to obtain pre-treated corn stover.    USE - Microwave-assisted pre-treatment method of corn stover.    ADVANTAGE - The method effectively degrades lignin, reduces cellulose crystallinity, improves efficiency of hydrolysis of corn stover cellulose and hemicellulose, is simple, does not require the use of high-pressure equipment, has low energy consumption, and is suitable for industrial production.
NOVELTY - Puerarin crude product and soybean daidzein crude product are prepared by crushing dry radix puerariae, spray-drying raw material with water, stacking, covering, insulating, naturally fermenting at 24-48 hours to 50-55 degrees C, cooling to 25-35 degrees C, placing in a tank, extracting thrice under reflux, combining extraction liquids, filtering, introducing filtrate into distillation recovery tank, filtering filter cake to obtain filtrate, dehydrating filtrate to obtain greater than or equal to 25% puerarin crude product, washing filter cake with clean water, and drying to obtain greater than or equal to 55% soybean daidzein crude product.    USE - Preparation of puerarin crude product and soybean daidzein crude product by fermentation.    ADVANTAGE - The extracted puerarin and daidzein content is a 14-16% improvement from previous methods. The method has increased product yield, low production cost, and low environmental impact.    DETAILED DESCRIPTION - Puerarin crude product and soybean daidzein crude product are prepared by crushing dry radix puerariae into 20-40 meshes of coarse powder, spray-drying raw material with 2-2.5 times of water into wet material, stacking wet material, covering, insulating, naturally fermenting at 24-48 hours to 50-55 degrees C, naturally cooling to 25-35 degrees C when fermentation is finished to obtain fermented material, placing in a tank, extracting thrice under reflux, each time using 5-10 times the amount of 9% ethanol or methanol to obtain extraction liquid, combining extraction liquids, filtering to obtain filtrate, introducing filtrate into distillation recovery tank through liquid pump to dilute filtrate, filtering filter cake to obtain filtrate, dehydrating filtrate to obtain greater than or equal to 25% puerarin crude product, washing filter cake with clean water, and drying to obtain greater than or equal to 55% soybean daidzein crude product.
NOVELTY - A fermented sugar from bamboo biomass waste enzymatic hydrolysis 2-step preprocessing is produced by naturally drying bamboo waste slice, crushing, sieving coarse bamboo powder, soaking bamboo powder in dilute alkali or dilute acid, performing steam blasting process at ratio of bamboo powder and water of 1:10-20 g/ml and steam pressure of 1-2 MPa for 6-10 minutes, washing with water until neutral, drying, adding 5-30 FPU cellulase and beta -glucosidase per gram of material from steam explosion process, and hydrolyzing at 45-60 degrees C and 100-150 rpm for 48-72 hours.    USE - Production of fermented sugar from bamboo biomass waste enzymatic hydrolysis preprocessing.    ADVANTAGE - Production process utilizes petrochemical resources and waste.
NOVELTY - Method for performing cattle breeding and producing cattle manure, involves setting cattle breeding unit and cattle manure production facility adjacently, providing bullpen, cow manure collecting plots, cowshed and ditches connected by underground pipe below the bullpen, continuously collecting the manure from the bullpen, mixing the collected manure, corn stalks or sunflower stalks, and water in ditch having piping facilities and forming heap of the manure.    USE - The method is useful for performing cattle breeding and producing cattle manure (claimed).
NOVELTY - Composite herbicide comprises 3-20 pts. wt. scattered broadleaf, 1-10 pts. wt. chlorophenol, 3-10 pts. wt. pretilachlor, 2-8 pts. wt. butralin, 8-10 pts. wt. diatomite, 5-10 pts. wt. surfactant and 10-20 pts. wt. water.    USE - Used as composite herbicide.    ADVANTAGE - The herbicide exhibits good weeding effect, does not provide drug resistance to weeds, and has long term effect. The method has simple preparation procedure, and is environmental friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing herbicide, comprising (i) mixing scattered broadleaf, chlorophenol and pretilachlor, and uniformly mixing by adding surfactant; (ii) adding water, and rotating at a speed of 200-400 rotations/minute, and mechanically stirring for 30-50 minutes, and stirring by adding butralin; and (iii) adding diatomite into traditional Chinese medicinal liquid, and mechanically stirring for 10-30 minutes under rotating speed of 200-400 rotations/minute, to obtain the final product.
NOVELTY - Producing organic fertilizer using sugar mill mud, by mixing sugar mill mud and adjusting material having moisture content of 10-70%, adding the mud fermentation material into a three-dimensional fermentation apparatus composed of 2-40 layers and 2-40 groups of belt conveyors in the horizontal direction for dynamic aerobic fermentation, and after the mud fermentation material is converted into a decomposed organic material, directly applying the decomposed organic material as an organic fertilizer or an organic raw material for producing organic fertilizer products.    USE - The method is used for producing organic fertilizer using sugar mill mud (claimed).    ADVANTAGE - The method is environmentally-friendly.    DETAILED DESCRIPTION - Method for producing organic fertilizer using sugar mill mud, involves mixing sugar mill mud having moisture content of 60-80% and adjusting material having moisture content of 10-70% to obtain a mud fermentation material having moisture content of 50-75%, adding the mud fermentation material into a three-dimensional fermentation apparatus composed of 2-40 layers and 2-40 groups of belt conveyors in the horizontal direction for dynamic aerobic fermentation, and after the mud fermentation material is converted into a decomposed organic material, directly applying the decomposed organic material as an organic fertilizer or an organic raw material for producing organic fertilizer products.
NOVELTY - Improving saline land, by using water purification plant sludge compost which is prepared by collecting sludge, stacking, drying, adding cow dung and crushed straw, adjusting moisture content and organic matter content fermenting in 2 phases, preferably medium temperature phase and high temperature phase, adjusting moisture content, carbon/nitrogen ratio, and pH, turning, ventilating, adjusting oxygen content, increasing ventilation time, fermenting, composting, adjusting pH and moisture content, processing, granulating the processed product, and drying the granules.    USE - The process is used for improving saline land using water purification plant sludge compost (claimed).    DETAILED DESCRIPTION - Process for improving saline land, involves using water purification plant sludge compost which is prepared by collecting sludge, stacking, drying, adding cow dung and crushed straw, where the sludge, cow dung and straw are in mass ratio of 20:10:1, adjusting moisture content to 63% and organic matter content to 25-85%, fermenting in 2 phases, preferably medium temperature phase and high temperature phase for 9-13 days, adjusting moisture content to 35-63%, carbon/nitrogen ratio to 20-45, and pH to 5-6.5, turning once every 2-3 days for 6-9 hours, ventilating for 10 hours/day, adjusting oxygen content to 7-16%, in last 1-2 days increasing ventilation time when temperature reaches 60 degrees C, fermenting at 37-40 degrees C and carbon/nitrogen ratio of 25 or less for 18-26 days, composting, adjusting pH to 6.5-8.5, and moisture content to 27-33%, processing, granulating the processed product, and drying the granules.
NOVELTY - Organic fertilizer is prepared using 30-40 pts. wt. chicken manure, 20-35 pts. wt. decomposed plant straw, 10-15 pts. wt. wheat bran, 10-15 pts. wt. peanut oil residue, 5-10 pts. wt. oil sludge, 5-10 pts. wt. humic acid, 2-5 pts. wt. urea, 10-20 pts. wt. trace elements, 5-10 pts. wt. complex microbial agent and 5-10 pts. wt. functional microbial agent.    USE - As organic fertilizer for watermelon.    ADVANTAGE - The organic fertilizer enables to improve quality and yield of watermelon.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) weighing the above-mentioned raw materials, mixing uniformly except complex microbial agent and functional microbial agent, and stacking mixture, (b) spraying complex microbial agent and functional microbial agent, adjusting moisture content to 70%, fermenting mixture at 60 degrees C for 15 days, and turning mixture once for every four days, (c) adding functional microbial agent to fermented material when the temperature of fermented material reaches 40 degrees C, stacking mixture and fermenting mixture for seven days, and (d) crushing fermented product obtained from (c), sieving, granulating, drying, cooling, and packaging to obtain the product.
NOVELTY - Microbial soil conditioner comprises environmentally-friendly type decomposing bacterial strain and soil restoration-type bacterial strain.    USE - The microbial soil conditioner is useful for nourishing soil.    ADVANTAGE - The soil conditioner is environmentally-friendly, and utilizes traditional Chinese medicinal residue.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned microbial soil conditioner, which involves activating the above-mentioned bacterial strains, mixing the activated bacterial strains, and culture medium in a weight ratio of 1:80-120 to obtain bacterial culture, and mixing the obtained bacterial culture and feedstock in a weight ratio of 1:15-40, where the feedstock comprises Chinese medicinal residue, brown sugar, sodium hydrogen phosphate and calcium carbonate.
NOVELTY - Green lightweight matrix comprises decomposed vinegar residue, 3-6 parts cassava residue and crop straw mixed powder, 1-2 parts coconut husk silk, 1-2 parts ash, 1-2 parts peat, 0.5-1 parts perlite and 0.2-0.5 wt.% ternary compound fertilizer. The substrate has 35-50% water content, 65-75% total porosity, 0.35-0.5g/ml bulk density, 30% dry matrix organic matter content and 2-3% total nutrient content. The substrate has gas-water ratio of 1:2-4. The pH of substrate is 5.5-7.0.    USE - Used for gardens of high rise buildings.    ADVANTAGE - The matrix has brown color, no smell, specific gravity, high nutrient, and is suitable for urban trunk rails and overpasses.
NOVELTY - A garbage leachate is extracted by taking garbage filter liquid for detoxification treatment, and transporting treated waste leachate to roots of coconut trees.    USE - Method for extracting garbage leachate (claimed).    ADVANTAGE - The method has simple and convenient operation. It saves cost, and is ecological and environment-friendly.
NOVELTY - Manufacture of biologically-derived paraffinic jet and diesel fuels, solvents and base oils involves hydrotreating a biological hydrocarbonaceous oxygenated oil comprising triglycerides to form effluent mixture (A) comprising propane, carbon monoxide, carbon dioxide, water and n-paraffinic product, recovering the n-paraffinic product from the effluent mixture, and converting n-paraffinic product over a paraffin disproportionation catalyst to form effluent mixture (B) comprising light n-paraffinic biologically derived product and a heavy n-paraffinic biologically derived product.    USE - Manufacture of biologically-derived paraffinic jet and diesel fuels, solvents and base oils (claimed).    ADVANTAGE - The method enables manufacture of biologically-derived paraffinic jet and diesel fuels with high yield.
NOVELTY - The new type utility claims have one kind novel biomass gasification furnace, comprising a furnace body and a hollow cavity body, provided with feedstock wherein at upper part of furnace body, set with a slag outlet at the lower part of furnace body, wherein the furnace body side wall also respectively set with the air inlet and air outlet, provided with stirrer, the stirrer rotating shaft corresponding and connected in internal body cavity body, the rotating shaft by rotating electric machine drive set at upper part of furnace body, and provided with the inner wall adhered the wall scraping piece on the furnace body inner cavity body, wall and scratching piece corresponding to connected with the connecting rod, the connecting rod and the telescopic scratching motor connected with the telescopic motor is set with furnace body, scratching another end of connecting pole is in up and down sliding in the connecting rod sleeve. And process the utility new type capable of combusting in the biomass raw material in the furnace body by stir, effectively increase have biomass raw material and combustion efficiency, preventing burning process generate the tar equal accessory product adhesion plate, avoid have corrosion and combustion efficiency of the furnace body descending.
NOVELTY - A device comprises hydrogen evolution reaction catalyst, where the catalyst comprises component selected from transition metal phosphides, first row transition metal sulfides, and transition metal arsenides.    USE - Device.    ADVANTAGE - The device exhibits improved hydrogen evolution reaction.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) an electrode at which a hydrogen evolution reaction occurs    (2) a system comprising electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an electrode including hydrogen evolution catalyst.    Catalytic layer (6)    Electrode base (8)
NOVELTY - The method involves partially endothermally gasifying organic raw material e.g. biomass, in a reaction chamber (1) of a reactor (100) under usage of water vapor. Residues produced after the partial gasification of the material are supplied to other reaction chambers (2, 3, 4) in particulate form, where the residues are further endothermally gasified. The gasification of the material and/or the residues is carried out with temperature of 700 to 900 degrees Celsius. The chambers used for gasification are commonly heated, where gas products are produced during the gasification of the material.    USE - Method for producing gaseous mixture by partial thermal gasification of organic raw material e.g. biomass, charcoal, biogenous and/or fossil hydrocarbons (all claimed) in liquid or gaseous state.    ADVANTAGE - The method enables the supplying of the residues produced after the partial gasification of the material to other reaction chambers in particulate form, where the residues are further endothermally gasified, thus achieving improved gasification of the organic raw material in an efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of a reactor.    Reaction chambers (1-4)    Combustion chamber (5)    Steam pipe (7)    Collecting pipe (11)    Reactor (100)
NOVELTY - The new type utility claims have one plant with gas processing device of biomass gasification furnace, comprising making sum tank, a vibrator and gas processing device, in the artificial tank provided with sum in one layer, making sum on tank top provided with sealing cover, sealing cover set with feedstock wherein the feedstock wherein the upper part is provided with heating device, bottom of tank provided with sum; in the vibrator provided with motor, a connecting rod and a pressure plate, the connecting rod through sealing cover centre extends to making sum tank in, a connecting rod extends out one end making sum of tank through an eccentric wheel connected to motor transmission shaft on the left end of the air outlet pipe connected with gas processing device, gas processing device comprises processing device air inlet, dust and waste liquid collector and heat exchange tube, and right side dust and waste liquid collector by connecting pipe connected with processing device. The utility model is new type of construction is simple, the gas treatment device can be formed for gas from gasification furnace and from the cooling process, and to gas separation for the waste liquid and dust.
NOVELTY - The new type utility claims have biomass gasification furnace automatic feeding system of biomass gasification furnace automatic feeding device, sum of valve, atmolysis air suction pipe, frequency conversion adjustable speed motor, spiral transport machine, trigger and baffle plate, an electric inserting plate valve, discharging pipe, sum input tube, fuel gas nozzel, oxygen combustion-supporting pipe, oxygen air blower, air tube and biomass gasification furnace composed of. The utility model is new type of advantages as follows: the utility model is new type automatic degree is high, the PLC system by programming, touching screen set display, frequency conversion regulating, time for preventing biomass gasification furnace feedstock pyrolysis gas leakage to avoid feeding accident is stopped, feeding and cutting material cap top equal accident happen, and the biomass gasification furnace.
NOVELTY - The new type utility claims have one plant with feedstock mixing device of biomass gasification furnace, comprising a furnace body, a feedstock mixing device and fuel gas purification device, in the feedstock mix device provided with heat load sum and mixing room inlet and cone shape, the heat load sum air inlet pipe comprises heat load sum inlet end and heat load sum air inlet pipe, right end is mixing room provided with discharging mouth, the discharging mouth and the furnace feedstock mouth connected with the right side of right end device and an air outlet pipe connected with the pressure control device, the pressure control through connecting pipe connect to gas purification device, fuel gas purification system provided with in sequence by pipeline in series cyclone separator, a dust remover, a water film coke-removing device and drying device. The utility model is new type equipped with the feedstock device can make high temperature catalyst and biomass raw material mixture and carrying out full heat exchange, further increase have catalytic effect of catalyst, the gas purification device can be set to from gasification furnace and from the combustion gas can carry out purification.
NOVELTY - The system has a treated-water flow path which is provided to guide treated water discharged from a gasification reactor to a countercurrent-flow type heat exchanger (30). A raw material introducing unit is provided to introduce a gasification raw material into a low temperature side flow path. The taken-out gasification raw material is heated. A heat-tracing unit (35) is provided to return the heated gasification raw material to the halfway position of a raw material downstream rather than the taken-out position.    USE - System for gasifying gasification raw material such as biomass.    ADVANTAGE - The heat exchange effect in the heat exchanger is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the position of the heat exchanger.    Heat exchanger (30)    Inlet (31)    Discharge port (32)    Heat-tracing unit (35)    Low temperature side flow path (36)
NOVELTY - An electrochemical reactor (20) consists of an anode electrode (21) containing ruthenium and yttria-stabilized zirconia, a cathode electrode (22) containing nickel and a yttria-stabilized zirconia, and an electrolytic membrane (23) containing a yttria-stabilized zirconia, provided between anode electrode and cathode electrode. The electrolytic membrane permeates oxide ions and prevents transmission of carbon monoxide.    USE - Electrochemical reactor is used in composite electrochemical reaction device for generating oxygen gas from carbon dioxide or carbon monoxide, and hydrogen gas from methane (all claimed).    ADVANTAGE - The electrochemical reaction device has high-separation efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composite electrochemical reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the structure of the electrochemical reactor.    Electrochemical reactor (20)    Anode electrode (21)    Cathode electrode (22)    Electrolyte membrane (23)
NOVELTY - A kind of lignocellulose biomass without tar gas in stove of air-gas mixer and gasification furnace part composed of two. Air-gas mixer comprises stove head, water tank, gas introduction, gas-guide hole equal, gasification furnace comprises furnace core independently, dolomite, stainless steel wire net equal, air-gas mixer and gas cylinder and cone gasification furnace is fuel gas outlet, air-gas mixer also pass up the gas pipe and gasification furnace of water sealing groove and tightly connected with the fan. The utility model is new type of splitting the tar separating and sum the quadratic tar catalytic gasification device, change have the same series device in heavy smoke in use process, and pipe system is easy to be blocked, tar and tar produced is difficult to treat and difficult problem.
NOVELTY - The device has a settling chamber (7) whose upper part is connected with a biomass fuel gas inlet. An insulating layer (11) is formed close to the settling chamber that is connected with a high temperature combustion-supporting air pipeline (12). A fuel gas pipe (9) is connected with a high temperature combustion supporting air inlet and a high temperature biomass gas inlet. A high temperature fuel gas inlet of a furnace head (8) is connected with the insulating layer. The air pipeline is connected with the furnace head and the high temperature combustion supporting air inlet.    USE - Biomass gasification furnace fume purification device.    ADVANTAGE - The device reduces discharge amount of nitrogen oxides.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification furnace fume purification device. '(Drawing includes non-English language text)'    Settling chamber (7)    Furnace head (8)    Fuel gas pipe (9)    Insulating layer (11)    High temperature combustion-supporting air pipeline (12)
NOVELTY - Invention can be used in chemical industry. A suspension of nucleating seeds is prepared to obtain iron oxide pigments. At the step of oxidising scrap metal in an acidic medium, 20% aqueous potassium hydroxide solution is used to neutralise the acid and adjust pH. The pigment is washed multiple times. Effluent with potassium sulphate concentration of 5-10% is fed into a vacuum crystallisation apparatus for evaporating solutions. The potassium sulphate-contaminated process water is converted to pure water with salt concentration of 150 g/m3 by evaporation and condensation. The water is used in producing iron oxide pigments. The potassium sulphate obtained from evaporation is used as potassium fertiliser.    USE - Chemistry.    ADVANTAGE - Invention enables to prevent formation of contaminated waste water, solid wastes and ammonia vapour emissions and to obtain potassium sulphate as an additional product.1 dwg
NOVELTY - The method involves providing a symmetric solid oxide fuel cell with a bilayer structure. An anode (110) and a cathode (120) are arranged on two sides of electrolyte (130). A cathode baked material and solid material are obtained by precursor solution that is mixed with an organic binder. An electrode is printed on the sides of the electrolyte. The electrolyte is provided with ceria, lanthanum gallate, mixture, A-doped ceria, yttria stabilized zirconia, a scandia stabilized zirconia, Samaria and gadolinia.    USE - Symmetric solid oxide fuel cell manufacturing method.    ADVANTAGE - The method enables simplifying manufacturing process and improving economic efficiency. The method enables improving electric conductance performance at hydrogen atmosphere. The method enables improving thermal chemical stability, conductivity and large power density of the symmetric solid oxide fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a symmetric solid oxide fuel cell manufacturing method.    Symmetric solid oxide fuel cell (100)    Anode (110)    Cathode (120)    Electrolyte (130)
NOVELTY - Increasing production of ethanol on a cell-mass basis, by providing a microorganism which utilizes a carbon source to produce ethanol, genetically modifying the microorganism, and contacting the modified hemoglobin expressing microorganism with at least one carbon source comprising xylose under anaerobic conditions, where production of ethanol is greater on a cell-mass basis after the microorganism is genetically modified to provide for expression of the hemoglobin than before the microorganism is genetically modified to provide for expression of the hemoglobin.    USE - The method is used for increasing production of ethanol on a cell-mass basis (claimed).    DETAILED DESCRIPTION - Method for increasing production of ethanol on a cell-mass basis, involves (a) providing a microorganism which utilizes a carbon source to produce ethanol, where the microorganism expresses a xylose isomerase gene, (b) genetically modifying the microorganism, where the modifying comprises at least one genetic modification which provides for expression of a hemoglobin gene from a bacterium of Vitreoscilla, and (c) contacting the modified hemoglobin expressing microorganism of step (b) with at least one carbon source comprising xylose under anaerobic conditions, where production of ethanol is greater on a cell-mass basis after the microorganism is genetically modified to provide for expression of the hemoglobin than before the microorganism is genetically modified to provide for expression of the hemoglobin.
NOVELTY - The device has a first hopper (1) for containing bulk materials such as grains, rice husks, saw dust and wood shavings. A second hopper (2) is provided with a chipper for wood waste fragmentation of the material up to 100 mm. A bulk conveyor (5) is continued into a coupling crusher (6). An output coupling part of the coupling crusher is connected to staging masse conveyors (7). An output end of a buffer tank (8) is connected to a discharging screw conveyor (9) joined to a pyrolyzer, where the device is provided with a suction device (10) and the device optionally encompasses a tailing pond.    USE - Device for preparing and dispensing mixture of biomass for pyrolysis processes for treating biomass of agricultural, forest and urban origin into a homogeneous mixture with optimal composition. Uses include but are not limited to grains, rice husks, saw dust and wood shavings.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for preparing and dispensing mixture of biomass.    Hoppers (1, 2)    Bulk conveyor (5)    Coupling crusher (6)    Staging masse conveyors (7)    Buffer tank (8)    Discharging screw conveyor (9)    Suction device (10)
NOVELTY - Preparing biomass mixture comprises: mixing at least one kind of 5-95 wt.% woody biomass and at least one kind of 5-95 wt.% phytomass; and stirring the mixture, followed by crosslinking, homogenizing and drying. The woody biomass is a wood waste with a particle size of 25-60 mm. The phytomass is pretreated disintegrated straw packages, crushed and blended with natural moisture content. The method further comprise mixing an another kind of biomass which is grain, straw or sawdust shavings sawdust with a moisture content of 25% and particle size of 0.1-15 mm.    USE - The method is useful for preparing biomass mixture which is useful as a raw material for the pyrolysis process.
NOVELTY - The new type utility claims a middle pressure pipe net air inlet detection control system in marsh gas station, compressor group and pressure pipe network, the purification gas by a low pressure pipeline transmitting a compressor group, the compressor group through a high pressure pipe for purification gas transfer to medium-pressure pipe network, also have a pipeline and a PLC control cabinet, a pipeline respectively connected with the low pressure pipe and high pressure pipe, a connecting pipe and a high pressure pipe and a head mounted with a gate valve and the first modulator, a middle part pipe is mounted with the second modulator, a pipe connecting the oxygen content detecting instrument and methane content detecting device, said high pressure pipe equipped with a pneumatic valve and the diffusion device. The utility model is new type for depending a mass of air in that existing marsh gas station for quality of air inlet of a network management, resulting in no qualified marsh gas enter into a pressure pipe network of problem.
NOVELTY - The new type utility claims a different removing butane tower device, comprising supporting frame, comprising pedestal, a reaction kettle, a motor, a speed reducer, a stirring shaft, a locking ring, a heating tube. And the current technology compared to the different removing butane tower device, a heating pipe pedestal in the give quartz sand heating, again using heat conduction give the reactant in the reaction kettle by quartz sand, through motor drive rotating drive speed reducer rotating, again drive stirring shaft rotate by a speed reducer, a stirring shaft stirring make reaction, make the reactant is heated uniformly, the device structure design, strong function, uniform reaction, speed;
NOVELTY - The new type utility claims have one kind organic waste water treatment device, comprising internal tower is set with Anaerobic sludge, the tower body bottom connected the water inlet pipe for the treatment of the organic waste water, the tower body lumen along the vertical direction for at least two of the reaction room, the top of each of reaction room are provided with corresponding three phase separator, the three phase separator through lifting tube connected to the tower body top is equipped with gas-liquid separator, the gas-liquid separator connected with relux tube to tower body bottom, the tower body lumen up most layer set with water out pipe. The utility model is new type construction is simple, low cost, good economical efficiency, formed through the inner circulation of organic waste water and realize efficient, at the same time biogas generated by burner for burning, the production of heat also can be carry out heat can use to avoid direct discharge to cause pollute environment.
NOVELTY - The new type utility claims an upflow anaerobic biological filter bed reactor, comprising reactor main body, the following internal from the reactor main body is orderly upwards provided with biological mud bed area, biological mud suspension area, and marsh gas overflow out area, wherein, the reactor main body provided with biological mud circulation system at bottom of the biological sludge bed area, the mud suspension area provided with floating biological filler layer, the reactor main body provided with out water system at the top of the upper clarification area. The upflow Anaerobic biological filter bed reactor using biological mud circulation system optimizing to replace have existing technology and using the balance cloth water system, stirring device, and structure is complex sum lifting structure. Make sewage biological mud and full mixing, to obtain good mass transfer condition. And increase storage inventory for the Anaerobic biological fungus by equipped with floating filler layer in biological mud suspension area, thus it can effective increase and longer time maintain sewage treatment ability of Anaerobic biological filter bed flow reactor.
NOVELTY - The utility model is new type supply have one rotating bed pyrolysis furnace A and organic waste pyrolysis system, wherein, organic waste pyrolysis system comprising: crushing device, drying device, rotary bed pyrolysis furnace, pyrolysis solid processing device, cooling and purification device, the oil storage tank and heat accumulating type rotary heat exchanger, wherein, rotary pyrolysis furnace in bed can rotate and comprises, for containing the pyrolysis raw material is cloth plate, plate for rotating bed pyrolyzing furnace is divided into the distributing plate in the upper part of the pyrolysis chamber, and supply heat chamber under the cloth plate, wherein, upper cloth plate comprises multiple connected pyrolysis chamber of through hole and the supply heat chamber, regenerative rotary heat exchanger respectively connected and hot air inlet of cooling and purification device and rotary bed pyrolysis furnace. Thereby using the new type practical example of said organic waste pyrolysis system can be active of carrying out pyrolysis for organic waste.
NOVELTY - The utility model is new type provides one kind pyrogenation gastification furnace for life garbage sewage processing system, comprising raw material, raw material pre-treatment device, a pyrolysis furnace, oil water separating device, a water collection, coal cooling device, sewage primary purification device, comprehensive sewage treatment system, coal collection device, raw material connected with the raw material pre-processing device, raw material pre-processing device through pipeline connected with the pyrolysis furnace, raw material through pipeline connected with collecting basin, pyrolysis furnace and oil water separating device connected with the pyrolysis furnace by the discharging mouth connected with the pyrolysis coal cooling device, pyrolysis coal outlet connected with said sewage primary purification device. The new type utility claims the system, not only reducing have sewage device investment, simplify have technique process, at the same time but also saves have coke quenching water. Re-developing have absorbing function is pyrogenation gastification furnace for life garbage coal for processing pyrolysis for sewage, and not cause second time pollute, reach to have " to treat) the goal, effective method of treatment is pyrolysis and one sewage plant green and environment-friendly.
NOVELTY - The new type utility claims have one plant biomass forming fuel particle and preparation system, the utility model is new type of preparation system comprises raw material processing system, forming system and boiler system, a boiler system through high temperature steam pipe to the raw material processing system providing high temperature steam, the boiler system through high temperature air supply pipe to bake system providing high temperature smoke sum. The utility model is new type of system operation cost low, molding condition is mild, molding equipment loss small, heat can use rate high, the obtained molding fuel property is good.
NOVELTY - The boiler has a first furnace body connected with a second furnace body. A valve hopper is fixed with an air blower. The first furnace body is divided into a combustion chamber and a gasification room. A bottom part of the gasification room is provided with a ventilating mouth. The ventilating mouth is connected with the air blower that is fixed with a water tank. A top part of the gasification room is connected with the combustion chamber. The second furnace body is connected with an air inlet and air outlet of the first furnace body.    USE - Fluidization bed biomass multi-return air boiler.    ADVANTAGE - The boiler is simple in structure and convenient to use, and has high heat utilization rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a fluidization bed biomass multi-return air boiler.
NOVELTY - The apparatus has a grading condensing tower shell (1) that comprises a spiral water channel (11). The lower portion of condensing portion comprises overflow pipe connected to periphery of liquid product exit (6). A three level liquid product outlet (7) is set with periphery portion. The bottom of first-stage condensing section is set with grading condensing cooling water outlet (13). A spherical condensing tower is comprised with spherical condensing pipe which is set with spherical condensing pipe shell. The top end of spherical condensing pipe is set with condensing outlet (9).    USE - Biomass rapid thermal steam condensate fractionating apparatus.    ADVANTAGE - The blockage of the pipe is prevented, and low investment is ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the biomass rapid thermal steam condensate fractionating apparatus.    Grading condensing tower shell (1)    Liquid product exit (6)    Three level liquid product outlet (7)    Condensing outlet (9)    Spiral water channel (11)    Grading condensing cooling water outlet (13)
NOVELTY - The device has a furnace grate formed with an embedded bracket. Thickness of a fan-shaped double-arc surface structured furnace grate module is equal to diameter of a round disk. The furnace grate module and embedded pieces are inter-connected with each other. The fan-shaped double-arc surface structured furnace grate module is provided with a cloth outlet structure.    USE - Biomass gasification furnace combined grate mounting device.    ADVANTAGE - The device prevents generation of slag in an effective manner. The device has better ventilating effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification furnace combined grate mounting device.
NOVELTY - The apparatus (1) has a cell stack to which water steam electrolysis cells which have outer electrode layer (13) with perovskite type complex oxide containing lanthanum are connected. A first manifold (4) is arranged for supplying gas to water steam electrolysis cell. A second manifold (7) for recovering gas emitted from the water steam electrolysis cell. The distance between manifold with which high temperature gas flows, and outer electrode layer is longer than the distance of the other manifold with which gas with low temperature flows, and outer electrode layer.    USE - Water-vapor-electrolysis cell stack apparatus of electrolyzer (claimed).    ADVANTAGE - The distance between manifold with which gas with high temperature flows among the gas which flows through another manifold, and outer electrode layer is longer than the distance of the other manifold with which gas with low temperature flows, and outer electrode layer, so that the water-vapor-electrolysis cell stack apparatus can be improved with the hydrogen generation efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electrolyzer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of water-vapor-electrolysis cell stack apparatus.    Water-vapor-electrolysis cell stack apparatus (1)    Manifolds (4)    Outer electrode layer (13)    Inter-connector (14)    Support substrate (15)
NOVELTY - Producing ethanol using lignocellulosic raw material, involves (a) processing the lignocellulosic raw material with alkali, (b) performing solid-liquid separation of lignocellulose raw material, (c) making enzyme and microorganism to act on the solid content, and performing saccharification, performing fermentation by making the microorganism to act on liquid discharged from the saccharification process, and (d) performing second solid-liquid separation from suspension discharged from fermentation process.    USE - The method is useful for producing ethanol using lignocellulosic raw material (claimed).    ADVANTAGE - The method increases productivity of ethanol.    DETAILED DESCRIPTION - Method for producing ethanol using lignocellulosic raw material, involves (a) processing the lignocellulosic raw material with alkali, (b) performing solid-liquid separation using first solid-liquid separator for separating solid content and liquid content of lignocellulose raw material, (c) making enzyme and microorganism to act on the solid content, and performing saccharification, performing fermentation by making the microorganism to act on liquid discharged from the saccharification process, and (d) performing second solid-liquid separation to separate solid content and liquid content from suspension discharged from the fermentation process using second solid-liquid separator, circulating the lignocellulosic raw material through solid content separated using the second solid-liquid separation process, and performing saccharification and fermentation process.
NOVELTY - Activated charcoal production involves using iron salts as activating agents, such as ferric chloride, ferrous chloride, ferrous sulfate, ferric nitrate, iron oxalate or others without restricting. The iron salts are mixed with conventional activating agents selected from potassium hydroxide, sodium hydroxide, aluminum chloride, zinc chloride or hypophosphoric acid in different proportions.    USE - Method for producing activated charcoal for adsorption and removal of organic, inorganic or metallic contaminants in an aqueous medium and for use as catalysts support in various chemical reactions to environmental and industrial applications (all claimed).    ADVANTAGE - The method produces the activated charcoal in a simple manner with high specific surface area.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation depicting isotherm volume of the adsorbed nitrogen.
NOVELTY - Fluazuron and novaluron synthesis involves producing benzoylphenyl urea through synthesis route without using phosgene gas such as chlorine source in isocyanate compound formation. The benzoylphenyl urea is obtained by using oxalyl chloride, dimethyl carbonate or carbonyldimidazole as phosgene substitute. The purified benzoylphenyl urea and alcohols, acetates and esters are treated different ratios.    USE - Method for synthesizing fluazuron and novaluron for use in injectable drug formulations.    ADVANTAGE - The method synthesizes fluazuron and novaluron in a simple, cost-effective and eco-friendly manner without using phosgene gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic skeleton of the carbohydrate chitin. (Drawing includes non-English language text).
NOVELTY - Manufacture of carbon material (CC) involves physically-milling (BB) a carbon material formed by the covalent bonding of carbon atoms, increasing the distance between carbon contained in the carbon material by flowing a subcritical or supercritical fluid (AA) into the milled carbon material, and forming a functional group at the carbon material by reacting the milled carbon material with the subcritical or supercritical fluid.    USE - Manufacture of carbon material e.g. layered graphite, layered activated charcoal, carbon nanotubes, and amorphous carbon used for forming carbon material layer used as antistatic layer, filler for thermal-radiation product, and electrode material of secondary battery (all claimed).    ADVANTAGE - The method enables efficient manufacture of carbon material with high productivity and improved interlayer space, by fast process.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view explaining manufacture of carbon material.    Fluid supply unit (30)    Supercritical fluid (AA)    Milling of carbon material (BB)    Carbon material (CC)    Vent (DD)
NOVELTY - Use of exhaust gases heat for controlling amount of water injected into biogas specific content of methane, carbon dioxide and water, and increasing chemical energy of biogas produced from organic materials, is claimed. The device for increasing chemical energy of biogas produced from organic materials comprises biogas plant for reheating to the desired temperature, burner for reheating, pipe carrying amount of fuel, regulated valve controlled by signal-run lead with a controller, where the controller is based on the temperature of biogas.    USE - Exhaust gases heat for controlling amount of water injected into biogas specific content of methane, carbon dioxide and water, and increasing chemical energy of biogas produced from organic materials.    DETAILED DESCRIPTION - Use of exhaust gases heat for controlling amount of water injected into biogas specific content of methane, carbon dioxide and water, and increasing chemical energy of biogas produced from organic materials, is claimed. The device for increasing chemical energy of biogas produced from organic materials comprises biogas plant for reheating to the desired temperature, burner for reheating, pipe carrying amount of fuel, regulated valve controlled by signal-run lead with a controller, where the controller is based on the temperature of biogas, the method for increasing chemical energy of biogas produced from organic material is provided by adjusting amount of biogas fed into the burner through the valve of air quantity valve, controlling by the controller and supplying signal through the line.
NOVELTY - The utility model is new type relates to one plant farm sewage treatment circulation use system, comprising pigsty, piggery internal side provided with one of heating plate, another side set with moving defecation grate, moving defecation lower grate part set with urine temporary section by defecation and urine pipe and sewage pool connected with the sewage pool and regulating pool connected with the regulating pool respectively connected with marsh gas pool and sediment pool, marsh gas pool upper part provided with a boiler, a boiler by heating pipe and heating plate of each bottom connected with the sediment pool respectively pass transport slag pipe and field and pond connected with the sediment pool connected with clear water tank, a clear water tank and connected with the pigsty. The utility model is new type of beneficial effect is: can make the pig manure equal discharge object to use generating marsh gas, biogas residue so as to fish cultivating and planting vegetable and fruit, clean water recovery filter so as to wash the piggery, structure is simple, suitable, low cost, which can realize effective waste treatment in time, increase have economic benefit of pig farm, protection have pig surrounding environment.
NOVELTY - Producing compost, comprises (a) preparing powder composition by mixing mineral, zeolite and photocatalyst, and (b) fermenting by mixing livestock manure, powder composition and moisture controlling agent.    USE - The compost is useful for cultivating plant (claimed) and preventing bacteria.    ADVANTAGE - The compost kills harmful bacteria reduces odor generated from the composting process, increases disease resistance of the plants, promotes growth of plants, and is rich in minerals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for cultivating plant by fertilizing the compost.
NOVELTY - Treating nonylphenol and estrogen sludge involves adding nonylphenol and estrogen sludge into anaerobic reactor and then mixing to obtain mixture, where pH value of mixture is adjusted to 8-11. The mixture is fermented at 10-55 degrees C for 7-11 days to obtain fermented material.    USE - Method for treating nonylphenol and estrogen sludge (claimed).    ADVANTAGE - The method enables to treat nonylphenol and estrogen sludge that reduces nonylphenol and estrogen pollution.
NOVELTY - The device has a stove (1) connected with a purification room (6) through an air inlet pipe (2). The purification room is connected with a gasification furnace body (5). The air inlet pipe is fixed with an air outlet pipe (3). The air inlet pipe and the air outlet pipe are fixed with an upper control switch (4). The gasification furnace body is fixed with a handle (7). A lower end of the gasification furnace body is connected with an oxygen tube (9) that is connected with a fan (8). An upper part of the stove is arranged with an infrared network for distributing gas uniformly.    USE - Agricultural gasification furnace device.    ADVANTAGE - The device saves energy in an environment-friendly manner, and has simple structure and operation, high heating efficiency, better ventilating wind effect, large gasification furnace capacity and quick gas production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an agricultural gasification furnace device.    Stove (1)    Air inlet and outlet pipes (2, 3)    Upper control switch (4)    Gasification furnace body (5)    Purification room (6)    Handle (7)    Fan (8)    Oxygen tube (9)
NOVELTY - Fuel oil comprises 6-14 pts. kerosene, 20-40 pts. vegetable fats, 3-7 pts. vegetable oil acid, 10-16 pts. refined tar, 10-25 pts. methanol, 1-8 pts. surfactant, 5-15 pts. modifying additive, 85-95 pts. coal-oil slurry, 6-10 pts. lower ether, 0.1-1.0 pts. coking agent and 0.5-1.5 pts. emulsifier.    USE - Used as fuel oil.    ADVANTAGE - The preparation process is simple and suitable for producing high quality fuel oil, has good energy saving property, is environmentally-friendly. The fuel oil has strong adhesive force.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the fuel oil, comprising (a) taking a reactor with a stirrer, adding kerosene and vegetable fats, and completely mixing; (b) adding vegetable oil acid, refined tar and methanol into the reaction kettle, stirring and heating to 60-80 degrees C, for 2-4 hours; (c) cooling the reactor to 20-25 degrees C, adding coal-oil slurry and lower ether, stirring and allowing to stand for 5-10 hours; (d) pre-mixing the surfactant, modifying additive, coking agent and emulsifier to obtain mixing aid; and (e) removing the supernatant from step (c) adding the mixing aid, stirring thoroughly, to obtain the fuel oil, sealing and packaging.
NOVELTY - The new type utility claims have one vehicle A aqueous alcohol low temperature reforming hydrogen device, the theory is using vehicle engine waste heat for water containing alcohol through two level catalytic reforming for hydrogen-rich gas, again using hydrogen-rich gas into the vehicle engine and fuel mixture for combustion. The utility model is new type using two level honeycomb titanium network structure can produce large and catalyst contact surface area, which is good for the miniaturization of reforming hydrogen device, vehicle online producing hydrogen using the goal is maybe, structure of two grade catalytic implementation have catalyst and mutual synergistic effect, that have alcohol conversion efficiency using a single catalyst and hydrogen selectivity low equal problem, by mutual action of alkaline catalyst under in low temperature environment, have sintering and solves the problem of carbon catalyst, have increase using life of catalyst. The utility model is new type vehicle tail sum using waste heat, implement have goal of vehicle online doped hydrogen and increase combustion efficiency of fossil fuel, reducing emission of vehicle engine have harmful substance.
NOVELTY - The utility model is new type relates to one kind excrement treatment device, specifically livestock manure collection processing device, comprising spiral conveyor, a lifting device and fermentation tank, and the spiral conveyor with multi-number enter, one per port respectively enter and defecation outlet is connected with feeding room, the spiral conveyor end has the discharging mouth, the discharging mouth and lifting device connected with the lifting device and the box entrance connected with fermentation, the fermentation tank entrance has heating device. The utility model is new type supply of livestock manure collection processing device, through spiral conveyor for excrement of each one row of feeding room for automatically collecting, relieving have labour intensity, increase have efficiency of collection, the heating device on fermentation tank for waste by heating the fermentation time.
NOVELTY - The utility model claims a biogas circulating and indirect heating device using biomass, comprising pre-processing pool, marsh gas pool group, a biomass combustion furnace, the feedstock circulation pipe, circulation discharging pipe and discharging pipe, the marsh gas pool group comprising from front to rear in turn through material pipe connected in series connected with the marsh gas pool, marsh gas pool and pre-processing pool and the most material liquid through pipe connected with, each of marsh gas pool are respectively through one of the material pipe connected with circulation feedstock tube, on the tube equipped with material returning valve, circulation pipe feedstock material heating pipe is connected with the top end, a discharging mouth, circulation pipe and biogas pool discharging the circulation discharging pipe one end connected with material heating pipe and bottom end, another end connected with finally end up and provided with circulation pump, a discharging pipe end connected with a circulation discharging pipe on the circulation pump and biomass combustion furnace between upper, upper discharging pipe provided with the first switch valve. The utility model may increase marsh gas yield and full using biogas slurry circulation of biomass can indirectly heating device.
NOVELTY - A plastic biogas septic tank comprises first level fermentation tank (1), second level fermentation tank (2) and third level fermentation tank (3). The first level fermentation tank has feedstock (10). The third level fermentation tank has discharging mouth (8). The first level fermentation tank has side wall opened with first outlet. The second level fermentation tank has side wall with second entrance and second outlet.    USE - Plastic biogas septic tank.    ADVANTAGE - The tank has small volume, simple structure, and easy installation and cleaning set up.    DETAILED DESCRIPTION - Plastic biogas septic tank comprises first level fermentation tank (1), second level fermentation tank (2) and third level fermentation tank (3). The first level fermentation tank has feedstock (10). The third level fermentation tank has discharging mouth (8). The first level fermentation tank has side wall opened with first outlet. The second level fermentation tank has side wall with second entrance and second outlet. The third level fermentation tank has side wall with third entrance and third entrance connected. The second entrance height is not less than the first outlet height and the second outlet horizontal height is higher than the second entrance height. The third entrance height level is not lower than the second outlet height. The discharging mouth horizontal height is higher than the third entrance height.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the septic tank.    First level fermentation tank (1)    Second level fermentation tank (2)    Third level fermentation tank (3)    Discharging mouth (8)    Feedstock (10)
NOVELTY - The system has a bag-breaking sieving machine exit roller that is connected with a permanent magnetic separator inlet through a conveyor. The permanent magnetic separator outlet is connected with a machine inlet. A steam-type organic garbage disposal machine is connected with the inlet of a roller type drier whose outlet is connected with a cylinder scalping sieve inlet. A circular groove inner wall is provided with the hanging teeth. The outside wall of the rotating handle end portion is made with rotary shifting teeth.    USE - Fertilizer system with feed screw cap organic waste disposal machine.    ADVANTAGE - The fertilizer time is shortened. The garbage processing amount is large. The fertilizer effect is improved. The production is suitable with strong operability. The garbage pollute environment is avoided. The fertilizer system is featured with green and environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the fertilizer system with feed screw cap organic waste disposal machine. (Drawing includes non-English language text)
NOVELTY - The fertilizer system has pressure ejection device controller which is provided with movable rotary frame, horizontal air cylinder, vertical air cylinder, fluted disc, pneumatic actuator and teeth roller. The movable rotary frame is mounted on upper track in which a horizontal air cylinder and piston rod are fixed. The vertical air cylinder is fixedly installed on rotary frame through tray. The rotary air cylinder is arranged in vertical to piston rod corresponding to rotary frame mounted with pneumatic actuator for driving teeth roller.    USE - Fertilizer system for organic waste disposer.    ADVANTAGE - The rotary air cylinder is arranged in vertical to piston rod corresponding to rotary frame mounted with pneumatic actuator for driving teeth roller, such that the fertilizer time is shortened. The garbage processing amount is reduced. The fertilizer effect is ensured. The productivity and strong operability are attained. The pollution to environment is reduced. The environment friendly is attained.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fertilizer system. (Drawing includes non-English language text)
NOVELTY - The system has a bag-breaking sieving machine exit roller that is connected with a permanent magnetic separator inlet through a conveyor. The permanent magnetic separator outlet is connected with a machine inlet. A steam-type organic garbage disposal machine is connected with the inlet of a roller type drier whose outlet is connected with a cylinder scalping sieve inlet. The two ends of the discharge guide cylinder are respectively connected with superheated separator. The upper and lower sliding plates are fixed between supporting columns.    USE - Fertilizer system with steel dragon catapult organic waste disposal machine.    ADVANTAGE - The fertilizer time is shortened. The garbage processing amount is large. The fertilizer effect is improved. The production is suitable with strong operability. The garbage pollute environment is avoided. The fertilizer system is featured with green and environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the fertilizer system with steel dragon catapult organic waste disposal machine. (Drawing includes non-English language text)
NOVELTY - Fragrant biomass boiler fuel comprises 1000 pts. wheat straw, 860 pts. mud, 450 pts. hay, 400 pts. fallen leaves, 200 pts. anthracite, 10 pts. candle, 5 pts. cinnamon, 0.2 pts. jasmine essential oil and 0.3 pts. orchid oil.    USE - Used as fragrant biomass boiler fuel.    ADVANTAGE - The method is economical and reduces pollution to the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing fragrant biomass boiler fuel, comprising crushing the wheat straw, mud, hay, air-dried fallen leaves and anthracite, then adding candle and treating at 62-85 degrees C for 10-15 minutes, stirring, adding remaining materials, freezing at -25 to -35 degrees C, pressing into particle shaped finished product.
NOVELTY - Sewage sludge fuel strip comprises 58-62 pts. dehydrated sludge, 38-42 pts. straw, 0.04-0.06 pts. efficient plant grain and 0.006-0.008 pts. high potassium permanganate.    USE - Used as sewage sludge fuel strip.    ADVANTAGE - The sewage sludge fuel strip has improved combustion, is economical, has high heat efficiency, great economic and social benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the sewage sludge fuel strip, comprising (i) adding dehydrated sewage sludge into a mixer, adding 30 meshes crushed straw, efficient plant grain and high potassium permanganate, and stirring; and (ii) adding the mixture into molding machine, block molding, and drying.
NOVELTY - The new type utility claims cleaning device used for domestic sewage purification biogas pool, cleaning device comprising a machine body, a purification tank, the wind cover and a vulcanization absorbing device, the wind cover comprises a wind cover and a wind cover, a wind cover through locking mechanism connected with a wind cover, inner wind-collecting cover set inside with cleaning mechanism, cleaning mechanism comprises a plate and internal and joining platform, a machine body set up with display window, machine body set with the first electric engine and transmission storage tank set with biogas purification treatment pool and a vulcanization treatment pool, slag processing pool through air suction pipe connected with the cleaning machine, a vulcanization process pool set with overflow plate in a vulcanization absorbing device is set with the second internal electric machine, end part of a vulcanization absorbing device set with vulcanization hydrogen concentration sensor. The utility model is new type structure is simple, the practicability is strong, not only increase have cleaning efficiency of biogas residue, and can be for vulcanization of a gas in marsh gas pool for detection and absorption, increase have the safety when working.
NOVELTY - The utility model is new type category in compost facility construction technology field, relating to one kind of natural ventilated static state compost. It comprises layer board, ventilating layer,, compost material, the covering layer, is a layer board made bamboo chip woven strip and round panel, ventilating layer is circular layer of straw is formed by laying the, casing is made bamboo strip weaved piece type wall panel, the covering layer is decomposed sludge cover face, double layer board to block up and down in parallel set at lower part position, ventilating layer set at the interlayer position between two block layer board, surrounding wall is set with upper layer board on week edge location, compost material stack is upper layer board, surrounding the inner side position, cover layer cover for compost material upper surface position. The utility model is new type comprises following characteristics: facility construction is very simple and cost-saving, compost effect better and compost period is shortened.
NOVELTY - The utility model is new type category rural agricultural compost production equipment design matching technology field, relating to one kind compost burdening mixing stirring device matched. It comprises pedestal, mixing tank, stirring system, drive system, driving system, a discharging system, weigh system, pedestal is set with lower part position, mixing tank is set on location pedestal, stirring system is set with seat mixing tank and the inner side and the outside mixing box connected with drive system, driving system main side two platform motor, is equipped with side outside mixing box and main electric machine and drive system connected with, a secondary electric machine and discharging system connected with. The utility model is new type comprises following characteristics: device matched with complete, low investment cost is large, production capacity is strong, mixing uniformity is high, fit scale character compost operation use.
NOVELTY - Rapid degradation of 1,1-bis(p-chlorophenyl)-2,2,2-trichloroethane (DDT) comprises taking 20 mL vials with PTFE cap gasket, adding 30-50 mg microflaky/nano zerovalent iron and 1 mL 5 ppm DDT to each vial, vortex oscillating for 1-2 minutes, adding 0-100 mu L 1 M hydrochloric acid, performing thermostat shaking at 25 degrees C and 200-300 Hz for 5 minutes, repeating adding hydrochloric acid and performing thermostat shaking until end of reaction, adding 5 mL HPLC grade n-hexane, vortex oscillating for 2-3 minutes, performing stratification and collecting supernatant.    USE - Method for rapidly degrading 1,1-bis(p-chlorophenyl)-2,2,2-trichloroethane used in wastewater treatment (claimed).    ADVANTAGE - The method is simple, green and environment-friendly, does not use hazardous substances, and has low reaction temperature, large processing capacity, short processing time and inexpensive raw materials.
NOVELTY - Producing low-phosphorus containing fertilizer involves dissolving wastewater ammonium sulfate with phosphoric acid solution slurry, and then with potassium hydrogen sulfate slurry. Ammonia is added in the mixture and mixing in a tubular reactor to obtain material slurry. Urea and ammonium sulfate as solid material are added in material slurry, and then subjected to spray granulation and coating process.    USE - Method for producing low-phosphorus containing fertilizer (claimed).    ADVANTAGE - The method enables to produce low-phosphorus containing fertilizer in an eco-friendly manner.
NOVELTY - Producing compost involves utilizing 30-50% bio-organic fertilizer, 0-20% diammonium phosphate (60% content), 0-45% urea (41% content), 0-40% thio ternary compound fertilizer (48% content), 0-20% potassium dihydrogen phosphate.    USE - Method for producing compost used for planting peanut (claimed).    ADVANTAGE - The method enables to produce compost is eco-friendly, compost improves soil air permeability and soil plate structure, and ensures peanut root system growth.
NOVELTY - Preparing microbial fertilizer involves fermenting high-quality strains of seaweed in presence of microbes in acidic environment. The cell wall of seaweed is softened and ruptured by enzymes secreted by the microbes. The seaweed active ingredient are released.    USE - Method for preparing microbial fertilizer (claimed).    ADVANTAGE - The method enables to prepare microbial fertilizer that promotes root growth, reduces pests and disease, and provides cold and drought resistant ability, and ensures large scale production in short time, and simple, cost-effective and environment-friendly preparation.
NOVELTY - Preparing microbial fertilizer involves stirring 8.8% Bacillus thuringiensis, 43.2% potassium sulfate, 32.0% diammonium hydrogen phosphate and 11.0% additive uniformly.    USE - Method for preparing microbial fertilizer (claimed).    ADVANTAGE - The method enables to prepare microbial fertilizer that ensures soil improvement and green production in environment-friendly manner.
NOVELTY - Fertilizer comprises polyacrylamide, potassium fulvate, sodium nitrophenolate, Bacillus subtilis product and polyaspartic acid.    USE - Fertilizer.    ADVANTAGE - The fertilizer loosens soil plate and soil particle, and ensures no tillage or deep plowing.
NOVELTY - The machine has mixing chamber (12) whose upper portion is provided with garbage entrance. The lower portion of the mixing chamber is provided with the inner container (11). The bottom portion of the inner container is provided with a collection chamber (14) which is provided with leakage opening. The bottom portion of the inner container is adhered with a heating strip (17) which is provided with a temperature sensor. The inside of box portion (10) is set with bend stick (18) and mixing chamber which is connected with stirring motor (19).    USE - Kitchen waste fertilizing machine.    ADVANTAGE - The efficiency of the kitchen waste fertilizing machine is improved and the garbage processing cost is reduced. The kitchen waste fertilizing machine is environment friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for kitchen waste fertilizing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the kitchen waste fertilizing machine.    Box Portion (10)    Inner container (11)    Mixing chamber (12)    Collection chamber (14)    Heating strip (17)    Bend stick (18)    Stirring motor (19)
NOVELTY - The system has broken bag outlet that is connected with magnetic separator machine through conveyor. A permanent magnetic separator outlet is connected with winnowing machine. A steam catapult-type organic waste disposal machine is set with packing ejection device and controller. A guide tube is installed at lower portion of packing material ejection device. A steel cage is slidably mounted on steel cylinder holding pressure steam. A solid support column is mounted on periphery of opening between the sliding plates. The steel cage and discharge spout guide cylinder are matched.    USE - Fertilizer system.    ADVANTAGE - The fertilizer manufacturing time is shortened and waste disposal capacity is improved. The fertilizer efficiency and production are improved. The pollution of the environment by rubbish is prevented. The system is environment friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a block flow diagram of the fertilizer system. (Drawing includes non-English language text)
NOVELTY - Heating type organic fertilizer fermentation bed comprises fermentation bed (1), insulating plate (2), pipe (3), electric heating belt (4) and convex edge (5). The fermentation bed is set on floor is equipped with heating part. Insulating plate is set with pipe, which is connected with electric heating belt or hot water circulation. Rear edge of the fermentation bed is equipped with convex edge.    USE - Heating type organic fertilizer fermentation bed.    ADVANTAGE - The heating type organic fertilizer fermentation bed reduces fertilizer use, and environmental pollution caused by livestock manure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of heating type organic fertilizer fermentation bed.    Fermentation bed (1)    Insulating plate (2)    Pipe (3)    Electric heating belt (4)    Convex edge (5)
NOVELTY - Hypsizygus marmoreus culture medium waste is pulverized, to obtain pulverized granular media. The peanut shells with water content of 10-15% and straw in weight ratio of 1:1-1:1.2 are added to pulverized granular media, and biological-modulated. The obtained biomass fuel is stirred and mixed. The modulated biomass fuel is extruded with machine extrusion, to obtain biomass fuel.    USE - Production of biomass fuel (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly production of biomass fuel with high calorific value.
NOVELTY - Preparation of biodiesel oil comprises heating waste oil at 75-85 degrees C with vacuum degree of 15-20 KPa, adding concentrated sulfuric acid in methanol solution, placing mixture in reactor, carrying out esterification reaction at 50-64 degrees C until acid value reaches equilibrium, carrying out dealcoholation at 45-61 degrees C with vacuum degree of 10-35 KPa, adding methanol until acid value decreases to less than or equal to 2 mg potassium hydroxide/g, separating the upper layer by settling, adding sodium methoxide, carrying out transesterification reaction at 63-65 degrees C and refining to obtain biodiesel and byproduct glycerol.    USE - Method for preparing biodiesel oil (claimed).    ADVANTAGE - The method is energy-saving and has high production rate.
NOVELTY - A high-efficient fuel combustion-supporting agent contains 40-50 pts. wt. oleic acid ester, 10-14 pts. wt. polyether polyol, 18-20 pts. wt. isooctanol, 14-16 pts. wt. fatty acid amide, 8-10 pts. wt. Triethylamine, 3-5 pts. wt. di-iso-octyl-diphenylamine, 1-3 pts. wt. alkyl sulfonate and 6-8 pts. wt. methyl tert-butyl ether.    USE - High-efficient fuel combustion-supporting agent (claimed).    ADVANTAGE - The fuel combustion-supporting agent can be energy efficiently prepared with reduced emission and excellent burning effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of high-efficient fuel combustion-supporting agent, which involves mixing above raw materials and stirring for 3-6 minutes.
NOVELTY - The system has gas feed pipe stopper plates which are respectively formed between one end of annular pipe (30) and fermentation outlet tube (20), and between other end of annular pipe and feed pipe (10). A cloth bacteria device is comprised with an inter drainage cloth, cloth bacteria pipe, cloth bacteria hole, drain pipe and hydraulic connector. The cloth bacteria pipe is fixed within sidewall of annular pipe, while adapting shape of the annular pipe as same as cloth bacteria pipe. The cloth bacteria pipe is formed with several holes along vertical direction.    USE - Marsh gas fermentation system.    ADVANTAGE - The problem related to inadequate and poor liquidity strains caused by uneven distribution of the slurry is solved effectively, so that the fermentation efficiency is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the marsh gas fermentation system.    Feed pipe (10)    Fermentation outlet tube (20)    Annular pipe (30)    Discharge pipe (42)    Exhaust pipe (46)
NOVELTY - Method for preparing liposomes, involves homogenizing mixture of (a) water and (b) solution of at least one phospholipid and at least one water soluble solvent at 3000-20000 revolutions/minute (rpm), where the amount of lipid in the water-soluble solvents is 0.001-30 wt.%.    USE - The method is useful for preparing liposomes which is useful in personal care composition (claimed) having pharmaceutical, cosmetics and dermatological applications.    ADVANTAGE - The method prepares liposomes simply, rapidly conveniently and cost-effectively and is suitable for industrial production. The liposome is suitable for incorporating in both oil-soluble and water-soluble temperature sensitive actives and environmental friendly as it does not contains alcohol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for personal care composition which comprises the liposome which is prepared by the above-mentioned method, adjuvants, and active agents.
NOVELTY - The new type utility claims have one kind integrated full-automatic ecological septic tank, including sheet from winding composed of the cylinder, two cylinder end closeness connected with respectively provided with feces pipe and outlet pipe and end cover, inner cylinder by two clapboards divide into three of the whole area, and the three are in turn number is a precipitation zone, Anaerobic biochemical treatment area, sum pre-hanging slag area; the Anaerobic zone comprises connected for excrement and sink water pipe bending head, the biochemical treatment area including spiral wound hollow telescopic pole and chain filler, hollow telescopic pole over pole body set with air holes, inside pole body set with composite flora; in the soluble sum pre-hanging slag area set with bracket connected with cylinder bottom by the solution engine and sum for pre-hanging slag machine connected with the cylinder top part, corresponding to the hanging machine provided with slag discharge groove is connected with end cover. The utility model is new type by using septic tank is divided into a precipitation zone, Anaerobic biochemical treatment area, sum pre-hanging slag area of three are implementation have excrement, waste liquid solid-liquid separating, the waste liquid until, second time using the technology goal.
NOVELTY - The new type utility claims have one kind organic garbage aerobic composting device comprises compost material cabin, moving cover, motor, pore plate and rotating shaft, the pore plate and the rotating shaft are set in the compost material in storehouse, fine sieve plate and between the bottom of the compost material storehouse composed of air inlet buffer layer, the electrical machine mounted on the moving cover on the upper end of the rotary shaft and rotating end of the motor connected with the lower end of the rotation axis and center of said fine sieve plate fixedly connected with, the compost material chamber lower part inner wall is set with clamping slot base edge of the fine sieve plate card in annular groove of the clamping slot base inside. The utility model is new type for all organic garbage is applied to weight on pore plate on the motor drive through pore plate rotate, to organic garbage can be full of mixing and reaction, reaction efficiency is high and structure is simple.
NOVELTY - The new type utility claims one kind organic garbage have no ozone aerobic compost reactor, comprising compost material chamber, is set with moving cover compost material at the top part, wherein rotating shaft is set with internal compost material cabin, the first pore plate, the second pore plate and pore plate, third compost material cabin bottom set with liquid discharging pipe and sum for pipe, the side wall lower part set with discharging pipe, moving upper cover set with discharge pipe, rotary shaft vertical set and is through out of moving cover and compost material chamber, upper rotating shaft set with stirring teeth, the cabin wall and the cover body moving cover of fertilizer material chamber are as interlayer structure, are formed with insulating layer in stack interlayer of fertilizer material chamber and moving cover, between the first sieve plate pore and the second pore plate fill with odour adsorbent. And the utility model is new type of material reaction speed block, the discharging gas would not have smell, and suitable ventilating system connected to ensure lasting into outside air.
NOVELTY - The utility model is new type of organic fertilizer providing automatic turning device, comprising pedestal, main body, machine frame, turning mechanism, wheels, motor, handle, the hydraulic pressure control device, a far-near hydraulic pressure control device, video camera, electric control module, video frequency display device and remote control device. The utility model is new type can be full of know scene condition by video display equipment, and far-near control hydraulic pressure control device by remote control device and electric control module high and low hydraulic pressure control device, the operator realize far distance control the organic fertilizer automatic turning device.
NOVELTY - The new type utility claims photoelectric catalytic decomposing hydrogen production reaction analyzing detecting system, comprising photoelectric catalytic decomposing hydrogen production device and gas quantitative analysis detection system, photoelectric catalytic decomposing hydrogen production device comprises reactor, a jacket and cover, gas quantitative analysis detecting system comprises the vacuum pressure table, sum phase chromatography, vacuum pump, detecting the first gas inlet system and detection system the second air inlet, detecting the first gas inlet system and detection system the second air inlet respectively equipped with rotary cover and two side wall of the first air outlet and the second air outlet sealing connection. When in using process, product directly enter into gas phase chromatography for detecting sum. The utility model is new type of technology scheme can at the same time provide external voltage and illumination condition, structure is simple, the system volume is small, controllable temperature, suitable, and can constantly for monitoring the gas product.
NOVELTY - A foliar fertilizer comprises 20-30 pts. wt. animal bones and seaweed fermentation liquid, 5-8 pts. wt. amino acid, 10-15 pts. wt. nitrogen, phosphorus and potassium mixture, and 15-20 pts. wt. rice and wheat fermentation liquid.    USE - Foliar fertilizer.    ADVANTAGE - The fertilizer is rich in protein, vitamins and trace elements, can effectively improve soil structure and fertility, improves seedling rate, improves quality of crops, and has simple preparation and promoting effect on rapid development and growth of plant roots.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer comprising mixing raw materials, uniformly stirring, reacting to below 30-40 degrees C for 1-3 days under sealed environment, stirring uniformly, and drying.
NOVELTY - Foliar fertilizer comprises 15-20 parts fermented product and leaves of spinach, 8-10 parts manganese sulfate, 6-8 parts fulvic acid, 10-12 parts calcium sulfate, and 3-5 parts titanium pigment.    USE - The foliar fertilizer is useful for controlling blight, and bacterial wilt.    ADVANTAGE - The foliar fertilizer is prepared rapidly, and recovers growth of plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned foliar fertilizer, which involves preparing and drying the fermented product and leaves of spinach, adding remaining materials to the dried product, uniformly stirring the mixture, reacting the mixture for 3-5 days in sealed environment and maintaining the reacted mixture at 20-30 degrees C.
NOVELTY - A wheat composite fertilizer comprises 40-60 wt.% wheat straw fermentation product, 35-40 wt.% sawdust fermentation product, 4-5 wt.% ammonium phosphate, 3-5 wt.% potassium sulfate, and 3-4 wt.% nitrogen fertilizer.    USE - Wheat composite fertilizer.    ADVANTAGE - The composite fertilizer is environment-friendly and rich in lignin, cellulose, hemicellulose and mineral substance needed for growth of crops, saves cost, increases yield of crops to 5-15%, and has complete organic matter content and adequate nutrient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite fertilizer comprising mixing raw materials, uniformly stirring, reacting to 30-40 degrees C for 30-40 minutes, drying until it is 80% dry, and grinding into powder or mechanically grinding into powder.
NOVELTY - Foliar fertilizer formulation comprises 30-40% water, 23-30% rotten vegetable leaves, 20-30% plant ash, 15-20% biogas liquid diluent, 5-10% aqueous solution of rare earth fertilizer, and auxiliary agent (required amount).    USE - As foliar fertilizer formulation for cabbage leaf (claimed). The foliar fertilizer formulation is useful for increasing insect resistance, drought resistance and disease resistance of plant, and promoting plant growth.    ADVANTAGE - The foliar fertilizer formulation provides phosphorous, calcium, iron, magnesium and sulfur, and is rich in nutrients and cost-effective to prepare.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the foliar fertilizer formulation, which involves crushing rotten vegetable leaves and plant ash to obtain slurry, diluting the slurry, performing fermentation in a cylinder at 20-30 degrees C for 10-20 days, then adding remaining materials, stirring added materials, and performing fermentation at 60-80 degrees C for 3-5 minutes.
NOVELTY - Preparing amino acid microbial organic fertilizer comprises taking animal and plant protein raw material and 95% sulfuric acid aqueous solution mixture, hydrolyzing, adding ammonium bicarbonate, filtering, collecting the filtrate to obtain amino acid liquid, uniformly mixing urea, calcium superphosphate, diammonium phosphate, magnesium sulfate and zinc sulfate, crushing to obtain inorganic fertilizer, mixing amino acid liquid and inorganic fertilizer to obtain complex amino acid liquid, adding complex microbial inoculum, mixing, freeze-drying, adding organic fertilizer and mixing uniformly.    USE - The method is useful for preparing amino acid microbial organic fertilizer (claimed).    ADVANTAGE - The fertilizer: is economical; has high bioavailability; has simple preparation method; is prepared into powder, which is easy to store; ensures stable bioactivity of amino acid and microbial inoculum; is diluted with water for application; promotes the growth of beneficial microorganisms; and promotes crop growth.    DETAILED DESCRIPTION - Preparing amino acid microbial organic fertilizer comprises (a) taking animal and plant protein raw material and 95% sulfuric acid aqueous solution mixture in a mass ratio of 1:1-2, hydrolyzing at 80-90 degrees C for 12-48 hours, adding ammonium bicarbonate to adjust the pH to 3-6, filtering, collecting the filtrate to obtain amino acid liquid, (b) taking 5-15 pts. wt. urea, 5-10 pts. wt. calcium superphosphate, 1-10 pts. wt. diammonium phosphate, 1-10 pts. wt. magnesium sulfate, 1-10 pts. wt. zinc sulfate, mixing uniformly, crushing to 50-100 meshes to obtain inorganic fertilizer, (c) uniformly mixing amino acid liquid and 30-60 pts. wt. inorganic fertilizer to obtain complex amino acid liquid, (d) adding 5-20 pts. wt. complex microbial inoculum, uniformly mixing, freeze-drying to obtain complex microbial inoculum and amino acid powder, and (e) adding 30-60 pts. wt. organic fertilizer, and mixing uniformly.
NOVELTY - Bio organic fertilizer comprises 20-30 pts. wt. edible fungus residues, 10-20 pts. wt. stone powder, 30-50 pts. wt. sandysoil, 1-3 pts. wt. liquid probiotics, 15-20 pts. wt. swill, 5-10 pts. wt. charcoal powder and 3-5 pts. wt. sulfur powder.    USE - The bio organic fertilizer is useful for preventing rotting of cactus (claimed).    ADVANTAGE - The fertilizer: improves soil conditions; activates soil microbial activity rate; overcomes soil hardening by increasing soil air permeability; and absorbs excess soil moisture.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing fertilizer comprising adding liquid probiotics and swill after diluting the material, stirring uniformly, placing into the pit, sealing, carrying out anaerobic fermentation for 8-10 days in summer or 15-30 days in winter, observing appearance of alcohol, which denotes successful completion of fermentation, removing from the pits, drying, crushing and packing or can be used directly.
NOVELTY - Microbial amino acids fertilizer comprises 30-60 pts. wt. hydrolytic activity amino acid liquid, 5-20 pts. wt. composite microbial inoculum, 30-60 pts. wt. organic fertilizer, 5-15 pts. wt. urea, 5-10 pts. wt. calcium superphosphate, 1-10 pts. wt. diammonium phosphate, 1-10 pts. wt. magnesium sulfate and 1-10 pts. wt. zinc sulfate.    USE - Used as microbial amino acids fertilizer.    ADVANTAGE - The fertilizer has high bioavailability of amino acids, which promotes health thrive and crop production.
NOVELTY - Preparing microbial fertilizer composition, comprises mixing rooting powder, industrial slag, industrial and agricultural waste, and industrial waste strain, and fermenting; where the industrial slag includes gypsum, weathered coal and phosphorus slag; and the industrial and agricultural waste includes crop residues, weeds, lees, peanut shell powder and shell powder.    USE - The microbial fertilizer composition is useful for promoting maize crop rooting (claimed).    ADVANTAGE - The method has low production cost, does not require fermentation equipment, realizes natural fermentation. The fertilizer increases the rooting number, root length, root diameter and yield of maize crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for microbial fertilizer composition, prepared as mentioned above.
NOVELTY - The system has a double-spiral feeder (1) whose end is fixed with a large inclination conveyer (2) for lifting materials. An output end of the large inclination conveyer is provided with a raw material distribution belt conveyor (3) and an electric three-way distributor. Multiple strips are arranged under the belt conveyor in a parallel manner. Multiple cyclone separators (7) are connected with a summarizing bag-type dust remover (14). Three platforms are arranged at a gas-liquid separator (9). An electrical tar precipitator (10) is connected with a fuel gas input storage tank (11).    USE - Biomass sum parallel production system for use in a biomass gas industry.    ADVANTAGE - The system utilizes multiple sum furnaces to be collective gas platforms in a parallel manner and a purification system delivery system to realize optimal mutually production equipment configuration process and reduce production equipment idle time consumption, thus ensuring management production performance and saving integration labor resources. The system is environment-friendly, and has high productivity. The system avoids local device operation influencing phenomenon when fault service is occurred in a local device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass sum parallel production system.    Double-spiral feeder (1)    Large inclination conveyer (2)    Raw material distribution belt conveyor (3)    Cyclone separators (7)    Gas-liquid separator (9)    Electrical tar precipitator (10)    Fuel gas input storage tank (11)    Summarizing bag-type dust remover (14)
NOVELTY - Sludge bioorganic fertilizer comprises 40-50 pts. wt. pond sludge, 30-50 pts. wt. cow and horse manure, 20-30 pts. wt. plant straw, 10-20 pts. wt. tea residue, 15-20 pts. wt. wheat bran and 3-5 pts. wt. decomposing inoculant.    USE - Used as sludge bioorganic fertilizer.    ADVANTAGE - The fertilizer: has high organic substances content; is economical; utilizes pond sludge, which has high water content and organic substances that are easy to decompose; has small particle size; can regulate characteristics of soil; and comprises tea residue and horse manure, which further increases soil nutrients.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparation of the fertilizer, comprising crushing the raw material expect adding decomposition inoculant, uniformly mixing, sealing, fermenting for 2-3 months at 20-30 degrees C, adding white vinegar to accelerate the fermentation, and digging out of the cellar, high temperature sterilizing and crushing into particles.
NOVELTY - Preparation of special microorganism fertilizer comprises mixing Lactobacillus plantarum, yeast and antibiotic bacteria at mass ratio of 1-5:1-5:2-3 to obtain mixed bacteria composite; mixing rice straw or weed, crop straw and rapeseed meal at mass ratio of 1-3:4-5:2-3 and adding water to form 30-70 wt.% solid content of mixture as fermentation substrate; mixing with 0.5-2 wt.% mixed bacteria composite and fermenting at 35-42 degrees C; and filtering using 0.2 mu m membrane filter, collecting resulting solid, and drying.    USE - Method for preparing special microorganism fertilizer used for vegetable (claimed).    ADVANTAGE - The fertilizer has dual fertilizer effect and can process organic waste.
NOVELTY - Microbial fermented organic fertilizer comprises corn straw and complex microbial agent, where the complex microbial agent includes Bacillus subtilis, Bacillus megaterium, Bacillus licheniformis, Bacillus cereus, Bacillus mucilaginosus, Lactobacillus plantarum and yeast mixture.    USE - The organic fertilizer is useful for corn straw (claimed).    ADVANTAGE - The organic fertilizer is environmentally-friendly, increases soil organic matter, improves soil fertility, has reduced dosage amount and achieves waste disposal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the microbial fermented organic fertilizer, comprising:(i) crushing the corn straw in crusher to a particle size of 80-200 meshes; (ii) adding crushed corn straw into water, mixing, controlling corn straw moisture to 30-50%; (iii) adding step (ii) corn straw into complex microbial agent, uniformly mixing, incubating at 30-50 degrees C for 10-15 days, decomposing straw and drying.
NOVELTY - Biological fertilizer comprises 5-20 pts. wt. hydrolyzed active polypeptide, 10-20 pts. wt. complex microbial inoculants, 40-50 pts. wt. peat, and 20-30 pts. wt. inorganic additive. The hydrolyzed active polypeptide is prepared by mixing soybean meal and aqueous sulfuric acid at mass ratio of 1:2, hydrolyzing at 80-90 degrees C for 24-48 hours, adding ammonium bicarbonate, adjusting pH to 2-5, filtering, concentrated filtrate, freeze-drying.    USE - Biological fertilizer used for organic Chinese cabbage (claimed).    ADVANTAGE - The fertilizer has low cost, promotes healthy living of organism, and increases microbial effect and Chinese cabbage production.
NOVELTY - Fertilizer comprises fermented liquid of fruit, urea, amino acids, weathered coal and potassium hydroxide in weight ratio of 15:8:5:3:0.8.    USE - As fertilizer for fruit trees (claimed).    ADVANTAGE - The fertilizer is stable, produced simply, and cost-effective, improves soil structure, and increases yield and quality of fruits.
NOVELTY - A wheat special fertilizer comprises soybean cake ferment, urea, plant ash, humic acid and potassium fertilizer at weight ratio of 35:20:12:5:3.    USE - Wheat special fertilizer.    ADVANTAGE - The special fertilizer provides best proportion of nutrient elements needed for fast growth of wheat, can make wheat to quickly absorb soil nutrients, increases yield of wheat, and has simple process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of wheat special fertilizer comprising mixing raw materials, crushing, high-temperature sterilizing, putting in granulator, granulating to 5-10 degrees C, and condensing.
NOVELTY - Preparation of an agrochemical active ingredient, comprises reacting a carboxylic acid agrochemical active ingredient having a carboxylic acid group with alkyl ether of ethoxylated alkanolamine, in presence of a solvent, to produce a salt of carboxylic acid agrochemical active ingredient with alkyl ether of ethoxylated alkanolamine.    USE - The process is useful for preparing agrochemical active ingredient which is useful in agriculture and horticulture (claimed) and as herbicide, pesticide, fungicide, weed killer, plant health agent or plant growth regulator. The ability of the agrochemical active ingredient to control weed to was tested in narrow leaf weed in direct seeded rice using in vitro assay. The results showed that agrochemical active ingredient (comprised of quarternary salt of bispyribac acid with lauryl ether of ethoxylated dimethylethanolamine) exhibited 90% weed control.    ADVANTAGE - The process: provides agrochemical active ingredient with improved wettability and water solubility in an economical manner; provides active ingredient with reduced use of auxiliary chemicals or adjuvants for application in agriculture or horticulture which makes the agrochemical cost effective; and is ecologically safe.
NOVELTY - The device has a left conduit (22) that is connected between the fermentation pipeline and the feeding pipes (42). A right conduit (24) is connected between the fermentation pipeline and the discharge pipes (44). The left and right conduits are set on the fermentation pipeline such that the slurry flows into a one-way check valve. A front conduit (32) is connected between the fermentation pipelines and provided with a one-way pressure control valve such that slurry flows into the fermentation pipelines.    USE - Device for promoting multistage barometric disturbance fermentation for use in biogas system.    ADVANTAGE - The biogas stirring drive and uniform distribution of strain are effectively promoted, and the fermentation efficiency is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the perspective view of the device for promoting multistage barometric disturbance fermentation.    Left conduit (22)    Right conduit (24)    Front conduit (32)    Feeding pipes (42)    Discharge pipes (44)
NOVELTY - Tedizolid preparation involves reacting amine compound (I) with chloroformate to give benzyloxy carbamate compound (II). The benzyloxy carbamate compound (II) is reacted with isopropyl acetate to give boron hydroxide compound (III). The obtained boron hydroxide compound (III) is treated with coupling reaction to give cynate compound (IV). The obtained cynate compound (IV) is treated with glycidyl acetic acid to give hydroxy compound (V).    USE - Method for preparing amine tedizolid (claimed).    ADVANTAGE - The method for preparing amine tedizolid in a simple and eco-friendly manner under on industrial scale under mild reaction condition.    DETAILED DESCRIPTION - Tedizolid preparation involves reacting amine compound of formula (I) with chloroformate to give benzyloxy carbamate compound of formula (II). The benzyloxy carbamate compound of formula (II) is reacted with isopropyl acetate to give boron hydroxide compound of formula (III). The obtained boron hydroxide compound of formula (III) is treated with coupling reaction to give cynate compound of formula (IV). The obtained cynate compound of formula (IV) is treated with glycidyl acetic acid to give hydroxy compound of formula (V), which is reacted with azide to give the finished tedizolid compound.
NOVELTY - The multifunctional system comprises a device (1), an aromatization reactor (2), a quench tower (3), separation towers (4,5,6), a separation unit (9), and a reactor. The propylene reactor is provided for conversion of ethylene as main product. The hydrocarbon and separation tower are provided for obtaining state hydrocarbon into separation unit for separating hydrogen, methane, ethylene, ethane, propylene or propane.    USE - Multifunctional system for preparing ethylene, propylene and aromatic hydrocarbon.    ADVANTAGE - The multifunctional system can be prepared in a simple manner with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing multifunctional system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the multifunctional system for preparing ethylene, propylene and aromatic hydrocarbon.    Device (1)    Aromatization reactor (2)    Quench tower (3)    Separation towers (4,5,6)    Separation unit (9)
NOVELTY - Cultivation bag comprises lower layer matrix, microbial agent and upper layer matrix (from bottom to top). The matrix 200 mg/kg nitrogen, 20 mg/kg phosphorous, 200 mg/kg potassium, 100 mg/kg magnesium, 5 mg/kg zinc, 5 mg/kg copper, and perlite and river sand (remainder). The weight ratio of the perlite and river sand is 1:4. The microbial agent is Glomus intraradices strain BEG141.    USE - The bag is useful for cultivating sweet potato seedling (claimed).    ADVANTAGE - The method reduces usage of fertilizer, enables retention of nutritional components of soil, and is performed cost-effectively, and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for cultivating sweet potato seedling, which involves mixing the G.intraradices strain BEG141 with sand, stirring obtained mixture, inoculating 10 weight/weight% mixture in composition comprising corn and clover, maintaining temperature at 25-35 degrees C and relative humidity at 60%, providing illumination for 14-16 hours/day, pouring water once for every 2-3 days, adding Hoagland nutrient liquid once for every week, and harvesting the seedling.
NOVELTY - Preparing matrix involves pulverizing corn straw to obtain powder of particle size less than or equal to 3 mm. Obtained powder is mixed with edible fungus and bran in a ratio of 2:1 with stirring. Cassava residue is mixed with extracting solvent in a ratio of 1:2 for extraction. Obtained extract is centrifuged, and dried to reduce moisture content to 13-15%. Both the obtained products, and vermiculite (5-8%), and microbial agents (2-4%) are mixed for fermentation for 28-30 days. Fermented material is mixed with fertilizer (2-3%) of silicon, calcium and magnesium for 20-25 minutes to obtain final product.    USE - Method for preparing matrix used for soilless cultivation of wheat (claimed).    ADVANTAGE - The method enables to prepare matrix which ensures balanced supply of nutrient to crop, and improved disease resistance of crop.
NOVELTY - Fumigant comprises traditional Chinese medicinal composition. The traditional Chinese medicinal composition comprises 50-70 pts. wt. folium artemisiae argyi, 3-5 pts. wt. radix isatidis, 3-5 pts. wt. plantain seed, 5-10 pts. wt. rhizoma atractylodis, 5-10 pts. wt. Forsythia, 5-10 pts. wt. clove, 3-5 pts. wt. radix scutellariae, and 3-5 pts. wt. radix asteris.    USE - The fumigant is useful for repelling mosquitoes and flies in chicken coop (claimed).    ADVANTAGE - The fumigant is nontoxic, environmentally-friendly and prepared simply and cost-effectively, leaves no residues, and causes no side effects.    DETAILED DESCRIPTION - method for preparing the fumigant, which involves (a) cleaning and drying the above-mentioned components, respectively crushing dried components, and sieving obtained powders using sieve having 65 mesh size, and (b) mixing the powders using mixer to obtain product.
NOVELTY - Refining and purifying oxiracetam comprises adding oxiracetam crude product with methanol to reflux and dissolve, adding activated coal to continuously reflux and dissolve for 0.5-2 hours, filtering when it is hot, washing filter cake with hot methanol, combining the washing liquid and filter liquor, concentrating under reduced pressure, stirring at -5?Oc to 0 degrees C for separating out white crystal oxiracetam primary refined product, adding the primary product with methanol, and repeatedly refining to obtain oxiracetam with more than 99% purity and less than 0.1% single impurity content.    USE - The method is useful for refining and purifying oxiracetam (claimed).    ADVANTAGE - The method: has mild conditions, simple operation and low cost; can recycle the solvent; and is suitable for large-scale industrial production.
NOVELTY - A biomass briquette comprises 50-60 wt.% raw coal powder, 30-40 wt.% of biomass dry powder, 5-7 wt.% clinker powder, 2.4-4.8 wt.% clay powder and 0.2-0.6 wt.% coal burning additive. The coal additive comprises 2-8 wt. manganese dioxide, 8-22 wt.% ferrocene, 22-50 wt.% barium nitrate, 3-15 wt.% sodium nitrate, 6-20 wt.% potassium nitrate, 6-24 wt.% potassium chlorate, 0.3-1.2 wt.% calcium chloride, and 1.8-15.75 wt.% industrial salt.    USE - Biomass briquette.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the biomass briquette comprising mixing the raw materials, mold pressing and forming, and cold pressing and forming at 20-35 degrees C.
NOVELTY - A domestic waste degradation device comprises housing (1), upper hopper (4) at top of housing, and hopper cover. Degradation tank, heat insulation layer, equipment installation chamber, humidity sensor, temperature sensor, deodorizing device, discharge pump, crushing device and stirring device are arranged in the housing. The front side of housing is provided with degradation product outlet (19) matched with side cover, control room (14), and automatic waste conveying device (2). Programmable logic controller control chip and corresponding control button are arranged in control room.    USE - Domestic waste degradation device.    ADVANTAGE - The device allows for more effective and environment-friendly conversion of kitchen waste into organic fertilizer.    DETAILED DESCRIPTION - A domestic waste degradation device comprises housing (1), upper hopper (4) at top of housing, and hopper cover. Degradation tank, heat insulation layer, equipment installation chamber, humidity sensor, temperature sensor, deodorizing device, discharge pump, crushing device and stirring device are arranged in the housing. The stirring device comprises first motor connected to stirring shaft through a chain. The stirring shaft is fixed with stirring rod. The front side of housing is provided with a degradation product outlet (19) matched with side cover, a control room (14), and an automatic waste conveying device (2). Programmable logic controller control chip and corresponding control button are arranged in control room.    DESCRIPTION OF DRAWING(S) - The drawing shows a three-dimensional view of domestic waste degradation device.    Housing (1)    Automatic waste conveying device (2)    Upper hopper (4)    Control room (14)    Degradation product outlet (19)
NOVELTY - Preparing cultivation material involves drying and crushing 65-75% tree material, 12-16% bagasse, 10% rice bran, 3-4% mushroom, 1.5% lime and 1% gypsum. The dried product is fermented by soaking with clean water (20-30 times) at low temperature for 18-24 hours, and then covered with tarpaulin to carry out natural fermentation at 60 degrees C for 24 hours. The fermented product is placed into polyethylene bag having width of 15 cm, length is 60 cm and thickness is 0.04 mm. Auricularia polytricha is introduced in perforated polyethylene bag, and then kept in dark room.    USE - Method for preparing cultivation material for planting Auricularia polytricha (claimed).    ADVANTAGE - The method is eco-friendly, saves labor cost and coal resource, and enables to prepare cultivation material and plantation of Auricularia polytricha in low carbon environment.    DETAILED DESCRIPTION - Preparing cultivation material involves drying and crushing 65-75% tree material, 12-16% bagasse, 10% rice bran, 3-4% mushroom, 1.5% lime and 1% gypsum. The dried product is fermented by soaking with clean water (20-30 times) at low temperature for 18-24 hours, and then covered with tarpaulin to carry out natural fermentation at 60 degrees C for 24 hours. The fermented product is placed into polyethylene bag having width of 15 cm, length is 60 cm and thickness is 0.04 mm. Auricularia polytricha is introduced in perforated polyethylene bag, and then kept in dark room, where bacterial growth occur. The dark room temperature is controlled at 20-22 degrees C and humidity at 60-75%.
NOVELTY - Lightweight container seedling cultivation matrix comprises Flammulina velutipes residue, peat and chaff in volume ratio of 2-4: 3-5: 2-4, where amount of nitrogen, phosphorus and potassium is 1.5-2.5kg/m3. Lightweight container seedling cultivation matrix is prepared by drying and sieving Flammulina velutipes residue and then mixing remaining components. The mixture is fermented by using a mushroom planting matrix. Mushroom planting matrix comprises 40-50 wt.% corn core, 10-20 wt.% bran, 8-10 wt.% cottonseed hull, 20-30 wt.% rice bran and 0.1-0-3 wt.% calcium carbonate.    USE - Lightweight container seedling cultivation matrix.    ADVANTAGE - The lightweight container seedling cultivation matrix is cost-effective, and easy to operate, improves container seedling quality, replaces grass peat, and reduces amount of peat from 60% to 36-42%.    DETAILED DESCRIPTION - Lightweight container seedling cultivation matrix comprises Flammulina velutipes residue, peat and chaff in volume ratio of 2-4: 3-5: 2-4, where amount of nitrogen, phosphorus and potassium is 1.5-2.5kg/m3. Lightweight container seedling cultivation matrix is prepared by drying and sieving Flammulina velutipes residue and then mixing remaining components. The mixture is fermented by using a mushroom planting matrix. Mushroom planting matrix comprises 40-50 wt.% corn core, 10-20 wt.% bran, 8-10 wt.% cottonseed hull, 20-30 wt.% rice bran, 0.1-0-3 wt.% calcium carbonate and 0.1-0.5 wt.% lime.
NOVELTY - Compound fertilizer comprises 35-40 pts. wt. wheat straw stick, 26-30 pts. wt. cattle and sheep excrement, 2-3 pts. wt. Celastrus angulatus vine, 8-10 pts. wt. fructus cnidii selinum, 2-3 pts. wt. herba houttuyniae, 5-8 pts. wt. yam, 9-10 pts. wt. pomegranate rind, 6-7 pts. wt. radix isatidis, 4-5 pts. wt. Acanthopanax, 8-10 pts. wt. pseudoginseng, 4-5 pts. wt. garlic, 1-3 pts. wt. camphor, 1-4 pts. wt. folium artemisiae argyi and 6-10 pts. wt. dried orange peel.    USE - Compound fertilizer used preventing and treating blight of lily (claimed).    ADVANTAGE - The compound fertilizer is nutritious, eco-friendly and cost-effective, and has wide industrial applicability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing compound fertilizer, which involves:    (A) crushing components to obtain powder and then leaching with water (5 times) for 2 hours;    (B) extracting the soaked product for 1 hour and filtering to obtain filter liquid and residue;    (C) extracting residue by soaking with water (2 times) for 1 hour and filtering obtain other filter liquid;    (D) combining the filter liquids to obtain medicinal liquid;    (E) crushing wheat straw and mixing cattle and sheep excrement in a fermentation pool to carry out fermentation at room temperature for 20 days; and    (F) spraying the medicinal liquid on fermented product, drying it by using a drier, and then crushing to obtain final product.
NOVELTY - Organic fertilizer comprises 30-50% human and animal excreta, 20% plant ash, 5% bean dregs, 20-30% corn straw powder, 10% lignite and 1-3% organic phosphorus compound.    USE - The organic fertilizer is useful for potato plant.    ADVANTAGE - The fertilizer provides nutrition to potato plant by increasing its yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing organic fertilizer, comprising mixing all raw materials (except organic phosphorus compound), adding proper amount of water, fermenting at 30-40 degrees C for 6-8 days, adding organic phosphorus compound, stirring uniformly, drying, pelletizing and administered on potato plant during intermediate growing stage.
NOVELTY - Organic fertilizer comprises chicken manure, duck manure, sludge, kelp, phosphate fertilizer, and potash fertilizer according to the ratio of 5:3:2:1:2.5:2.    USE - The fertilizer is used for increasing plant cold resistant and drought-resistant ability.    ADVANTAGE - The fertilizer has strong fertility, supplements plant nutrition, can improve the soil characteristic, makes soil more fertile, can make plant stem tough, ensures bud formation, large bright color flower, and fruit precocious puberty, develops plant growth and.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing organic fertilizer comprising taking chicken manure, duck manure, sludge, and kelp, stirring uniformly, fermenting for 8-10 days in sealed environment, placing for 40-60 minutes raw material in environment of 60-80 degrees C, adding phosphate fertilizer and potash fertilizer, stirring uniformly, compressing using a compressor to obtain particle.
NOVELTY - Preparing potted plant nutrient soil comprises e.g. taking leaf mold, garden soil, river sand, active microorganism, pine needle, bone powder and liquorice, and mixing uniformly, adding raw materials in a sealing tank and fermenting at 50-60 degrees C, adding hulled rice husk ash in obtained product and mixing uniformly, adjusting pH value of mixed substrate to be 6.5-6.8, adding phosphate fertilizer, and potash fertilizer in obtained product, stirring uniformly, sterilizing product, and smashing product, sieving to product with particle diameter of 2-3 cm, and obtaining the potted nutritional soil.    USE - The method is useful for preparing potted plant nutrient soil (claimed).    ADVANTAGE - The method has simple operation, and saves time and labor force. The nutrition soil can be directly added for improving flower growth, has high nutrient value, is rich in calcium, phosphorus and other minerals, and continuously supplies nutrition.    DETAILED DESCRIPTION - Preparing potted plant nutrient soil comprises (i) configuring potted plant nutrient soil: taking raw material 50-70 pts. wt. leaf mold, 30-50 pts. wt. garden soil, 5-10 pts. wt. river sand, 2-5 pts. wt. active microorganism, 5-10 pts. wt. pine needle, 5-15 pts. wt. bone powder, and 0.5-1.2 pts. wt. liquorice, and mixing uniformly, (ii) adding step (i) raw materials in a sealing tank and fermenting at 50-60 degrees C, (iii) adding less amount of 5-8 pts. wt. hulled rice husk ash in step (ii) obtained product and mixing uniformly, adjusting pH value of mixed substrate to be 6.5-6.8, (iv) adding 3-5 pts. wt. phosphate fertilizer, and 1-3 pts. wt. potash fertilizer in step (iii) obtained product, and stirring uniformly, (v) sterilizing step (iv) obtained product, and (vi) taking step (v) obtained product and smashing, sieving to product with particle diameter of 2-3 cm, and obtaining the potted nutritional soil.
NOVELTY - Organic fertilizer composition, comprises chicken manure, corn stalk, gluconate and tartaric acid, organic phosphorus compound and hydrogen peroxide in the weight ratio of 5:2:0.8-1:1:0.025.    USE - The composition is useful for preventing plant pests (claimed), eliminating stomach poisoning, and inhibiting cholinesterase for delaying neurotransmission, spasm, and movement disorders, and promoting the growth of plants.    ADVANTAGE - The composition includes plant nutrition supplements.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer composition, comprising uniformly stirring the mentioned components, fermenting at 80-100 degrees C for 50-60 minutes, when the acid alkali degree reaches to neutral, adding organic phosphorus compound, stirring uniformly, and drying.
NOVELTY - Pollution-free organic fertilizer comprises 20 pts. wt. sewage sludge, 30-50 pts. wt. seaweed fermentation product, 20 pts. wt. kelp, 10-20 pts. wt. soybean straw fermentation product, 5-10 pts. wt. organic phosphorus compound, 0.5-2 pts. wt. citric acid, and hydrogen peroxide (required amount).    USE - The fertilizer is used for promoting growth of plant.    ADVANTAGE - The fertilizer can stimulate plant non specific activity factor of production, regulates endogenous hormone balance, with different regulating effect on different crops and different stage of crops, prevents the pest damage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing pollution-free organic fertilizer comprising adding hydrogen peroxide at 60-80 degrees C environment, reacting for 30-50 minutes, intermediate stirring once, adding citric acid, when acid alkali degree reach to neutral, adding organophosphorus, stirring uniformly, drying, continuing to stir uniformly to obtain fertilizer.
NOVELTY - Knee pad comprises outer layer and inner layer containing ginger and outer layer of thin fabric. The inner layer drug passes through the outer layer of skin contact gap.    USE - The knee pad relieves pain, and ensures no skin injury, low cost, environmental protection, no side effect and and multiple and long-term use.
NOVELTY - The device has membrane-electrode assembly (MEA), the keysets (50), the spacer (30) and encapsulant (40,41). The encapsulant is provided with a passage unit (72) for transporting the electrolyte and generating gas for hermetically preventing the leakage. The hydrogen electrode (20), the oxygen electrode (10) and the separation film (60) are provided in main portion. The nickel foil film is formed on surface in which nickel alloy thin film is formed. The pressure-molded porous nickel supporter is provided in state where nickel electrode includes nickel powder.    USE - Electrolysis device used in food, metal, lamp, welding, deodorization and sterilization lamp industry.    ADVANTAGE - The exhaustion of the generating gas is facilitated and the hermetic sealing of the stack each inter-layer is guaranteed. The exhaustion of the electrolysis participation material with the simple manufacturing method is uniformly performed. The cost of the electrolysis device is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of electrolysis device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolysis device.    Oxygen electrode (10)    Hydrogen electrode (20)    Spacer (30)    Encapsulant (40,41)    Keysets (50)    Separation film (60)    Passage unit (72)
NOVELTY - A saline land modifier comprises 50-70 parts mass gypsum, 20-30 parts mass basic animal manure having moisture content of 10% or less, 5-10 parts mass furfural residue having moisture content of 10% or less, 2-5 parts mass nitrogen-phosphorus fertilizer, and 3-5 parts mass calcium nitrate. The gypsum is naturally dried gypsum.    USE - Saline land modifier (claimed).    ADVANTAGE - The saline land modifier is prepared by simple, easy, environmentally-friendly and economical method by recycling flue gas desulfurization waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of saline land modifier.
NOVELTY - Method for preparing eco-fertilizer, involves (a) mixing weathered coal humic acid and ammonium bicarbonate, spraying Bacillus fermentation broth on the mixture, and composting mixture, (b) adding superphosphate to concentrated molasses broth to the mixture, further adding shell powder to the mixture, adjusting pH of the mixture, and composting mixture, and (c) uniformly mixing products of steps (a) and (b), adding ammonium sulfate to the mixture, adding mixture into disc granulator, drying mixture, adding chitosan, and cooling mixture.    USE - The method is useful for preparing eco-fertilizer (claimed).    DETAILED DESCRIPTION - Method for preparing eco-fertilizer, involves (a) mixing 900-1050 kg weathered coal humic acid and 90-110 kg ammonium bicarbonate, spraying 40-50 kg Bacillus fermentation broth on the mixture, and composting mixture for 64-72 hours, (b) adding 900-1100 kg superphosphate to 90-110 kg 40-50% concentrated molasses broth to the mixture, further adding 200-300 kg shell powder to the mixture, adjusting pH of the mixture to 6.5-8, and composting mixture for 10-20 hours, and (c) uniformly mixing products of steps (a) and (b) in a ratio of 1:1, adding 200 kg ammonium sulfate to the mixture, adding mixture into disc granulator, drying mixture at 80 degrees C, adding chitosan as carrier to the mixture, and cooling mixture to 50 degrees C.
NOVELTY - Method for preparing mushroom cultivation material, involves adding water to crushed mushroom mixture, soaking mixture, adding mushroom residue, cotton hulls and soybean, piling mixture, fermenting, maintaining the mixture, turning, adding lime and gypsum, maintaining the mixture, fermenting the mixture, cooling fermented product, loading the cooled product in polypropylene bags, bagging product, creating hole in the bags, inoculating fungal strains in hole, culturing bags in dark room at 20-22 degrees C and humidity of 60-75%, and obtaining mycelium.    USE - The method is useful for preparing mushroom cultivation material (claimed).    ADVANTAGE - The method is environmentally-friendly, and saves labor.    DETAILED DESCRIPTION - Method for preparing mushroom cultivation material, involves (a) obtaining 82-86% cotton seed hull, 8-10% soybean, 3-4% mushroom stock, 2.5% lime and 1% gypsum, and crushing shiitake mushroom into particles of 2-3 mm, (b) adding 20-30 times water to crushed mushroom mixture, soaking mixture for 18-24 hours, adding mushroom residue, cotton hulls and soybean to the mixture, piling mixture at height of 1-1.2 m and width of 2-3 m, controlling mixture until the dry weight of the mixture reaches 300-500 kg, and fermenting the mixture, (c) maintaining the mixture at 60 degrees C for 24 hours, turning mixture once, adding lime and gypsum to the mixture, maintaining the mixture for 5-6 days, and fermenting the mixture until the moisture content reaches 63-65%, and (d) cooling fermented product, loading the cooled product in polypropylene bags (17 cmx 35 cmx 0.004 cm), bagging product, creating hole in the bags, inoculating fungal strains in hole, culturing bags in dark room at 20-22 degrees C and humidity of 60-75% for 23-25 days, and obtaining mycelium.
NOVELTY - Method for preparing ecological fertilizer, involves concentrating sludge, dehydrating the concentrate, performing anaerobic digestion of the dehydrated concentrate to achieve stabilization of sludge, obtaining sludge concentrate, analyzing organic matter, nitrogen, phosphorus, potassium and other nutrient content in pre-treated sludge based on crop needs, adding Bacillus biological additives to the sludge, adding e.g. polysaccharide polymer, and dimethyl phthalate, mixing materials, and naturally drying or drying product.    USE - The method is useful for preparing ecological fertilizer (claimed).    ADVANTAGE - The method is cost-effective.    DETAILED DESCRIPTION - Method for preparing ecological fertilizer, involves (a) concentrating sludge, dehydrating the concentrate, performing anaerobic digestion of the dehydrated concentrate to achieve stabilization of sludge, obtaining sludge concentrate with no odor, no significant mechanical impurities, no odor, coliform bacteria value of 0.1-0.01, roundworm and other parasites egg mortality of 95%, and moisture content of 40-60%, (b) analyzing organic matter, nitrogen, phosphorus, potassium and other nutrient content in pre-treated sludge based on crop needs, and adding Bacillus biological additives to the sludge, where the prepared product has organic matter content of 30% and nutrient content of less than or equal to 4%, and (c) adding 5-10% polysaccharide polymer, 0.2-5% polysaccharide, 0.2-1% glycerol, 0.2-0.5% tributyl citrate, 0.5-1% dimethyl phthalate, and 82.5-93.9% water sludge to the prepared sludge product, uniformly mixing materials, naturally drying or drying product until the moisture content reaches 20% or less.
NOVELTY - Preparing bifenthrin (I), comprises carrying out esterification reaction of lambda -cyhalothric acid (II) with 2-methyl-3-phenyl-benzyl alcohol (III) in aqueous organic solvent in presence of a catalyst in an autoclave, and then removing aqueous organic solvent and the reaction-generated water to obtain final product.    USE - The method is useful for preparing bifenthrin.    ADVANTAGE - The method: has high conversion rate of 2-methyl-3-phenyl benzyl alcohol, and less amount of synthetic waste; and utilizes catalyst, which is easy to separate and recover.    DETAILED DESCRIPTION - Preparing bifenthrin of formula (I), comprises carrying out esterification reaction of lambda -cyhalothric acid of formula (II) with 2-methyl-3-phenyl-benzyl alcohol of formula (III) in aqueous organic solvent in presence of a catalyst in an autoclave, and then removing aqueous organic solvent and the reaction-generated water to obtain final product.
NOVELTY - Leaves, wood, vegetables, waste paper plastics, waste cloth and other organic combustible substances are pyrolyzed, water is removed, and dried. The combustible waste is calcined and carbonized to obtain alkane, carbon monoxide, tar and water vapor. The waste is distilled, redox reaction is carried out by the action of water vapor to obtain carbon monoxide, hydrogen and other combustible gases. The inorganic slag discharged from the bottom of the reactor is pyrolyzed, recovered, molded and the resulting mixture is sintered to obtain domestic waste-pyrolyzed sintered brick.    USE - Preparation of domestic waste-pyrolyzed sintered brick used for building.    ADVANTAGE - The method provides domestic waste-pyrolyzed sintered brick with reduced energy consumption of 650 kcal.    DETAILED DESCRIPTION - Leaves, wood, vegetables, waste paper plastics, waste cloth and other organic combustible substances are added from the top of the combustion furnace to the pyrolysis gasification furnace, pyrolyzed at 80-120 degrees C for 1-2 hours, water is removed, and dried. The combustible waste is calcined at 200-450 degrees C and carbonized to obtain alkane, carbon monoxide, tar and water vapor. The waste is distilled, redox reaction is carried out at high temperature of 1100-1200 degrees C by the action of water vapor to obtain carbon monoxide, hydrogen and other combustible gases. The inorganic slag discharged from the bottom of the reactor is pyrolyzed, purified, recovered, molded and the resulting mixture is sintered to obtain domestic waste-pyrolyzed sintered brick.
NOVELTY - The device has a shredder (1) connected with a pump (2) that is connected to a lower fitting unit (3) of a methane reactor (4). A discharge pipe (5) is closed by a constriction part (6), which is located in an upper part of the methane reactor. The constriction part is connected to a gas conduit (7) that is equipped with an electrovalve (8). The discharge pipe is connected to a hydrogen pipe (9). A carbon dioxide sensor (10) is placed in the methane reactor and connected to an electrical control panel (11).    USE - Device for increasing amount of methane in a methane biogas reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for increasing amount of methane in a methane biogas reactor.    Shredder (1)    Pump (2)    Lower fitting unit (3)    Methane reactor (4)    Discharge pipe (5)    Constriction part (6)    Gas conduit (7)    Electro valve (8)    Hydrogen pipe (9)    Carbon dioxide sensor (10)    Electrical control panel (11)
NOVELTY - The apparatus has a dehumidifier that is installed in exterior wall of main portion (100) for removing the moisture of the inside. A suction unit is formed in the main portion and a driving portion is provided for inhaling the generated gas inside main portion. A heater heat-treats the transferred gas inhaled from the suction unit. The handle is combined in end portion of shaft gear to eject the waste received to the main portion in front side. The exhaust door is combined to open and close vent. The shaft gear delivers power in switching operating of exhaust door.    USE - Organic waste treatment apparatus.    ADVANTAGE - The installation cost of the organic waste treatment apparatus is reduced and the high-quality compost is produced. The organic waste treatment apparatus is environment friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the organic waste treatment apparatus.(Drawing includes non-English language text)    Main portion (100)    Driving portion (200)    Gas treating section (300)
NOVELTY - Preparation of eucalyptus organic fertilizer involves mixing 30-40 pts. wt. cow dung having water content of 70-80% and 60-70 pts. wt. corn stalk, adding fermentation agent to the resultant product, mixing, adjusting water content to 50-60%, fermenting by adding the obtained mixture to fermentation plant by carrying out aerobic fermentation, fermenting again by anaerobic fermentation, adjusting water content of the resultant product to 20-30%, crushing the resultant product, sieving and obtaining powdered or granular organic fertilizer.    USE - Preparation of eucalyptus organic fertilizer (claimed).    ADVANTAGE - The method enables preparation of eucalyptus organic fertilizer having reduced size and weight, by carrying out pyrolysis by killing pathogens, eliminating odor and reducing moisture content.    DETAILED DESCRIPTION - Preparation of eucalyptus organic fertilizer involves mixing 30-40 pts. wt. cow dung having water content of 70-80% and 60-70 pts. wt. corn stalk, adding 1 pt. wt. fermentation agent to the resultant product with respect to 5000 pts. wt. cow dung, mixing, adjusting water content to 50-60%, fermenting by adding the obtained mixture to fermentation plant having piled windrow shape with windrow width of 1.8 m and height of 1.2-1.6 m by carrying out aerobic fermentation for 15-20 days, turning once every two days, fermenting in winter for 25-30 days, turning once every 3-4 days, fermenting again by anaerobic fermentation for 5-9 days, adjusting water content of the resultant product to 20-30%, crushing the resultant product, sieving and obtaining powdered or granular eucalyptus organic fertilizer.
NOVELTY - Extraction of oleuropein involves adding ethanol solution containing alkyl glycoside or alkyl glycoside aqueous solution to Syringa reticulata, extracting, filtering resulting mixture, adding water to the mixture, filtering the mixture, carrying out macroporous resin adsorption, eluting using ethanol, concentrating eluate and drying.    USE - Extraction of oleuropein from S.reticulate (claimed).    ADVANTAGE - The method enables extraction of oleuropein with high extracting efficiency, by simple and environmentally-friendly process.
NOVELTY - Ethylene splitting furnace operation efficiency improvement involves establishing ethylene splitting operation production data including ethylene splitting and production material object character parameter, working condition data and decoking device parameter. The object character parameter comprises coking rate data and ethylene splitting product average yield, object character parameter of material of collecting ethylene splitting industrial on site, real time working condition data and market, cost data, and production data.    USE - Method for improving operation efficiency of large ethylene splitting furnace (claimed).    ADVANTAGE - The method improves operation efficiency of large ethylene splitting furnace in a simple manner with increased furnace production, optimized furnace decoking operation, and maximized splitting operation.    DETAILED DESCRIPTION - Ethylene splitting furnace operation efficiency improvement involves establishing ethylene splitting operation production data including ethylene splitting and production material object character parameter, working condition data and decoking device parameter. The object character parameter comprises coking rate data and ethylene splitting product average yield, object character parameter of material of collecting ethylene splitting industrial on site, real time working condition data and market, cost data, and production data. The operation object character parameter is closed to material in splitting ethylene with real time working condition data and the cost data.
NOVELTY - Dendrobium endophytic fungal strain NT43J06 belonging to the genus Phyllachora sp. deposited under CCTCC No. M2014333, is new, where 18S ribosomal DNA (rDNA) sequence of the strain comprises SEQ ID No: 1 (a 1680 base pair sequence fully defined in the specification).    USE - The new strain is useful for preparing fungal elicitor culture medium and biological fertilizer for growing Dendrobium (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) use of strain for growing Dendrobium; (2) use of strain for preparation of fungal elicitor culture medium, which involves activating strain, seeding in liquid culture, fermenting, filtering fermentation broth under vacuum, grinding mycelium with liquid nitrogen, combining with filtrate after sterilization to obtain fungal elicitor and accessing fungal elicitor to Murashige and Skoog (MS) culture medium to obtain fungal elicitor culture medium; and (3) use of strain for preparation of biofertilizer, which involves activating strain, seeding in liquid culture, fermenting, adding bark powder to fermentation broth, and uniformly mixing to obtain biofertilizer.
NOVELTY - Method for preparing liquid fertilizer, involves filling rock wool raw materials in cupola, combusting raw material at 1550-1600 degrees C, generating fiber into diameter of 5-7 mu m in fibrosis spinner using high-speed rotation, cooling mixture, stirring mixture, shaping mixture, cutting product into flake of 5-20 mm, adding water and nitric acid to the flakes, heating mixture at more than 80 degrees C, dissolving the mixture in nitric acid, calcium nitrate tetrahydrate and silicate solution, neutralizing the mixture using aqueous lime solution, to neutralize the nitric acid in excess of aluminum hydroxide, ferric hydroxide and filtering mixture.    USE - The method is useful for preparing liquid fertilizer (claimed).    ADVANTAGE - The method is environmentally-friendly, and prepares liquid fertilizer simply and easily.
NOVELTY - Cultivating Hypsizigus marmoreus comprises fermenting, bagging, sterilizing, inoculating, shelving, culturing fungi, opening the bag, budding, fruiting and harvesting; where the fermentation includes: mixing 56% cottonseed hull, 18% sawdust, 18% oatmeal, 5% corn flour, 2% nutrient solution, 2% lime and water, stacking, turning once every 7-10 days, to obtain culture materials with moisture content of 66-68%, pH of 7.3-7.6.    USE - The method is useful for cultivating Hypsizigus marmoreus (claimed).    ADVANTAGE - The method is environmentally-friendly, simple to operate, and easy to popularize.
NOVELTY - A Bacillus licheniformis strain UTM115 capable of degrading azo compound (CGMCC No 9680), is new.    USE - The B.licheniformis strain UTM115 is useful for treating organic solid waste containing azo compound and degrading azo compound. The organic solid waste is urban and rural sewage sludge, food waste, livestock manure, and waste from printing and dyeing industry (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) primer for cloning 16S ribosomal DNA (rDNA) B.licheniformis strain UTM115 comprising forward primer comprising base pair sequence of: 5'-agagtttgatcctggctcag-3' and reverse primer comprising base pair sequence of: 5'- ggttaccttgttacgactt-3'; (2) microbial inoculum comprising B.licheniformis strain UTM115; and (3) use of B.licheniformis strain UTM115 for treating organic solid waste containing azo compound.
NOVELTY - A Bacillus licheniformis strain UTM108 having biomass hydrolase activity (CGMCC No 9679), is new.    USE - The B.licheniformis strain UTM108 is useful for treating rural and urban organic solid waste compost and producing environmentally friendly biofertilizer. The organic solid waste includes municipal sewage waste, food waste, animal carcasses and animal manure (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) primer for cloning 16S ribosomal DNA (rDNA) B.licheniformis strain UTM108 comprising forward primer comprising base pair sequence of: 5'-agagtttgatcctggctcag-3' and reverse primer comprising base pair sequence of: 5'- ggttaccttgttacgactt-3'; (2) microbial inoculum comprising B.licheniformis strain UTM108; and (3) use of B.licheniformis strain UTM108 for treating rural and urban organic solid waste compost and producing environmentally friendly biofertilizer.
NOVELTY - A Bacillus licheniformis UTM118 strain (CGMCC No.9681) is new.    USE - New Bacillus licheniformis UTM118 strain (CGMCC No.9681) for microbial inoculum, compost inoculum, organic solid compost fermentation of waste and preparation of organic fertilizer (all claimed).    ADVANTAGE - The strain is capable of producing high temperature resistant acid alpha -amylase. Fertilizer has green environment protection, good performance and good social and economic benefits.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) microbial inoculum comprising Bacillus licheniformis UTM118 strain; (2) preparation of compost inoculums which involves preparing fermentation liquid using B. licheniformis bacterial strain UTM118 which is fermented in Luria-Bertani( LB) liquid culture medium, and drying to obtain powder shape; and (3) use of B. licheniformis UTM118 strain in organic solid composite fermentation of waste and for preparing organic fertilizer.
NOVELTY - Brewing method of wine lees involves performing alkali treatment of wine lees and performing fermentation.    USE - Brewing method of wine lees for producing marsh gas (claimed).    ADVANTAGE - Pollution problem can be solved, clean energy can be provided, and environment can be protected.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of producing marsh gas which involves using wine lees derived from treated garbage waste, straw waste, compost, and other related substances and performing fermentation.
NOVELTY - A ginsenoside Rh2 enzymatic method is performed by using compound containing ginsenoside Rg3 composite as substrate, preparing 0.5-5 mg/ml aqueous solution, controlling pH value to 4-7, controlling temperature to 50-65 degrees C for 0.5 hour, using catalyst based on Rg3 ratio of 1:5-1:100 and adding Aspergillus oryzae containing glycosyl hydrolase or corresponding glycosyl hydrolase, reacting at 25-65 degrees C for 3-48 hours, performing alcohol precipitation and removing enzyme and solubilizer, and freeze-drying reaction solution.    USE - Ginsenoside Rh2 enzymatic method.    ADVANTAGE - Method has high efficiency and is environment-friendly.
NOVELTY - Food waste and sludge acidification hydrogen production pretreatment involves (a) mixing pulverized food waste and sludge, mixing obtained feedstock with sulfuric acid, hydrolyzing at 135 degrees C for 15 minutes to obtain fermentation feedstock, (b) taking feedstock in fermentation bottle, adjusting pH, adding yeast powder, inoculating hydrogen producing bacteria by dark fermentation, passing high-purity nitrogen gas, and acidifying to obtain liquid hydrogen, and (c) adjusting pH of liquid hydrogen, adding methanogen, and fermenting anaerobically to produce methane.    USE - Food waste and sludge acidification hydrogen production pretreatment to improve methane production rate (claimed).    ADVANTAGE - The method effectively improves methane production rate, such that the methane production peak time is reduced by 50%. The unit volume of fermenter equipment is reduced by 50%, thus reducing waste decomposition time.    DETAILED DESCRIPTION - Food waste and sludge acidification hydrogen production pretreatment involves (a) mixing pulverized food waste and sludge in a mass ratio of 1:1 to obtain pretreated feedstock, mixing pretreated feedstock with 1 %mass sulfuric acid to obtain a pretreated feedstock mixture a concentration of 20-30 g/L, hydrolyzing at 135 degrees C for 15 minutes to obtain fermentation feedstock, (b) taking 200-500 ml fermentation feedstock in 600 ml fermentation bottle, adjusting pH to 6.4-6.6 using 6 mol/L sodium hydroxide, adding 0.2-0.5 g yeast powder, inoculating 20-50 ml hydrogen producing bacteria by dark fermentation, passing high-purity nitrogen gas for 20 minutes to create anaerobic fermentation environment, and acidifying at 37 degrees C to obtain acidified pretreated liquid hydrogen, and (c) adjusting pH of liquid hydrogen to 7.9-8.1 using 6 mol/L sodium hydroxide, adding 20-50 ml methanogen, and fermenting anaerobically at 37 degrees C to produce methane.
NOVELTY - A primer pair set for detecting and distinguishing the different sheep Morse babesia, and/or undefined species Xinjiang strains of ovine babesia, is new.    USE - The primer pair set and kit are useful for detecting and distinguishing the different sheep Morse babesia, and/or undefined species Xinjiang strains of ovine babesia (claimed).    ADVANTAGE - The primer pairs and kit have the advantages of high sensitivity, high speed, high specificity and the like on detection; the environmental pollution can be avoided; the detection time is shortened; and the primer pairs and the kit are especially suitable for detection and diagnosis of large batch of samples with acute and subclinical infection.    DETAILED DESCRIPTION - A primer pair set for detecting and distinguishing the different sheep Morse babesia, and/or and undefined species Xinjiang strains of ovine babesia, where the primer sequence is: acctctgaacgtaacaaac (SEQ ID NO: 1) and cacggagcaacagtagaa (SEQ ID NO: 2); and/or agacctctgaacgtaacc (SEQ ID NO: 4) and gctgataattaatgccacatac (SEQ ID NO: 5), is new. An INDEPENDENT CLAIM is included for a kit for detecting and distinguishing sheep M. babesia and undefined species Xinjiang strains of ovine babesia, which comprises: (a) the primer pair for sheep Morse babesia having the sequence of SEQ ID NO: 1 and SEQ ID NO: 2; (b) the primer pair for undefined species Xinjiang strains of ovine babesia; and (c) a probe sequence Motas1-ProbJ; and (d) a probe sequence OBXJ-Prob, where the probe sequence is SEQ ID NO: 3 and SEQ ID NO: 6 and 5 combined light-emitting group FAM, 3 combined with fluorescent quenching group BHQ1.
NOVELTY - Substrate comprises 75-80 kg peat, 2-5 kg perlite, 15-20 kg vermiculite, and 0.6-0.7 kg water-soluble fertilizer having water content of less than or equal to 2%.    USE - The substrate is useful for planting tobacco (claimed).    ADVANTAGE - The substrate provides required nutrient to tobacco, can be prepared cost-effectively, has excellent moisture holding capacity, and increases growth rate of tobacco.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the substrate, which involves mixing and crushing the above-mentioned materials, performing fermentation at 28-30 degrees C, adding chitin to obtained product, stirring the materials together, making mixture into blocks, and spraying fertilizer solution on the blocks.
NOVELTY - Method for breeding pig and producing pig manure, involves providing fattening pigsty and pig manure pond, making ditches or underground pools in the pigsty which are connected by underground pipe, where the pig manure pond is provided below the fattening pigsty, allowing pigs to breed in the pigsty while collecting feces in the pig manure pond, collecting the feces, mixing the feces with corn stalks, sunflower stalks or straw, piling mixture, and periodically turning product to obtain fertilizer.    USE - The method is useful for breeding pig and producing pig manure (claimed).    ADVANTAGE - The method increases benefits of farmer.
NOVELTY - Photosensitive agent comprises 0.025-0.4 g phycobiliprotein and 95-99 ml phosphate buffer (PBS) composition.    USE - The photosensitive agent is useful for providing antimicrobial effect against Staphylococcus aureus, Bacillus subtilis, Aspergillus flavus, and A.niger (all claimed), and controlling and recycling water-blooming cyanobacteria.    ADVANTAGE - The agent is convenient to use, and prepared by simple method, cost-effective, and environmentally-friendly.
NOVELTY - Bacterial culture device comprises combining box (1), bacterial culture sample compartment (2), pollution sampling lid (3), the cooling tank (4), thermodynamic cycle tank (5) and power box (6). The right side of combination box is provided with carrying handle (7). The carrying handle is provided with soft handle (8). The combination box is also provided with provided with a reinforcing base plate(9). The lower side of reinforcing base plate is provided with wheel (10). The wheel is provided with fixed slip sheet (11).    USE - Bacterial culture device.    ADVANTAGE - The bacterial culture device is fully functional, easy to use, and prevents pollution and saves time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of bacterial culture device.    Combining box (1)    Bacterial culture sample compartment (2)    Pollution sampling lid (3)    Cooling tank (4)    Thermodynamic cycle tank (5)    Power box (6)    Carrying handle (7)    Soft handle (8)    Reinforcing base plate (9)    Wheel (10)    Slip sheet (11)
NOVELTY - Preparation of raw glyphosate powder involves carrying out air oxidation of N-(phosphonomethyl)iminodiacetic acid in activated carbon and water, heating, filtering, providing filtrate into crystallization reactor, stirring, filtering, repeating above process 3 times, then filtering to obtain diluted and concentrated glyphosate solutions, carrying out pyrolysis and rectification with respect to diluted glyphosate solution, recovering formaldehyde, repeatedly using the diluted glyphosate solution, cooling the concentrated solution, filtering, and removing phosphorus.    USE - Preparation of raw glyphosate powder (claimed).    ADVANTAGE - The method enables simple preparation of raw glyphosate powder with high productivity without generation of waste residues.    DETAILED DESCRIPTION - Preparation of raw glyphosate powder involves carrying out air oxidation of N-(phosphonomethyl)iminodiacetic acid in activated carbon (catalyst) and water at 701-751 degrees C to obtain glyphosate solution, heating glyphosate solution at 90-95 degrees C for 28-32 minutes, filtering to separate activated carbon, providing filtrate into crystallization reactor through frozen brine, stirring at 0-5 degrees C for 24 hours, filtering, repeating above process 3 times, then filtering using membrane filter to obtain diluted and concentrated glyphosate solutions, carrying out pyrolysis and rectification with respect to diluted glyphosate solution, recovering formaldehyde, repeatedly using the diluted glyphosate solution, cooling the concentrated solution, carrying out membrane filtration, and then removing phosphorus in an oxidation hydrolysis tower using phosphorus removal agent containing magnesium oxide, ammonium hydroxide and caustic soda. The bottom liquid contains 0.01-0.03 wt.% glyphosate, after pyrolysis. The ratio of bottom liquid, magnesium oxide, ammonium hydroxide and caustic soda is 1:(0.0005-0.002):(0.001-0.005):(0.001-0.004).
NOVELTY - A 2-(4,11-dimethyl-13-(2-oxoethyl)-1,5,10,14-tetraoxadispiro-hexadecan-2-yl)acetaldehyde derivative (I), is new.    USE - New 2-(4,11-dimethyl-13-(2-oxoethyl)-1,5,10,14-tetraoxadispiro-hexadecan-2-yl)acetaldehyde derivative is used for preparing statin (claimed).    ADVANTAGE - The 2-(4,11-dimethyl-13-(2-oxoethyl)-1,5,10,14-tetraoxadispiro-hexadecan-2-yl)acetaldehyde derivative enables economical, easy and environmentally-friendly preparation of statin with high yield.    DETAILED DESCRIPTION - A 2-(4,11-dimethyl-13-(2-oxoethyl)-1,5,10,14-tetraoxadispiro-hexadecan-2-yl)acetaldehyde derivative of formula (I), is new.    X=leaving group, azido, -CN, -OH, -OCOR1, -COOR1, -NH2, -NHR1, or -CHO, and    R, R1=ester residue.    An INDEPENDENT CLAIM is included for preparation of 2-(4,11-dimethyl-13-(2-oxoethyl)-1,5,10,14-tetraoxadispiro-hexadecan-2-yl)acetaldehyde derivative (I).
NOVELTY - Co-preparation of ammonium sulfate and glyphosate using glycine involves catalytic wet air oxidation of glyphosate mother liquor, concentrating, adding dilute sulfuric acid and aqueous ammonia, purifying, dehydrating, introducing the dichloromethane into a reactor, adding 18-32% aqueous sulfuric acid solution, reacting at 120-1320 degrees C at pH 4.3-4.5 in the presence of ammonia gas to obtain ammonium sulfate solution, filtering to remove impurities, carrying out multi-effect evaporation, obtaining ammonium sulfate wet product, centrifuging, crystallizing and drying.    USE - Co-preparation of ammonium sulfate and glyphosate (claimed).    ADVANTAGE - The method efficiently provides ammonium sulfate by an environmentally-friendly process.    DETAILED DESCRIPTION - Co-preparation of ammonium sulfate and glyphosate using glycine involves performing catalytic wet air oxidation of glyphosate mother liquor, concentrating, adding dilute sulfuric acid and aqueous ammonia, purifying, dehydrating, introducing dichloromethane into a reactor, adding 18-32% aqueous sulfuric acid solution, reacting at 120-1320 degrees C at pH 4.3-4.5 in the presence of ammonia gas, obtaining ammonium sulfate solution, filtering to remove impurities, carrying out multi-effect evaporation to obtain ammonium sulfate wet product, centrifuging, crystallizing and drying in air. Ammonia gas condensate is generated during the reaction process and titanium dioxide, ruthenium and rhodium as catalyst are fed into a catalytic wet oxidation tower, oxidized, then introduced into a biochemical pool and processed.
NOVELTY - Preparation of arbekacin involves reacting 3',4'-dideoxy-3',4'-didehydro-kanamycin B with tert-butyl dicarbonate as protecting reagent, obtaining protected compound in which three amino groups of 2', 6' and 3 carbon positions are protected by tert-butoxycarbonyl, introducing direct selective side chain to free amino group of the 3" carbon position, acylating and hydrolyzing.    USE - Preparation of arbekacin (claimed).    ADVANTAGE - The method enables simple, environmentally-friendly and economical preparation of arbekacin with high yield, without using hydrazine hydrate.
NOVELTY - The system has a left conduit (22) that is connected between a primary fermentation pipeline and a secondary feedstock pipe (42). A right conduit (24) is connected with the primary fermentation pipeline and a secondary discharging tube (44). A feeding/discharging tube is connected with a lowest position of the secondary feedstock pipe below a horizontal plane. A front conduit (32) is provided with a one-way flow control valve for flowing the biogas into the primary fermentation pipeline.    USE - Vertical tower type secondary synchronization fermentation convection high-efficient fermentation system.    ADVANTAGE - The liquid circulation flow is promoted, the biogas stirring drive and uniform distribution of strain are effectively promoted and the fermentation efficiency is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the vertical tower type secondary synchronization fermentation convection high-efficient fermentation system.    Left conduit (22)    Right conduit (24)    Front conduit (32)    Secondary feedstock pipe (42)    Secondary discharging tube (44)
NOVELTY - The method involves pouring fermentation raw materials into two grade feedstock cylinders of two-stage fermentation systems (10,40). The fermentation region is formed between inner and outer biogas fermentation system, for accumulating biogas on side walls and out of cylinder block and the block adjacent to gas panel board. The marsh gas is produced using second level pipeline, so that the slurry provided within the storage chamber is flowed into primary and secondary fermentation biogas pipelines. The generation of methane is repeated and marsh gas is used.    USE - Tower type multistage circulation interaction method of producing high efficiency marsh gas fermentation system.    ADVANTAGE - The efficiency of the marsh gas fermentation system can be improved. The biogas can be produced in first-stage fermentation pipe extrusion inside of second level fermentation pipeline.    DETAILED DESCRIPTION - The extruded primary fermentation slurry is flowed inside two pipes (22,24), such that the biogas liquid is changed along with the increase of two guide pipes. The marsh gas is stored within the primary fermentation biogas pipeline, while passing slurry into primary fermentation pipeline through third and fourth conduits.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the tower type multistage circulation interaction method.    Two-stage fermentation systems (10,50)    Material cylinder (12)    Pipes (22,24)    Feedstock pipe (52)    Discharging pipe (54)
NOVELTY - Preparation of dibenzothiazyl disulfide, involves mixing 2-mercaptobenzothiazole and organic solvent in four-necked flask equipped with stirrer, a condensate pipe, a dropping funnel and a thermometer, placing the flask in a water bath and then heating at 40 degrees C, stirring, adjusting pH to 7 and then dripping mixture of solvent and hydrogen peroxide, reacting for 1-3 hours, filtering, washing, and drying.    USE - The method is useful for preparing dibenzothiazyl disulfide, which is useful as rubber accelerator.    ADVANTAGE - The method enables simple preparation of dibenzothiazyl disulfide with improved yield, quality and reliability in an environmentally-friendly manner. The solvent can be recycled.
NOVELTY - A compound cefalexin capsule comprises 220-270 pts. wt. cefalexin, 2-20 pts. wt. ambroxol, 25-125 pts. wt. polacrilin potassium, 50-100 pts. wt. chitooligosaccharide, 5-50 pts. wt. talc powder, and 10-75 pts. wt. starch.    USE - Compound cefalexin capsule.    ADVANTAGE - The capsule has reasonable prescription, high dissolution rate, simple preparation method without pollution, and no bad reaction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of compound cefalexin capsule comprising:    (A) sieving cefalexin, ambroxol, chitooligosaccharide, talc and starch respectively through 100 mesh sieve, mixing, adding water, and boiling to 95-115 degrees C for 2-4 hours to obtain paste mixture;    (B) loading into fluidized bed, spray-granulating to inlet air temperature of 90-120 degrees C and outlet temperature of 35-45 degrees C at pressure of 0.43-0.46 MPa and peristaltic pump speed of 150-200 revolutions/minute, and determining cefalexin and ambroxol contents to 0.05 g/capsule; and    (C) filling into capsule, and packaging.
NOVELTY - The device has a left conduit (22) is connected between the fermentation pipeline (41) and the feeding pipes (42). A right conduit (24) is connected between the fermentation pipeline and the discharge pipes (44). A control-way primary fermentation slurry pipeline is provided between the fermentation pipelines and the left and right conduits. A front conduit (32) is connected to the fermentation pipelines and provided with a one-way pressure control valve to flow the slurry into a one-way valve of the fermentation pipelines.    USE - Methane fermentation device of biogas fermentation system.    ADVANTAGE - The effective liquid flow circulation is realized, the biogas stirring drive and uniform distribution of strain are promoted, and the fermentation efficiency is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the methane fermentation device of tower double fermentation system.    Left conduit (22)    Right conduit (24)    Front conduit (32)    Feeding pipes (42)    Discharge pipes (44)
NOVELTY - The method involves performing near infrared spectrograph collecting process. A batch cloning Esopiclone chip sample is obtained. A near infrared diffuse reflection spectrum value is calculated. Separate aluminum plastic package testing process is performed based on a fourier conversion algorithm. Derivative and vector normalization process is carried out. A near infrared diffuse reflection spectrum qualification testing module is established. A multi-batch dynamic production sample is obtained. Esopiclone clone chip sample spectrum is tested.    USE - Near infrared spectrum based zopiclone tablet quick identifying method.    ADVANTAGE - The method enables increasing negative and positive sample robustness of the test module, quickly detecting market reliability, realizing quickly identification quality evaluation process of a cloning Esopiclone using plastic package and chip and reducing detected sample pre-processing complexity and sample pollution based on non-destructive green analytical technology in time and cost-effective and quick manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph view illustrating a relationship between two parameters related to a near infrared spectrum based zopiclone tablet quick identifying method.
NOVELTY - The device has pyroelectric transducer (20) having heat exchanger (2) connected with supply line (7). A valve device (8) supplies fluid streams (9,10) having high temperature (TH) and low temperature (TK). A reactor (3) includes pyroelectric material (12) with Curie temperature. The high and low temperatures of fluid streams lie in temperature window below Curie temperature. A circulating pump (6) is externally communicated with valve device via control unit (18) so that cleavage products (48,52) are formed by energy and material conversions using pyroelectric material in reactor.    USE - Device for energy and material conversions for preparation of cleavage products e.g. hydrogen and oxygen from water and carbon monoxide and oxygen from carbon dioxide for synthesis of methane and methanol (all claimed).    ADVANTAGE - The effectiveness of the energy and material conversion is improved by efficient use of the waste heat and the pyroelectric coefficient is increased so that the degree of purity of the chemical compounds is enhanced. The device for energy and material conversions is designed with compact construction at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for energy and material conversions for preparation of cleavage products.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the device for energy and material conversions. (Drawing includes non-English language text)    Heat exchanger (2)    Reactor (3)    Circulating pump (6)    Supply line (7)    Valve device (8)    Fluid streams (9,10)    Pyroelectric material (12)    Control unit (18)    Pyroelectric transducer (20)    Cleavage products (48,52)    High temperature (TH)    Low temperature (TK)
NOVELTY - The method involves hydrogenating in presence of the catalyst containing one type of noble metal chosen from periodic table group 8-10 in biodiesel fuel. The oxygen is made to exist inside the reaction system. The concentration of the oxygen is 150-3500 ppm as an oxygen molecule in biodiesel fuel. The gas containing oxygen is introduced into the reaction system. The inside of the reaction system is supplied by the supply unit different from the biodiesel fuel of a supply raw material. The fixed bed reactor is fixed in the reactor by the catalyst.    USE - Method for processing hydrogenation of biodiesel fuel.    ADVANTAGE - The oxidation stability of biodiesel fuel is improved. The biodiesel fuel excellent in oxidation stability and low-temperature fluidity is ensured. The improvement of the initial activity of a biodiesel fuel hydrogenation catalyst and active stabilization is achieved. The necessity to add the essential heavy-rare-earth element to a catalyst is avoided. The hydrogenation active deactivation is suppressed and the lifetime improvement of a catalyst is enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view illustrating the relationship between the influence of the oxygenation acting on the hydrogenation reaction activity of Jatropha oil fatty-acid methyl ester and the flow through time.
NOVELTY - The new type utility claims have one plant solid waste harmless processing device, comprising in turn connected and solid waste pyrolysis gasification furnace, gas distribution oxygen pre-mixing and filtering room, fuel gas combustion chamber, dechlorination and drying device, the solid waste pre-processing device, the solid waste harmless processing device also comprises fuel gas and oxygen distribution pre-filter room connected the biomass pyrolysis gasification furnace, dechlorination and drying device and connected the top and tail sum processing device. When using the utility model is new type method and device processing solid waste, the discharge amount of dioxin of tail by check sum is less than 0.023ng/m3, other CO, SO2, HC1, NOx equal discharge index is greatly better than the state for 2014 year 7 month 1 day issued and discharge standard (GB18485-2014), complete can reach environment-friendly requirement.
NOVELTY - Method comprises feeding into the outer chamber of the digestion tank of diluted organic wastes, the process of anaerobic fermentation in the outer and inner chambers of the digestion tank at the temperature of 12-60 degrees C, mixing the fermented mass, removal from the digestion tank of the fermented sludge and selection of biogas from the outer and inner chambers. Prior to the process of fermentation of diluted organic wastes in the outer chamber of the digestion tank the grinding of wastes is carried out by means of ultrasonic vibrations at a frequency of 20 plus minus 1.5 kHz and intensity of ultrasound from 2 to 5 W/cm2 for 40-60 min.    USE - Agriculture.    ADVANTAGE - Method provides accelerated processing of solid organic wastes without the loss of finished product quality, increase in the yield of biogas produced without loss of its caloric content, increase in the profitability of production.3 tbl, 3 ex
NOVELTY - Apparatus comprises: at least one compost submersion reservoir (105); at least one agitation reservoir (117); and a plumbing apparatus configured to convey liquid between or among reservoirs.    USE - The apparatus is useful to process aerated compost tea, and to process water for curing off antimicrobial agents (all claimed).    ADVANTAGE - The apparatus: is efficient in performing continuous multiple batch brewing of compost tea, in an economical manner; can be easily cleaned after use; can easily be used with large particulate matter size compost; is reliable; and provides the compost tea of superior quality within 15-24 hours.    DESCRIPTION OF DRAWING(S) - The figure shows a side perspective view of an aerated compost tea brewer.    Apparatus (105)    Agitation reservoir (117)    External frame (118)    Air pump (123)    Drain valve (126)
NOVELTY - A production of biochar involves providing a feedstock comprising cardboard and/or chipboard, reducing the size of the feedstock, charging the reduced size feedstock into a processing vessel and pyrolyzing at a maximum temperature of at least 500 degrees C.    USE - Production of biochar used for agricultural and environmental applications and providing bioenergy, e.g. provision of restorative nutrient and moisture to impoverished agricultural land, mitigating depreciating groundwater assets, and generation of alternative fuel to deforestation.    ADVANTAGE - The method produces biochar which enhances soil nutrient and moisture holding capacity, enhances plant physiological outcomes such as increased water use efficiency, and sorb heavy metals (e.g., lead, antimony, copper and arsenic) in soils and plants, and co-produces bioenergy as a byproduct. The process is carried out without the aid of enormous, scaled up production facilities and equipment. Processing vessel also enables a quicker and more effective pyrolysis.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of feedstock and wood fuel installation in the vessels.    Ceramic block (55)    Wood fuel (57)    Steel canister (59)    Aluminum feedstock holder (61)    Inner barrel (63)
NOVELTY - Manufacture of hydrocarbonaceous compound involves introducing a fuel stream comprising reformable fuel into anode of molten carbonate fuel cell and/or internal reforming element associated with the anode, introducing cathode inlet stream comprising carbon dioxide and oxygen into cathode inlet of the molten carbonate fuel cell, generating electricity, generating an anode exhaust comprising hydrogen, carbon monoxide, water and carbon dioxide, reacting portion of anode exhaust in presence of shifting Fischer-Tropsch catalyst and generating gaseous product(s) and non-gaseous product(s).    USE - Manufacture of hydrocarbonaceous compound for producing fuel, lubricant and chemical.    ADVANTAGE - The method enables manufacture of hydrocarbonaceous compound having high quality and purity, with reduced energy consumption.    DETAILED DESCRIPTION - Manufacture of hydrocarbonaceous compound involves introducing a fuel stream comprising reformable fuel into anode of a molten carbonate fuel cell and/or an internal reforming element associated with the anode, introducing a cathode inlet stream comprising carbon dioxide and oxygen into a cathode inlet of the molten carbonate fuel cell, generating electricity within the molten carbonate fuel cell, generating an anode exhaust comprising hydrogen, carbon monoxide, water and carbon dioxide, reacting portion(s) of the anode exhaust under effective Fischer-Tropsch conditions in presence of shifting Fischer-Tropsch catalyst and generating gaseous product(s) and non-gaseous product(s). The ratio of hydrogen and carbon monoxide in the anode exhaust is 2.1:1-2.5:1, preferably 2.5:1.
NOVELTY - Recovering non-hydrophilic components from algae-containing water, comprises: providing algae-containing water; providing a non-polar solvent; mixing the algae-containing water and the non-polar solvent in a high shear environment under conditions to lyse the algae and cause non-hydrophilic components within the algae to be solubilized within the non-polar solvent; separating the water and the non-polar solvent containing non-hydrophilic components from residual algal biomass; and recovering the non-polar solvent containing non-hydrophilic components.    USE - The process is useful for recovering non-hydrophilic components from algae-containing water, where the non-hydrophilic components comprise oil, nutraceuticals, and/or nutritional supplements (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a system (10) for recovering oil from algae-containing water, comprising a high-shear mixer, a separation system to (a) recover an oil/solvent phase from an aqueous phase and (b) recover residual algal biomass, many storage tanks, a source of non-polar solvent, a source of algae-containing water, an input connector (16) coupling the source of non-polar solvent and the source of algae-containing water to the high-shear mixer, an output connector (20) coupling the high shear mixer and the separation system, and a product connector (24) coupling the separation system and a first of the storage tanks to permit discharge of the oil phase into one storage tank and discharge of the residual algal biomass into a second of the storage tanks; and    (2) a ship comprising the system.    DESCRIPTION OF DRAWING(S) - The figure shows a block diagram of the system for recovering oil from algae-containing water.    System (10)    Input connector (16)    Output Connector (20)    Product connector (24)    Solvent recovery device (28)
NOVELTY - The new type utility claims have one plant high temperature high pressure gasification furnace uses spiral cold slag machine, comprising power device, slag transport cylinder, sealing box and spiral cooling transport shaft, wherein in the power device comprises drive motor and a speed reducer, a slag transport cylinder tube with interval space is set with concentric inner layer cylinder and outside layer cylinder, the inner cylinder wall adjacent outer cylinder one side welding with heat dissipation fin, a slag transport cylinder in two ends each is provided with the same structure and sealing box, the sealing box provided with at least 4 channel sealing ring, respectively is outside and sealing ring, sealing ring, nitrogen sealing ring, sealing ring, spiral cooling transport shaft shaft body through out of installation from the speed reducer machine at end of elastic pillar pin shaft joint to seal tank I-slag transport cylinder send cell-seal tank II and extending box body, shaft body is solid shaft and hollow shaft section, section around the hollow shaft section is equipped with two rotary section opposite to the spiral piece group, cavity, hollow shaft section of gap space, sealing tank cooling water can into inner layer cylinder and outer cylinder is in.
NOVELTY - The assembly has a support element, heater, and an actuator for extending and retracting the heater away from and toward the support element. An actuator (100) and the heater assembly are in a retracted state when the actuator is at or below a first prescribed temperature and in an extended state when the actuator is at or above a higher second prescribed temperature. A heating surface of the heater assembly is arranged closer to the support element, when the heater assembly is in the retracted state than the extended state.    USE - Heater assembly for hydrogen generator used in portable electronic device.    ADVANTAGE - The shape of the actuator is effectively changed as the temperature changes, without loss of contact or damage. The quantities of fuel composition can be sized and shaped so as to produce a desired amount of hydrogen gas fit within the fuel unit in a volume efficient manner. The cross-initiation of adjacent quantities is prevented. The release of generated hydrogen is effectively facilitated.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a hydrogen generator; and    (2) a method of operating a hydrogen generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hydrogen generator.    Housing (72)    Cavity (74)    Fuel units (86)    Intermediate support element (92)    Actuator (100)
NOVELTY - A plant biomass briquette is obtained by crushing raw material containing 90-95 wt.% biomass feedstock particles and 5-10 wt.% fuel additive substance, mixing, drying, granulating and extrusion molding. The biomass feedstock particles contain wood chips, bamboo and straw. The fuel additive substance contains quicklime, combustion improver and clay.    USE - Plant biomass briquette is used for boiler.    ADVANTAGE - The biomass briquette has low ash content, high combustion value and high efficiency.
NOVELTY - A coagulant is added to a tank to process wastewater by membrane bio-reactor which performs biological treatment by microorganisms in an activated sludge, and to carry out solid-liquid separation process by a separation membrane within the tank. The coagulant-unadded activated sludge is added to the tank, by an amount of 50 times or more of parameter of concentration of activated sludge (MLSS) with respect to the addition amount of the coagulant, in the treatment of wastewater.    USE - Treatment of wastewater e.g. domestic wastewater and industrial effluent.    ADVANTAGE - The method enables efficient treatment of wastewater with suppressed occlusion of separation membrane and provides treated water of high quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for wastewater treatment system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the wastewater treatment system.    Membrane separation activated sludge process equipment (10)    Membrane separation tank (11)    Membrane module (15)    Coagulant addition unit (16)    Sludge addition unit (17)
NOVELTY - A coagulant is added to a tank to process wastewater by membrane bio-reactor which performs biological treatment by microorganisms in an activated sludge, and to carry out solid-liquid separation process by a separation membrane within the tank. The membrane-separation treated water is further processed by bio-film method by which the water is biologically treated by the micro-organisms adhered to a support , in the treatment of wastewater.    USE - Treatment of wastewater e.g. domestic wastewater and industrial effluent.    ADVANTAGE - The method enables efficient treatment of wastewater with suppressed occlusion of membrane filter and provides treated water of high quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for wastewater treatment system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the wastewater treatment system.    Membrane separation activated sludge process equipment (10)    Membrane separation tank (11)    Membrane module (15)    Coagulant addition unit (16)    Bio-film processing apparatus (70)
NOVELTY - Biofuel production involves collecting fish viscera, extracting oils by heating indirectly at 60 degrees C for 45 minutes, and then chemically reacting the extracted oils with methyl, or ethyl alcohol, and catalyst.    USE - Method for producing biofuel, preferably biodiesel (claimed).    ADVANTAGE - The method produces the biofuel in a simple, cost-effective and eco-friendly manner by using animal fats, preferably fats of fish viscera discarded by fishing industry.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation depicting effect of molar ratio methyl alcohol and oil. (Drawing includes non-English language text).
NOVELTY - The system has a main portion that controls the water temperature of a to-be-processed water supplied to a back stage membrane separator (6) by reaction heat generated by biodegradation reaction of an organic substance in a membrane separation activated-sludge apparatus (3). The membrane filter of the separator is provided to be a reverse osmosis membrane or a nano membrane filter. A piping unit is tied to a membrane module and back stage membrane separator of membrane separation activated-sludge apparatus and membrane separation activated-sludge apparatus.    USE - System for treating waste water such as natural water such as sewage water, returned water, industrial wastewater, refuse advance water, excrement wastewater, agricultural effluent, livestock farming waste water, and culture wastewater.    ADVANTAGE - The water temperature of to-be-processed water supplied to the back stage membrane separator is controlled by reaction heat generated by the biodegradation reaction of the organic substance in the membrane separation activated-sludge apparatus so as to suppress fall of temperature of to-be-processed water supplied to back stage membrane separator. Thus, the fall of permeate flow rate of water is suppressed effectively while reducing the operational energy of system by enabling the initial investment of installation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for treating water. (Drawing includes non-English language text)    Dipping type membrane separation activated-sludge apparatus (3)    Diffuser (4)    Membrane separation treated-water supply line (5)    Back stage membrane separator (6)    Pump (7)
NOVELTY - Method for increasing lipid production in a host organism, involves introducing into an organism an expression vector comprising a heterologous nucleotide sequence or its fragments which comprises (a) an operably linked promoter that drives expression in the organism, and (b) a lipid regulatory transcription factor gene chosen from 17 sequences.    USE - The method is used for increasing lipid production in a host organism, preferably prokaryotic cell or eukaryotic cell, more preferably Cyanobacteria, plants, or algae (all claimed) used for producing biofuel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) expression vector;    (2) cell;    (3) plant; and    (4) method for enhancing lipid overexpression or lipid production activity in an organism.
NOVELTY - A cathode electrode structure comprises carbon catalyst and an ionomer, where the cathode electrode structure satisfies the expression as given in the specification.    USE - Cathode electrode structure for use in transfer sheet for manufacturing a membrane/electrode and fuel cell (all claimed) i.e. solid polymer electrolyte fuel cells.    ADVANTAGE - The electrode structure reduces the usage-amount of ionomer in an electrode, without using platinum for a cathode, has high power generation characteristics, and oxygen reduction characteristics.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a transfer sheet comprising cathode electrode structure    (2) a membrane/electrode joined body    (3) a fuel cell.
NOVELTY - Collecting carbon dioxide, comprises (a) separating moisture from the gas generated from fossil-fuel combustion process by a moisture separating device, and (b) removing the coarse gas by filtering the solids solidified at more than -78.5 degrees C using a cooling system, solidifying the gas components at cryogenic temperature or separating by solidifying carbon dioxide at less than or equal to -78.5 degrees C, and separating carbon dioxide by re-solidifying.    USE - The carbon dioxide is useful for producing carbonated beverage, photosynthesis of plants and microalgae in greenhouse, and producing bio-diesel (all claimed).    ADVANTAGE - The method is economical, enables storage of the dry ice by solidifying carbon dioxide, and recycles carbon dioxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for collection and utilizing carbon dioxide, comprising liquefying or vaporizing dry ice was collected by the above method, and supplying into a photobioreactor. The photobioreactor is upflow fluidized bed photobioreactor for preventing the precipitation of the microalgae. The inner side of the photobioreactor is provided with an impact plate for increasing the contact rate of carbon dioxide by generating turbulence. The photobioreactor supplies carbon dioxide and nutrients vaporized at the bottom.
NOVELTY - Device (1) comprises at least one first section, and at least a second section directly in communication with the first portion. The first section is formed as a heating zone (2) with a direct steam heating, comprising at least one steam entry device (3) through which steam enters into the continuous biomass passing through the heating zone and heats the biomass during operation. The second section is formed as delay zone (4) through which the heated biomass flows continuously during operation.    USE - The device is useful in a sewage treatment plant for continuous thermal hydrolysis of biomass, preferably sewage sludge, and clarifying water loaded with water (all claimed).    ADVANTAGE - The device produces biodegradable biomass in simple manner, and prevents occurrence of steam blows.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) continuous thermal hydrolysis of biomass, preferably sewage sludge in the above device, comprising (a) continuously supplying biomass, (b) heating the biomass to a temperature introducing steam into the biomass, and (c) maintaining the temperature for a period in a continuous flowing through delay time zone; and    (2) clarifying water loaded with water in a sewage treatment plant having at least one digester, at least one plant for nitrification and/or at least one plant for denitrification, comprising providing hydrolyzed biomass, and introducing into the digester, the plant for nitrification and/or the plant for denitrification.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the (Drawing includes non-English language text).    Device (1)    Heating zone (2)    Steam entry device (3)    Delay time zone (4)    Steam entry surface (31)
NOVELTY - Device comprises a device for introducing a difficult to digest biological starting material, an activator for digesting the starting material after being activated at an activation temperature (TA) exceeding the TA of more than 55 degrees C, and a device for thermal activation of combination of starting material and activator.    USE - The device is useful for producing biomass composition (claimed).    ADVANTAGE - The device: produces biomass composition from cereal straw, horse manure, lopping of trees, digestate and/or miscanthus as feedstock (starting materials), to convert the organic carbon in the starting material into energy-rich hydrocarbon (e.g. methane).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing biomass composition, comprising (a) providing hardly digestible biological starting material, (b) Providing an activator for decomposing the starting material, after being activated at an activation temperature (TA) exceeding the TA of more than 55 degrees C, and (c) thermal activation of combined starting material and activator by a device for thermal activation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for producing biomass composition.    Starting material (1)    Separator (2)    Heating element (21)    Activator (42)    Fluid starting material (53)
NOVELTY - The utility model is new type providing one kind of biomass solid particle forming atomizing device and biomass particle fuel production line, solving the technology of biomass granule fuel processing production line of biomass solid particle fuel finished product rate and low technology problem, biomass solid particle forming atomizing device comprising: nozzel device (1), a water inlet pipe (2) and sum for pipe (3), a nozzel device (1) comprises water inlet (1-1) and air inlet (1-2), a water inlet (1-1) and water inlet pipe (2) one end is connected with pipe, an air inlet (1-2) and air inlet pipe (3) one end is connected with pipe. The biomass particle fuel production line, comprising: machine chamber (4), adjustor (5), a forced feeder (6), a granulator (7) and particle biomass solid forming of said atomizing device (8) of biomass solid particle forming atomizing device fastening set on machine bin (4) and the discharging mouth and adjustor (5) and wherein between feedstock. The utility model is new type will yield of biomass 5% to 20%.
NOVELTY - A hydrogen fuel is derived from steaming water, where the hydrogen fuel is liquefied at -200 degrees C, and the gasified liquid hydrogen produces hydrogen gas.    USE - Hydrogen fuel for use in energy industry, drive vehicles, machinery, devices and gas stoves.
NOVELTY - The new type utility claims have one plant condensed liquid recovery device, belonging to electricity made hydrogen. It comprises sum liquid separator, a cooler and condensed liquid storage tank, provided with bottom air inlet on gas-liquid separator, the cooler one end through pipeline and gas-liquid separator connected, another end through condensed liquid collecting pipe and condensation liquid storing tank connected the top, also set with upper air outlet in the condensed liquid collecting pipe, the condensing liquid storage tank bottom through condensing liquid relux pipe and gas-liquid separator connected, with one-way valve and set in the condensing liquid relux pipe, the cooler is set on relative position of high gas-liquid separator, the condensed liquid storage tank is set on height direction between gas-liquid separator and cooler or cooler and the same height.
NOVELTY - The new type utility claims have one planting agaricus bisporus can saving fermentation tunnel, comprising wall body and anti-moisture-proof, heat preservation and heat preservation anti-moisture wall top form fermentation tunnel main body, upper wall body set with fermentation tunnel door, bottom of fermentation tunnel main body set with wind channel, wind channel set with ventilating layer, each wind channel connected with centrifugal fan, the centrifugal fan connected with circulation pipeline, circulation pipeline connected with filter, the filter comprises filter entrance and filter outlet, the filter entrance and exit at filter respectively set with one control air valve, in the fermentation tunnel body provided with the intelligent controller, the intelligent controller and the centrifugal fan electric connection. The utility model is new type can get for rice-wheat, corn core, corn stalk, cotton seed hull, cotton-stalk straw, cow dung chicken equal straw and animal feces conversion is edible fungus cultivation and high-quality culture material.
NOVELTY - The utility model is new type supply have one kind novel biomass gasification device step. Two large area device comprises the pyrolysis and combustion gasification, pyrolysis region comprises feeding port, a pyrolysis furnace, the lock hopper, distributing tank and pneumatic transport device, combustion gasification area comprises coal powder nozzel, sum nozzel, gasification furnace, the air outlet and the slag pool, feedstock wherein the pyrolysis furnace and connected with the pyrolysis furnace respectively connected with grinding machine and pyrolysis sum nozzel, grinding machine and lock hopper, distributing tank, a pneumatic transport device, coal powder nozzel in turn connected with the gasification furnace comprises upper part connected with the inside cylinder and outside cylinder, inside cylinder in for combustion area, inside outside cylinder is gasification area, inner cylinder bottom and sum nozzel pyrolysis and gasification furnace connected, outside the top of the the coal powder and gasification furnace nozzel connected, air outlet set on bottom of gasification furnace and outside cylinder and lower part connected with slag pool. The utility model is new type has advantages wherein gasification intensity is high, fit and large scale biomass gasification, gasification product almost not containing tar.
NOVELTY - The new type utility claims have one plant biology diesel oil continuous production series jet mixed esterification generator, comprises with shell is equipped with water inlet and water outlet, inner shell set with multi-pass connecting pipe in turn connected in series of the reaction tank, inside of each reaction tank are set with multiple layer jet plate, upper jet plate arranged jet holes, outlet direction of each jet hole of jet discharge hole is uniform and the jet hole and the radiation direction vertical to, and and the jet plate on the plane form a certain included angle. Process through jet plate to alcohol oil reaction raw material by mixing, reaction raw material flowing through the jet hole in the middle, form spiral jet flow shape, realize effective dissolve and alcohol, high esterification rate. Circulation esterification, continuous production, high efficiency, and it saves have using traditional kettle production equipment necessary and water washing and distillation process, have production technique, reduce have production cost, avoids have waste water, waste gas, waste slag and equal pollutant discharge and to avoid cause environmental pollute, realize effective energy saving and environment-friendly.
NOVELTY - The device has a feedstock device fixed on an air inlet device that is connected with a gasification reaction furnace. The feedstock device is fixed in the gasification reaction furnace. A hopper (21) is fixed with a grading pipe (28) i.e. square pipe, that is fixed with a fan (30). An upper part of the fan is fixed with a middle feeding port (29). A lower part of the fan is connected with an impurity outlet (32), a large particle outlet (23), a middle particle outlet (24) and a small particle outlet (25). A storage bin is connected with a vent pipe that is fixed with an air switch.    USE - Biomass gasification reaction device.    ADVANTAGE - The device can reduce sink bottom weight and increase air flow flushing quantity so as to increase biomass utilization rate.    DETAILED DESCRIPTION - The grading pipe is made of non-metal material.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gasification reaction device.    Hopper (21)    Large particle outlet (23)    Middle particle outlet (24)    Small particle outlet (25)    Grading pipe (28)    Middle feeding port (29)    Fan (30)    Impurity outlet (32)
NOVELTY - Process (P1) for making both ethanol and furfural from a mixture of pentoses and hexoses, involves (a) fermenting a mixture of hexoses and pentoses to convert hexoses in the mixture to ethanol, (b) concluding the fermentation prior to any substantial conversion of pentoses in the mixture to sugar alcohols, (c) separating unconverted pentoses in the mixture from ethanol formed in the fermentation, to yield an ethanol product, (d) dehydrating and cyclizing the separated unconverted pentoses to furfural, and (e) recovering a furfural product.    USE - The process (P1) is useful for making both ethanol and furfural from a mixture of pentoses and hexoses. The process (P2) is useful for making furfural from a mixture of pentoses and hexoses (all claimed).    ADVANTAGE - The process is simple, convenient to perform, and cost-effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) process (P2) for making furfural from a mixture of pentoses and hexoses; and    (2) continuous process (P3) for making furfural from a mixture of pentoses and hexoses.
NOVELTY - Preparation of gamma -polyglutamic acid-fertilizer-pesticide composition comprises mixing 10-80 pts. wt. microorganism fermentation liquid organic fertilizer and trace elements, 0.01-2.0 pts. wt. 0.3-1.1% matrine, 0.01-1.0 pt. wt. Bacillus thuringiensis, 0.1-10 pts. wt. osthol and 10-20 pts. wt. gamma -polyglutamic acid, release agents and surfactants.    USE - Method for preparing gamma -polyglutamic acid-fertilizer-pesticide composition (claimed) used for controlling crop fertilization and preventing pests.    ADVANTAGE - The product is environment-friendly and has improved efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of gamma -polyglutamic acid-fertilizer-pesticide composition comprising diluting composition with 200-800 times the amount of water and manually or machine spraying to the leaf.
NOVELTY - The separator has a sum room (1) connected with a biogas inlet and a methane outlet (3). A bottom side of the sum room is connected with a carbon dioxide air outlet (4). The methane outlet is connected with a methane compressor fan (5). The carbon dioxide air outlet is connected with a carbon dioxide compressor fan (6). The methane compressor fan and the carbon dioxide compressor fan are connected with an automatically power switch (7). Power ratio of the methane compressor fan and the carbon dioxide compressor fan is 65:35.    USE - Methane marsh gas and carbon dioxide gravity type separator.    ADVANTAGE - The separator can effectively separate methane marsh gas and carbon dioxide at low cost and discharge harmful gas and atmosphere waste by using a simple equipment. The separator is environment-friendly, and saves power energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a methane marsh gas and carbon dioxide gravity type separator. '(Drawing includes non-English language text)'    Sum room (1)    Methane outlet (3)    Carbon dioxide air outlet (4)    Methane compressor fan (5)    Carbon dioxide compressor fan (6)    Automatically power switch (7)
NOVELTY - The new type utility claims have one kind aerobic baffle device, the aerobic baffle device comprises a water inlet pipe and a water outlet pipe, a water inlet pipe and between the water out pipe set with one reaction container, internal of the reaction container by a plurality of guide flow plate is divided into several mutually connected in series of the reaction unit, the response unit internal of one guide plate is divided into aerobic reaction area and settlement zone, bottom of the aerobic reaction area provided with aeration device, the settlement of inclined plate layer is located on the inclined plate and lower layer part is buffering layer composed of. The utility model is new type and in aerobic reaction area, organic object in sewage by the microorganism full contact and then removing to obtain, when sewage enter into settlement zone, then providing to precipitate and place according to the shallow sediment " theory, settlement, and micro-sludge entrained in sewage to ensure the standard of the water outlet water quality suspended substance, thus no need in follow-up processing when discharged to sediment pool for precipitate again, make process simplify, production cost reducing.
NOVELTY - Organic fertilizer made from a mixture of guano, manure, leaf compost, kapok seed, straw compost and sea mud, or manure, rice straw and compost in a weight ratio of 1:1:1, is claimed.    USE - The organic fertilizer is useful for improving soil quality by improving the physical, chemical and biological properties of soil. No biological data given.    ADVANTAGE - The organic fertilizer: is simple; utilizes the raw materials which do not reduce the functionality of fertilizer; has a humidity of 20%, nitrogen-phosphorus-potassium grade of 5%, and black-brown colored, odorless and crumb structure; is formed from the mixture (preferably without sea mud) which exhibits best result (claimed) such as highest grade ergo; improves soil and water quality; reduces the salinity level of the soil; and makes the soil pH suitable for growth and increase the nutrients availability, preferably nitrogen-phosphorus-potassium level in soils that is affected by salt.
NOVELTY - Synthesizing tranilast, comprises (a) carrying out Knoevenagel reaction of 3,4-dimethoxybenzaldehyde and malonic acid in the presence of a weak base, to generate 3,4-dimethoxy cinnamic acid; (b) carrying out condensation reaction of 3,4-dimethoxy-cinnamic acid and methylanthranilate in presence of acylated condensing agent, to obtain tranilast methyl ester; and (c) hydrolyzing the tranilast methyl ester in presence of an inorganic base.    USE - The method is useful for synthesizing tranilast (claimed).    ADVANTAGE - The method has short process, simple operation, produces high yield product, and reduces the production cost and pollutant discharge.
NOVELTY - A diesel fuel contains 50-95 parts mass methanol, 5-10 parts mass diesel oil, 0.2-1 part mass flame retardant, 0.2-0.7 part mass synergistic agent, 0.1-0.3 part mass solvent, 0.05-0.45 part mass carbon reduction agent, 0.05-0.3 part mass smoking agent, 0.15-0.35 part mass odor agent, 0.05-0.25 part mass cleaning agent, 0.05-0.2 part mass noise reduction agent and 0.05-0.2 part mass anti-freezing agent.    USE - Diesel fuel (claimed).    ADVANTAGE - The diesel fuel is environmentally-friendly, and has excellent combustion rate, energy efficiency and combustion quality, uniform miscibility of components, low smoke, low pungent odor and low noise.
NOVELTY - The device has a dry fermentation mechanism (1) that is comprised with dry fermentation tank (11). The side wall of the lower portion of the dry fermentation tank is provided with discharge pipe. The side wall of upper portion of the dry fermentation tank is provided with first gas guide tube (15). The wet fermentation mechanism (2) is provided with wet fermentation tank (21) which is integrated with dry fermentation tank, and connected with heat exchanger. The side wall of upper portion of wet fermentation tank is set with second gas guide tube (24) and feeding pipe.    USE - Two-stage marsh gas fermentation device.    ADVANTAGE - The volume of the gas production rate is increased. The manufacturing cost of the marsh gas fermentation device is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the two-stage marsh gas fermentation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the marsh gas fermentation device.    Dry fermentation mechanism (1)    Wet fermentation mechanism (2)    Dry fermentation tank (11)    Air guide tubes (15,24)    Wet fermentation tank (21)
NOVELTY - The device has a power signal collecting module connected with a signal process circuit. A single chip is connected with a power supply cabinet that is connected with a control circuit plate. A hydrogen tank valve switch circuit is connected with a hydrogen fuel cell. The power signal collecting module is connected with the power supply cabinet. A signal acquisition module is formed as an xn02TH100HUMA-type air humidity sensor. The single chip is formed as an Atmel89C51-type.    USE - Hydrogen fuel cell air humidity detection device.    ADVANTAGE - The device avoids generating danger.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating operation of a hydrogen fuel cell air humidity detection device. '(Drawing includes non-English language text)'
NOVELTY - Inner power air pressure type automatic intermittent circulator. It is of plenum 11, water level control valve sum 6, 12, air inlet (water) pipe 3, relux tube 5, a check valve 14, to enter into digestion cell 13 bottom are composed of circulation loop. When closing water level control valve sum 6 biogas sum sum by seal 4, 12, through air inlet (water) pipe 3, continuously entering into plenum 11 inside, using plenum 11 within the pressure continuously enlargement to force the plenum 11 within the material liquid through relux pipe 5, a check valve 14, to enter into digestion cell 13 bottom. When in plenum 11 water low position to set water level when the water level control sum valve 6 is automatically opened, inner plenum gas is continuously discharging, when sum box 11 inside the water level to the set low water level when the water level control sum valve 6 is automatically opened, plenum 11 pressure reducing, area upper part of water through air inlet pipe 3, water is sucked, to set high water level when the water level control deflation valve 6 is automatically closed. Entering into the following one circulator wheel drainage, discharge the water circulation, realize to have power in automatic intermittent circulation.