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54results about How to "The process is easy to scale up" patented technology

Novel peptide with angiotonin transferase restraining liveness and method of producing the same

The present invention discloses a method of using biological enzyme decomposition to prepare a hydrolysis compound containing peptide of angiotensin transfer enzyme inhibitory activity, and three novel peptides of high ACE inhibitory activity. For the hydrolysis compound containing peptide of angiotensin transfer enzyme inhibitory activity of the present invention, the oxhide rich in praline is used as the raw material; the product of ACE inhibitory activity IC50 equal to 0.168mg / m can be prepared through the compounding and hydrolysis of biological enzyme. After ultrafiltration, the IC50 is equal to 0.079mg / ml. The means of analysis and detection determines the peptides, ISVPGPM, LGPVGNPGPA and DLSFLPQPPQQ, containing high ACE inhibitory activity. The three peptide sections are novel peptide sections containing high ACE inhibitory activity. Therefore, the three peptides have potential function of lowering blood pressure. The compounding and decomposition of biological enzyme of oxhide is a peptide type hydrolysis product, has inhibitory effects on angiotensin transfer enzyme (ACE), and can be widely used for health food, functional food, auxiliary drugs for lowering blood pressure and other products; the peptide has broad market prospects.
Owner:EAST CHINA UNIV OF SCI & TECH +1

Lithium ion batteries cathode material recovery method

The invention belongs to the field of battery materials, and specifically relates to a method for recovering positive active materials from battery material offcuts and slurry. The method comprises the following steps of: filling positive plate or dry positive slurry to be recovered into a pulverizer, screening into a powder, putting the powder into a fluidized bed and removing impurities of conductive carbon and a binder; letting a gas pass through a cyclone separator on the top of the fluidized bed to remove entrained powder, passing through a fixed bed to remove harmful gases, heating and blowing into the fluidized bed for cyclic utilization, cooling the powder at the bottom, and sieving to obtain a qualified positive powder. According to the invention, the process flow is short; the powder is in a fluidization state in the fluidized bed during the process of heat treatment; and the gas and the powder fully contact with each other and the reaction is complete. Therefore, the problems of high impurity content in the product and low recovery rate in a traditional technology are fundamentally resolved; in addition, cobalt and lithium elements are simultaneously recovered, the recovery rate of an active substance reaches up to 94%, and simultaneously side-effect will not be exerted on the active substance and it selectrochemical properties.
Owner:DONGGUAN AMPEREX TECH +2

Low-cost, efficient and continuous tea saponin extraction process

The invention discloses a low-cost, efficient and continuous tea saponin extraction process. The low-cost, efficient and continuous tea saponin extraction process comprises steps as follows: (1) pretreated oil-tea meal is dried; (2) the tea meal with water content adjusted enters an extractor for continuous extraction; (3) extracted wet meal enters a DTDC (desoloventizer, toaster, dryer and cooler) type dryer with multiple material layers and is dried, after the moisture content of dried meal is adjusted, the meal is metered and packaged, and feed grade tea meal is obtained; (4) a tea saponin mixed solution discharged out of the extractor enters a cyclone device for separation; (5) a separated tea saponin concentrated solution is fed into a drying section for drying, and a tea saponin crude product is obtained. With the adoption of the process, the extraction efficiency of tea saponin is effectively improved, and the processing cost is effectively reduced; the tea saponin can be taken as a raw material for feed; the purity of the extracted saponin crude product is improved; large-scale extraction of the tea saponin is easier to realize, the processing benefits of by-products are effectively improved, and the technical bottleneck problem in the aspect of development of byproducts of tea oil is solved.
Owner:RES INST OF SUBTROPICAL FORESTRY CHINESE ACAD OF FORESTRY

Combined preparation process of sophora flavescens total flavone and sophora flavescens total alkaloid

The invention provides a combined preparation process of sophora flavescens total flavone and sophora flavescens total alkaloid. The combined preparation process comprises the following steps: crushing raw sophora flavescens; extracting by using low-carbon alcohol; concentrating an extraction solution into extract; dissolving the extract by using acid water to obtain an acid water layer and a solid; washing the solid with water till the solid is neutral; dissolving the solid with a proper amount of ethanol; separating a solution by using polyamide resin; eluting with acid alcohol; collecting eluate; concentrating and drying the eluate to obtain high-purity sophora flavescens total flavone; taking the acid water layer, blending with alkali and precipitating; filtering out precipitates, and dissolving the precipitates with acetone; adding ammonia water into an acetone solution, and separating out and crystallizing; filtering out crystals, and refluxing and dissolving the crystals with 80-95% ethanol to obtain the sophora flavescens total alkaloid. The combined preparation process is easy to operate; the utilization ratio of the raw material is high; the sophora flavescens total flavone and the sophora flavescens total alkaloid with relatively high purity are prepared; and the combined preparation process is easy to expand.
Owner:苏州宝泽堂医药科技有限公司

LLarge scale human urine protein collection method

The invention discloses a large scale human urine protein collection method. The method comprises the following steps: placing absorption agents, which are used for absorbing urine proteins and have been packaged, in the places where urine will pass through to make the absorption agent be able to absorb the urine proteins in the urine; collecting the absorption agents which have absorbed the urine proteins; subjecting the collected absorption agents to a pretreatment; refrigerating and storing the pre-treated absorption agents; and transporting the absorption agents to a processing factory in batches to carry out urine protein desorption process to produce corresponding urine protein raw materials or urine protein products. The large scale human urine protein collection method is suitable for the mass industrial urine protein production, improves the processing amount of urine protein, reduces the transportation cost of absorption agents and the production cost of urine proteins, furthermore, the absorption agents containing urine proteins are subjected to a pre-treatment before storage, thus the urine protein activity is preserved, the urine protein degradation is reduced, the microorganism generation is reduced, so that the urine protein product quality is improved.
Owner:YANGZHOU AIDEA BIOTECH

Preparation method for collagen hydrogel

The invention discloses a preparation method for collagen hydrogel. The method comprises the following steps that (1) a collagen solution is prepared, specifically, a certain amount of collagen is weighed and put into a reaction kettle, a 0.05-0.5 mol/L organic acid solution with 40-200 times the weight of the collagen is added, and the solution is enabled to pass through a 50-400-mesh sieve repeatedly under the action of a peristaltic pump so as to reach a uniform state; (2) amino acid is added, specifically a certain amount of amino acid is added into the collagen solution prepared in the step (1), and the solution is continuously enabled to pass through a 50-400-mesh sieve repeatedly under the action of the peristaltic pump so as to reach a uniform state; (3) the pH is adjusted, specifically, the solution prepared in the step (2) is placed at a low temperature of 0-10 DEG C, solution replacement is carried out by adopting an ultrafiltration method, ultra-pure water or a buffer solution with the pH value of 6-8 is added in the ultrafiltration process, and ultrafiltration is continuously carried out until the difference value between the pH of permeate liquid and the pH of the added ultrapure water or the buffer solution is less than 0.2; and (4) irradiating is carried out, specifically, a sample prepared in the step (3) is subjected to split packaging and then is irradiated.The preparation method for the collagen hydrogel has the advantages that the uniform hydrogel can be prepared, and the problem of liquid precipitation after irradiation can be solved.
Owner:HEBEI COLLAGEN BIOTECH

Method for concurrent production of potassium chloride and mineralization fixation of CO2

The invention belongs to the comprehensive field of potassium fertilizer production and CO2 emission reduction, and provides a method for concurrent production of potassium chloride and mineralization fixation of CO2. The process steps comprise: (1) adopting potassium feldspar, calcium chloride and coal as raw materials, preparing materials, carrying out ball milling, and carrying out pressing molding or pelletizing; (2) conveying the molded material or the material balls into a rotary kiln from the kiln tail, conveying air into the rotary kiln from the kiln head, and controlling a residence time of the molded material or the material balls at a temperature range of 800-1000 DEG C to 20-40 min; (3) crushing the calcinated material, and adding water to carry out potassium leaching through the water; (4) adding water to the potassium leaching residue to carry out pulp conditioning, and introducing CO2 to carry out a mineralization reaction; (5) carrying out returning of the potassium leaching solution so as to be used for leaching of potassium from the calcinated material when the Baume degree of the potassium leaching solution is less than or equal to 29, and carrying out evaporation concentration on the potassium leaching solution to achieve the Baume degree of 42-42.5 when the Baume degree of the potassium leaching solution is more than 29, and cooling to carry out potassium chloride crystallization; and (6) cooling the potassium extraction mother liquor to carry out calcium chloride crystallization, and carrying out solid-liquid separation to obtain calcium chloride and the calcium extraction mother liquor.
Owner:SICHUAN UNIV

Conductive carrier self-supporting flower-shaped Co3V2O8 lithium ion battery negative electrode material and preparation

The invention discloses a conductive carrier self-supporting flower-shaped Co3V2O8 lithium ion battery negative electrode material and preparation, and belongs to the field of preparation and application of energy materials. In the composite material, flower-shaped Co3V2O8 uniformly grows on a conductive carrier. The flower-shaped Co3V2O8 is formed by laminating at least one sheet-shaped Co3V2O8.The preparation method of the composite material comprises the following steps: step 1, taking cobalt salt and urea as raw materials, and growing at least one layer of cobalt hydroxide as a precursoron a conductive carrier in situ by using a hydrothermal method; step 2, soaking the precursor template of the conductive carrier self-supporting cobalt hydroxide into the metavanadate solution for secondary hydrothermal treatment to obtain a conductive carrier self-supporting cobalt vanadium oxide composite material; and step 3, annealing the conductive carrier of the self-supporting cobalt-vanadium oxide in air to obtain the conductive carrier self-supporting flower-shaped Co3V2O8 composite material. The method is simple and feasible, the process can be enlarged, and the method can be appliedto the field of commercial lithium ion negative electrode materials.
Owner:BEIJING UNIV OF CHEM TECH

Fluid-bed reactor for oxido-reduction sintering of high calcium magnesium titanium slag

InactiveCN101117665AReduce axial backmixingImproved solid phase residence time distributionFluidised-bed furnacesProcess efficiency improvementOxido reductionMagnesium
The present invention relates to a fluidized bed reactor used for oxidizing and deoxidizing and baking high calcium magnesium titanium slag to remove calcium for improving the titanium inert solid grade, and comprises a cylindrical column material settlement section, a cylindrical column material reaction section, and a coniform column air preheating section. The main body of the cylindrical fluidized bed reactor is the cylindrical column material reaction section, and the top part is of a horn mouth shape, the top part of the horn mouth column body is connected with the cylindrical column material settlement section, the bottom end of the reaction is connected with the air preheating section. The upper part of the air preheating section is provided with a material feeding port, and the bottom part is arranged with an air distribution plate under which an air inlet is provided. The lower part of the material reaction is provided with a material discharging port, and the top part is provided with an air outlet. More than one baffle with holes is arranged in the material reaction. The present invention can make the residence time of particles of the high calcium magnesium titanium slag prolong following the increase of the grain size to satisfy the requirements of the reaction time of different grain sizes of particles.
Owner:INST OF PROCESS ENG CHINESE ACAD OF SCI

Method for concurrent production of potassium chloride and mineralization fixation of CO2

The invention belongs to the comprehensive field of potassium fertilizer production and CO2 emission reduction, and provides a method for concurrent production of potassium chloride and mineralization fixation of CO2. The process steps comprise: (1) adopting potassium feldspar, calcium chloride and coal as raw materials, preparing materials, carrying out ball milling, and carrying out pressing molding or pelletizing; (2) conveying the molded material or the material balls into a rotary kiln from the kiln tail, conveying air into the rotary kiln from the kiln head, and controlling a residence time of the molded material or the material balls at a temperature range of 800-1000 DEG C to 20-40 min; (3) crushing the calcinated material, and adding water to carry out potassium leaching through the water; (4) adding water to the potassium leaching residue to carry out pulp conditioning, and introducing CO2 to carry out a mineralization reaction; (5) carrying out returning of the potassium leaching solution so as to be used for leaching of potassium from the calcinated material when the Baume degree of the potassium leaching solution is less than or equal to 29, and carrying out evaporation concentration on the potassium leaching solution to achieve the Baume degree of 42-42.5 when the Baume degree of the potassium leaching solution is more than 29, and cooling to carry out potassium chloride crystallization; and (6) cooling the potassium extraction mother liquor to carry out calcium chloride crystallization, and carrying out solid-liquid separation to obtain calcium chloride and the calcium extraction mother liquor.
Owner:SICHUAN UNIV

Conductive graphene film and self-assembly preparation method thereof

The invention relates to a conductive graphene film and a self-assembly preparation method thereof. A graphene powder material and a dispersing aid are added into a reactor according to the mass ratioof 100-5: 1, then the mixture is added into a solvent, the mass-volume ratio of the solvent and graphene is 1-10: 1, the ultrasonic oscillation is performed for 30 minutes to 10 hours, the ultrasonicpower is between 20 and 300 W, and a graphene solution with good dispersion is obtained; and the graphene solution with good dispersion is transferred into a water bath with a temperature of between5 and 90 DEG C, the water bath temperature is lower than a boiling point of the solvent, the graphene solution is maintained in the water bath for 5 minutes to 3 hours, the graphene self-assembles ona gas-liquid surface to form a graphene film, and the graphene film is fished out from the liquid level and is dried at normal temperature to obtain the conductive graphene film. The square resistanceof the graphene film is within the range of between 5 and 3,000 omega/sq, the graphene film has good strength, and the thickness is between 2 and 100 mu m. The method has simple preparation process and easy operation; and the graphene film has the advantages of good conductivity and strength, controllable thickness, cuttable shape, adjustable scale, low cost, and easy process scale-up.
Owner:深圳清研紫光科技有限公司
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