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150results about How to "Good separation and purification effect" patented technology

Efficient separation and purification method for multi-residue sulfonamide antibiotics in biological samples

The invention relates to a method for efficiently separating and purifying multiresidue sulfonamide antibiotics in a biological sample. The method is characterized by comprising the following steps of: (1) preparing a molecular imprinted polymer, comprising the steps of burdening according to the mol ratio of template molecule to functional monomer to cross linking agent of being 1: (2-8): 25 and obtaining the molecular imprinted polymer with special identification function to the sulfonamide antibiotics by adopting a body polymerization method; (2) weighing certain amount of biological sample to be separated into a mortar, grinding the biological sample by the mortar, adding right amount of the molecular imprinted polymer, and further homogenating to obtain a homogenated sample, wherein the weight ratio of the biological sample to be separated to the molecular imprinted polymer is 2: (1-5), and (3) placing the homogenated sample in a solid phase extraction column, sequentially rinsing with 2.0-4.0ml of water, 2.0-4.0ml of 10wt% acetonitrile aqueous solution, and then eluting with 3.0-5.0ml of methanol/methanoic acid mixed solution; and separating the sulfonamide antibiotics from the biological sample to be separated by being instantly dissolved in the methanol/methanoic acid mixed solution. The method provided by the invention has wide selectivity and good separation and purification effect.
Owner:NINGBO UNIV

Radial-flow magnetic wastewater separative purification equipment

The invention discloses radial-flow magnetic wastewater separative purification equipment which comprises a frame, a water tank, a fluid connector, a residue scraping mechanism and a transmission mechanism, wherein the fluid connector, the residue scraping mechanism and the transmission mechanism are arranged on the water tank which is disposed on the frame. The equipment is characterized in thata hollow shaft is arranged in the water tank through a bearing block and provided with a plurality of magnetic disks, at least one end of the hollow shaft is open, and the open end and an external pipeline are in a dynamic sealed structure. The hollow shaft is provided with a plurality of through holes communicated with a cavity channel of the hollow shaft, and the residue scraping mechanism comprises a residue scraping component and a residue conveying component. Compared with existing semi-immersed disk type magnetic separators in advection or streaming modes, the equipment has the advantages that fully-immersed operation of magnetic disks is realized by means of radial flows, is lower in investment cost, smaller in occupied area, high in impact load bearing capacity and lower in energyconsumption, and is new-generation disk type magnetic separative purification equipment.
Owner:CHENGDU YUANRONG ENVIRONMENTAL TECH +1

Method for microwave-assisted reverse micelle separation and purification of kidney bean agglutinin

The invention discloses a method for microwave-assisted reverse micelle separation and purification of kidney bean agglutinin, and relates to a separation and purification method of the agglutinin, aiming at solving the problems of low ratio, high cost, more processes and long time for separation and purification of the kidney bean agglutinin. According to the method for the microwave-assisted reverse micelle separation and purification of the kidney bean agglutinin, the agglutinin is directly separated and purified from kidney bean agglutinin water extract; and the method comprises a pre-extraction process and a back extraction process. Under an auxiliary effect of microwave, water-soluble protein in kidney bean is quickly dissolved into the water extract, so that the dissolubility is greatly improved, and the leaching time is shortened. Based on a liquid-liquid extraction principle, the selectivity of extraction is improved, and high-efficiency pre-extraction and back extraction of the kidney bean agglutinin can be realized. By applying a reverse micelle extraction technology, a better separation and purification effect can be achieved with only the pre-extraction and back extraction steps; the method has simple steps and is convenient to operate; and the pre-treatment time can be greatly shortened in combination with microwave assistance so as to save the cost.
Owner:HARBIN INST OF TECH

Novel production process for total flavones of hippophae rhamnoides

The invention discloses a novel production process for total flavones of hippophae rhamnoides. The process comprises the steps as follows: washing raw materials; adding into a feeding hopper; rotating a mainframe of an extraction tank set; enabling materials to be fed into the front end of the extraction tank set backwardly and slowly; at the same time, enabling extracting solvents to enter into extraction tanks from a liquid inlet pipe at the tail end of the extraction tank set, penetrate through the moving materials from the rear ends of the tanks and flow to the front ends; and enabling the solid phase materials and the liquid phase materials to be fully contacted in the inverse motion so as to extract effective ingredients from the medicinal materials. Dregs are forcedly conveyed to a discharge hole for discharge through a discharge conveyer and squeezed by a special squeezer to squeeze out residual liquor in the dregs from the tissues of the medicinal materials so as to reduce the content of the residual liquor in the dregs. The extraction efficiency is higher and the extraction process is safer. The macroporous adsorption resin and the silica column chromatography for purification are selected and used at the same time, so that the separation effect is better. The finished total flavones of hippophae rhamnoides with the highest yield of 2% and the content of more than 70% can be obtained.
Owner:DAXINGANLING LINGOBERRY BOREAL BIOTECH CO LTD

Production technology for extracting usnic acid from usnea longissima

The invention discloses a production technology for extracting usnic acid from usnea longissima. The technology comprises the steps that a raw material is subjected to coarse grinding, and fed in from a feeding hopper; an extraction tank unit host rotates to slowly push the material from the front end of a unit backwards; an extraction solvent enters an extraction tank from a liquid inlet tube at the tail end of the unit, passes through the moving material from the back end of the tank, and flows towards the front end; and solid and liquid substances are contacted fully in an inverse motion, so that effective components in the medicinal material are extracted. Dregs are forcibly pushed to a dreg discharge port by a discharge transport and then discharged; a special juice squeezer squeezes the dregs; residual medicine liquor in the dregs is squeezed out of a medicinal material tissue; and the content of the residual medicine liquor in the dregs is reduced. The extraction efficiency is higher, and the extraction is more complete. The method adopts a continuous extraction tank unit for extraction, and is combined with a silica gel column chromatography for purification, so that a separating effect is better. Finished usnic acid with a maximum yield of 1% and the content above 95% can be obtained.
Owner:DAXINGANLING LINGOBERRY BOREAL BIOTECH CO LTD

Preparation method of drug-resistant pseudomonas aeruginosa broad-host range phage

The invention discloses a preparation method of drug-resistant pseudomonas aeruginosa broad-host range phage, which relates to a preparation method of phage and solves the problem of poor separation and purification effect in the traditional separation method of the pseudomonas aeruginosa phage. The method comprises the following steps: 1, selecting a sewage sample; 2, preparing a lysis solution; 3, carrying out mixed cultivation on the lysis solution and a pseudomonas aeruginosa host cell suspension to obtain a mixed solution; 4, preparing a single phage plaque; and 5, inoculating the phage into a pseudomonas aeruginosa-containing culture medium, culturing until the pseudomonas aeruginosa is completely dissolved, and finally filtering. The preparation method of pseudomonas aeruginosa phage has the advantages of simple operation, good separation and purification effect and no phage breakage. The prepared drug-resistant pseudomonas aeruginosa broad-host range phage can be used for manufacturing autoimmune (vaccines) biological agents for treating diseases caused by the infection of drug-resistant pseudomonas aeruginosa, can be especially used as a topical spray for treating epidermal infectious diseases, and can avoid the drug-resistant pseudomonas aeruginosa produced by the use of antibiotics.
Owner:INST OF MICROBIOLOGY HEILONGJIANG ACADEMY OF SCI

Liquid-phase synthesis method of eptifibatide

The invention relates to a liquid-phase synthesis method of eptifibatide as a polypeptide medicament and belongs to the technical field of synthesis of polypeptides. According to the technical scheme, the liquid-phase synthesis method comprises the following steps: (1) synthesizing a peptide fragment Mpa(R1)-Lys(R2)-Gly-OH; (2) synthesizing a peptide fragment H-Asp(R3)-Trp-Pro-Cys(R4)-NH2; (3) condensing the peptide fragment Mpa(R1)-Lys(R2)-Gly-OH and the peptide fragment H-Asp(R3)-Trp-Pro-Cys(R4)-NH2 to obtain a linear peptide Mpa(R1)-Lys(R2)-Gly-Asp(R3)-Trp-Pro-Cys(R4)-NH2; (4) cyclizing the linear peptide Mpa(R1)-Lys(R2)-Gly-Asp(R3)-Trp-Pr-Cys(R4)-NH2 to form an intramolecular disulfide bond to obtain a side chain protected cyclopeptide; (5) removing a side chain protecting group of the cyclopeptide; and (6) converting a side chain amino group of the cyclopeptide Lys into a guanidine group to obtain the eptifibatide. According to the liquid-phase synthesis method of the eptifibatide, an initiating raw material, namely an Fmoc-Har-OH special amino acid derivative is avoided, a condition and method for converting the amino group of the cyclopeptide into the guanidine group are established, and a raw material reagent is low in cost and easily obtained, so that the product cost is effectively reduced and the production benefit is remarkably increased.
Owner:山东博创生物科技有限公司

Micro-fluidic chip for enriching and purifying CTCs (circulating tumor cells)

The invention discloses a micro-fluidic chip. The micro-fluidic chip comprises positioning holes located in four corners of a chip body, a sample adding hole, a sample reaction cavity, a physical screening flow channel, a liquid waste flow channel, a liquid waste collecting cavity, a magnetic adsorption cavity plated with a magnet on the upper surface, a product flow channel, a product collectingcavity and a product absorption hole, wherein the sample reaction cavity and the magnetic adsorption cavity are communicated through the physical screening flow channel; the magnetic adsorption cavityand the product collecting cavity are communicated through the product flow channel; the lower side wall of the physical screening flow channel is communicated with the liquid waste flow channel through a notch formed in the lower side wall. The invention further discloses a method for enriching and purifying CTCs (circulating tumor cells) by adopting the micro-fluidic chip. An experiment can becompleted by only one centrifugal machine, the operation is fast and simple, an expensive EpCAM antibody is not needed, and the cost is relatively low; the obtained CTCs not only expresses the type ofthe EpCAM antibody, but also has better separation and purification effects, no immunomagnetic beads exist on the surface, and biological activity of the micro-fluidic chip is better.
Owner:苏州绘真医学检验有限公司 +2

Method for preparing saikoside from bupleurum longiradiatum

The invention discloses a method for preparing saikoside from bupleurum longiradiatum. The method comprises the steps that a raw material is subjected to coarse grinding, and fed in from a feeding hopper; an extraction tank unit host rotates to slowly push the material from the front end of a unit backwards; an extraction solvent enters an extraction tank from a liquid inlet tube at the tail end of the unit, passes through the moving material from the back end of the tank, and flows towards the front end; and solid and liquid substances are contacted fully in an inverse motion, so that effective components in the medicinal material are extracted. Dregs are forcibly pushed to a dreg discharge port by a discharge transport and then discharged; a special juice squeezer squeezes the dregs; residual liquor in the dregs is squeezed out of a medicinal material tissue; and the content of the residual liquor in the dregs is reduced. The extraction efficiency is higher, and the extraction is more complete. The method adopts a continuous extraction tank unit for extraction, and is combined with a silica gel column chromatography for purification, so that a separating effect is better. Finished saikoside with a maximum yield of 4% and the content above 95% can be obtained.
Owner:DAXINGANLING LINGOBERRY BOREAL BIOTECH CO LTD

A kind of separation method of chenodeoxycholic acid and ursodeoxycholic acid

The invention discloses a method for separating chenodeoxycholic acid from ursodesoxycholic acid, which belongs to the technical field of biochemical separation and is characterized by comprising the following steps in turn: (1) preparing column loading solution, namely dissolving mixture of ursodesoxycholic acid and chenodeoxycholic acid in alkaline aqueous solution according an equivalence ratio of 1:2.5, regulating the pH value of the solution to 7 to 8, and diluting deionized water till the solid content is 10 to 20 percent; (2) loading onto a column for absorption, namely pumping the column loading solution into a resin column filled with nonpolar porous synthetic absorbent; (3) desorbing, namely preparing eluting solution by using water soluble organic solvent, and pumping the eluting solution into the resin column for desorbing; and (4) performing post-treatment, namely concentrating under vacuum, recovering solvent, adding acid solution into the concentrated product to regulate the pH value to 2 to 3, precipitating, filtering, washing till the pH value is 7, drying, crystallizing and drying under vacuum to obtain a finished product. The method has the advantages that: the macroporous resin has high separation and purification performance and high accuracy; the ursodesoxycholic acid is separated from chenodeoxycholic acid with high yield; the process is simple; the production cost is low; and the industrial production efficiency is high.
Owner:上海华震科技有限公司

Production method for extracting hyperin from pyrola rotundifolia

The invention discloses a production method for extracting hyperin from pyrola rotundifolia. The method comprises the steps that raw materials are subjected to coarse grinding and then put in from a feeding hopper; an extraction tank unit host rotates; the materials are slowly pushed from the front end of a unit backwards; an extracting solvent enters an extracting tank from a liquid inlet tube at the tail end of the unit, passes through the moving materials from the rear end of the tank, and flows to the front end; and solid and liquid substances are sufficiently contacted in a reverse motion, so that active ingredients in medicinal materials are extracted. Dregs are forcibly pushed to a slag hole by a discharge transport and then discharged, a special juice squeezer extrudes the dregs and extrudes residual liquor in the dregs out of a medicinal material tissue, the residual liquor content of the dregs is reduced, the extraction efficiency is higher, and the extraction is more complete. The production method adopts continuous extraction and multi-stage extraction, and is combined with silicagel column chromatography for purification, the separation effect is better, and the finished hyperin with a maximum yield of 0.6% and content of above 95% can be obtained.
Owner:DAXINGANLING LINGOBERRY BOREAL BIOTECH CO LTD

Short flow process for preparing high-purity cobalt from low-content nickel-cobalt bioleaching solution

The invention discloses a short flow process for preparing high-purity cobalt from a low-content nickel-cobalt bioleaching solution. The short flow process for preparing the high-purity cobalt from the low-content nickel-cobalt bioleaching solution comprises the following steps that (1) a combined extractant is added into a diluent Mextral DT100 to prepare an organic phase; (2) co-extraction is carried out on the nickel-cobalt bioleaching solution at an initial pH of 1.5 to 3.0 and an equilibrium pH of 3.0 to 4.0; (3) sulfuric acid is added in the organic phase for back extraction to realize nickel-cobalt preconcentration and deep purification; (4) double-extractant extraction resin is prepared; and (5) a HAc-NaAc buffer solution with pH of 3.0 to 5.5 and the sulfuric acid with pH of 1.0 to 3.5 are separately used for two-stage gradient leaching, and a cobalt-containing rich solution obtained by leaching is concentrated and then subjected to electrolytic deposition to obtain a cathodecobalt product. The short flow process for preparing the high-purity cobalt from the low-content nickel-cobalt bioleaching solution has the advantages of multilevel and high efficiency, high selectivity, good mass transfer effect and the like, the purification separation purification efficiency of the cobalt solution is improved, and simple process, easy operation and little environmental pollution are achieved.
Owner:GRIMAT ENG INST CO LTD

Method for preparing 3,4-dichloro bromobenzene

The invention belongs to the chemical engineering field, and particularly discloses a method for preparing 3,4-dichloro bromobenzene. The method comprises steps of adding reduced iron powder into the raw material o-dichlorobenzene, inletting bromine water under certain pressure and temperature, and carrying out bromination reaction in a bromination kettle; carrying out multistage crystallization on the crude bromized 3,4-dichloro bromobenzene through solution, so as to purify the 3,4-dichloro bromobenzene, wherein the crude bromized 3,4-dichloro bromobenzene is crystallized by at least one stage, generally by multiple stages, namely, from one stage to three stages, so that a complete cycle of crystallization and purification of the 3,4-dichloro bromobenzene product is formed. The method has the main beneficial effects that the product is not polluted by foreign solvents or other materials, for the byproduct 2,3- dichloro bromobenzene generated in preparation of 3,4-dichloro bromobenzene through o-dichlorobenzene is used as the solvent; particularly, reduction of the yield of 3,4-dichloro bromobenzene caused by intensified side reaction of the 2,3- dichloro bromobenzene due to rectification high temperature is avoided; the method has the characteristics of high yield of the product, high purity and high production efficiency.
Owner:福建桦智工程技术有限公司

Process and system for producing cyclohexane plasticizer by liquid phase hydrogenation of o-benzene plasticizer

The invention relates to a process and a system for producing a cyclohexane plasticizer by liquid phase hydrogenation of an o-benzene plasticizer. The process for preparing a cyclohexane plasticizer by liquid phase hydrogenation of an o-benzene plasticizer comprises the following steps: (1) heated inert gas is introduced into the bottom of a reduced pressure distillation tower in a pulse pneumaticconveying manner; and (2) a plasticizer product is preheated and then enters the bottom of the reduced pressure distillation tower, and the inlet of the plasticizer product on the reduced pressure distillation tower is higher than the inlet of the inert gas, so that the plasticizer product is mixed and heated with the rising inert gas flow in the downward flowing process, and the target product is separated from the by-product. According to the process and the system disclosed by the invention, heated inert gas is fed into the reduced pressure distillation tower in a pulse manner, and the characteristic that the flow of inert gas is changing is utilized to better simulate the characteristics of fluidization, mixing and heating at the bottom of the reduced pressure distillation tower, so that better mixing, heating, separation and purification effects on the plasticizer product are realized.
Owner:ZHENGZHOU RAILWAY VOCATIONAL & TECH COLLEGE
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