Patents
Literature
Patsnap Copilot is an intelligent assistant for R&D personnel, combined with Patent DNA, to facilitate innovative research.
Patsnap Copilot

56 results about "Chromatography liquid" patented technology

Liquid chromatography (LC) refers to any chromatographic procedure in which the moving phase is a liquid, in contrast to the moving gas phase of gas chromatography. Traditional column chromatography (whether adsorption, partition, or ion-exchange), thin-layer and paper chromatography, and modern LC are each examples of liquid chromatography.

Liquid Chromatography Apparatus

A multi-column liquid chromatography system (10) for performing a plurality of liquid chromatography separations in parallel is based on a column plate structure (12) having parallel grooves (20) formed in a surface (22) of a plate (18), a cover sheet (40) bonded to the surface (22) to cover the grooves (20) and a stationary phase (38) contained in each covered groove (20). Through holes (24, 26) in the plate (18) define respective inlets (24) for the chromatography columns (14) and flow cells (16) at outlets, with the cover sheet (40) providing an optically transparent end wall for the flow cells (16) and another cover sheet (42) bonded to the opposite surface (30) of the plate (18) providing the other optically transparent end wall for the flow cells (16). Thus merely three parts need be provided for a structure for providing the chromatography columns, that is, a plate having grooves and through holes plus two cover sheets. The chromatography system (10) additionally includes a pumping system (46) comprising a syringe pump (48) for each column (14), an optical system (28) for transmitting analytical radiation through the flow cells (16) and a fraction collection sheet (110) containing wells (112) which is fed past outlets (34-35) from the column plate structure (12).
Owner:VARIAN AUSTRALIA PTY LTD

Method for extracting beta-thymidine from fermentation liquid

The invention discloses a method for extracting beta-thymidine from fermentation liquid. The method comprises the following steps: (1) preheating the fermentation liquid; (2) performing microfiltration on the fermentation liquid; (3) performing ultrafiltration on the microfiltration liquid; (4) performing electrodialysis on the ultrafiltration liquid; (5) concentrating the electrodialysis liquid; (6) performing chromatography on the concentrated liquid; and (7) concentrating and crystallizing the chromatography liquid. According to the method, a membrane separation technique, an electrodialysis technique and a chromatography separation technique are implemented in the extraction process of the beta-thymidine fermentation liquid, so that a good impurity removal effect can be achieved, and the process is simple, convenient and environment-friendly and high in automation degree. By adopting the extraction process disclosed by the invention, the purity of the liquid phase of a beta-thymidine product is greater than or equal to 98.5%, the external standard content is greater than or equal to 98.5, the total yield is greater than or equal to 70%, industrial application of extracting beta-thymidine from the fermentation liquid is achieved, and good economic benefits and industrial popularization prospects can be achieved.
Owner:NANCHANG UNIV

Purification method of human immunoglobulin for intravenous injection

The invention discloses a purification method of human immunoglobulin for intravenous injection. The purification method is used for purification of a secondary sedimentation ingredient. The purification method of the human immunoglobulin for the intravenous injection is characterized by comprising the following steps of: S1, dissolve: dissolving the secondary sedimentation ingredient with water for injection, and stirring for 2-4h at 2.0-8.0 DEG C to form a dissolve liquid, S2, filtration: filtering the dissolve liquid with a 0.45 micrometers filter membrane and then with a 0.2 micrometers filter membrane to form a filtrate, S3: filtrate adjustment: adjusting a pH (potential of hydrogen) of the filtrate to 5.60-6.00, a protein concentration to 10-13g/L, and conductivity to 0.2-1.90ms/cm to form a pre-chromatography liquid, S4, chromatography: performing chromatography with strong anion exchange gel, flushing the gel before the chromatography for balancing to allow a difference betweena pH of the gel and a pH of the liquid before the chromatography to be from -0.10 to 0.10, performing gel chromatography sample loading at a linear flow rate of 0.5-1.5cm/min and chromatography loading capacity of not exceeding 600g/L, and collecting a liquid after the chromatography. The method is simple and controllable, and greatly reduces a content of IgA (immunoglobulin A) and IgM (immunoglobulin M) in the human immunoglobulin for the intravenous injection.
Owner:HUALAN BIOLOGICAL ENG CHONGQING +1

New SMB Process

The present invention provides a chromatographic separation process for recovering a polyunsaturated fatty acid (PUFA) product from a feed mixture, which process comprises the steps of: (i) purifying the feed mixture in a first separation step in a simulated or actual moving bed chromatography apparatus having a plurality of linked chromatography columns containing, as eluent, an aqueous organic solvent, to obtain an intermediate product; and (ii) purifying the intermediate product obtained in (i) in a second separation step using a simulated or actual moving bed chromatography apparatus having a plurality of linked chromatography columns containing, as eluent, an aqueous organic solvent, to obtain the PUFA product; wherein (a) the first and second separation steps are carried out sequentially on the same chromatography apparatus, the intermediate product being recovered between the first and second separation steps and the process conditions in the chromatography apparatus being adjusted between the first and second separation steps such that the PUFA product is separated from different components of the feed mixture in each separation step; or (b) the first and second separation steps are carried out on separate first and second chromatography apparatuses respectively, the intermediate product obtained from the first separation step being introduced into the second chromatography apparatus, and the PUFA product being separated from different components of the feed mixture in each separation step.
Owner:BASF PHARMA CALLANISH

Method for recovering 16-dehydropregnenolone acetate from 16-dehydropregnenolone acetate mother liquor

InactiveCN103554208AApplication utilization rate is highLow priceSteroidsDehydropregnenolone acetateChromatography liquid
The invention relates to a method for recovering 16-dehydropregnenolone acetate from a 16-dehydropregnenolone acetate mother liquor, wherein the method is intended to provide the method with advantages of simple technology, high recovery rate and good product quality. The method for recovering 16-dehydropregnenolone acetate from the 16-dehydropregnenolone acetate mother liquor comprises the following steps of: mother liquor condensation, solvent extraction, chromatography to remove impurities, condensation of a chromatography liquid, refining, crystallization, centrifugation and drying, to obtain 16-dehydropregnenolone acetate. The method for recovering 16-dehydropregnenolone acetate from the 16-dehydropregnenolone acetate mother liquor can make an overall yield of the 16-dehydropregnenolone acetate reach 72%, raising 4-7% compared with a traditional technology; a used reagent belongs to a common chemical product, and has advantages of easy availability, low cost, simple technology operation and convenient industrialization; and the method is used for recovering the 16-dehydropregnenolone acetate from the 16-dehydropregnenolone acetate mother liquor, wherein the purity of the 16-dehydropregnenolone acetate obtained after refining is larger than 99%, the obtained 16-dehydropregnenolone acetate can be directly used as a product, and a secondary mother liquor can be reused into the 16-dehydropregnenolone acetate production.
Owner:XIANGXI HUALI PHARMA

Separation and purification method of pneumocandin B0 serine analog

The invention relates to a separation and purification method of a pneumocandin B0 serine analog. The separation and purification method comprises the following steps of (a) performing chromatographyenrichment for the first time through polymer substrate chromatogram fillings, performing isocratic elution, and collecting parts of which the purity is greater than 30%; (b) performing chromatographyenrichment for the second time through chromatogram fillings having hydrophilic effects, performing isocratic elution, and collecting parts of which the purity is greater than 60%; (c) performing chromatography enrichment for the third time through antiphase silica gel substrate chromatogram fillings, performing isocratic elution, and collecting parts of which the purity is greater than 80%; and(d) after purifying for the third time, performing decompressed concentration on chromatography liquid of which the pneumocandin B0 serine analog purity is greater than 80%, removing a solvent, and performing freeze-drying so as to obtain the pneumocandin B0 serine analog. Through the adoption of the preparation method disclosed by the invention, the pneumocandin B0 serine analog of which the purity is greater than 80% is subjected to structure identification, and a base is established for further performing biological activity screening or performing biological activity screening after structure modification.
Owner:ZHEJIANG MEDICINE CO LTD XINCHANG PHAMACEUTICAL FACTORY

Liquid chromatography high-pressure resistant gradient valve and liquid chromatography liquid inlet system

The invention discloses a liquid chromatography high-pressure resistant gradient valve and a liquid chromatography liquid inlet system. The liquid chromatography high-pressure resistant gradient valvecomprises a valve body and at least two high-pressure valves, wherein a mixing outlet and at least two interfaces are formed in the valve body, and each the interface is communicated with the mixingoutlet; each the interface is respectively connected with one of the high-pressure valves, each the high-pressure valve comprises an outer shell, a valve core, an elastic holding piece and an electriccontrol driving piece, a liquid inlet cavity, a liquid outlet cavity and a communication cavity which are sequentially communicated are formed in each the outer shell, a liquid inlet is formed in each the liquid inlet cavity, a liquid outlet is formed in each the liquid outlet cavity, and each the liquid outlet is connected with each the interface; the valve cores are arranged in the liquid outlet cavities in a movable manner; the elastic holding pieces are arranged in the liquid outlet cavities, and the elastic holding pieces are abutted against the valve cores to block the valve cores at the communication cavities; and the electric control driving pieces are arranged on the outer shells and are matched with the valve cores to drive the valve cores to move, and the electric control driving pieces drive the valve cores to open the communication cavities when receiving liquid inlet information. The liquid chromatography high-pressure resistant gradient valve has the characteristics ofhigh pressure resistance and gradient accuracy.
Owner:ANHUI WAYEE SCI & TECH CO LTD

Method for purifying loropetalum chinense flower red pigment by using aluminum oxide-calcium carbonate composite adsorbent

The invention discloses a method for purifying loropetalum chinense flower red pigment by using an aluminum oxide-calcium carbonate composite adsorbent. The method comprises the following steps: 1) preparing a loropetalum chinense flower red pigment concentrated solution, namely, firstly, extracting a loropetalum chinense flower red pigment extract from loropetalum chinense pollen powder, and further concentrating the loropetalum chinense flower red pigment extract, thereby obtaining the loropetalum chinense flower red pigment concentrated solution; and 2) purifying the loropetalum chinense flower red pigment, namely, by taking aluminum oxide and calcium carbonate as a composite adsorbent, feeding the loropetalum chinense flower red pigment concentrated solution onto a column for adsorption, and eluting by using an eluent, thereby obtaining the a purified loropetalum chinense flower red pigment chromatography liquid. As activated neutral aluminum oxide and calcium carbonate with the mass ratio of 2:1 are adopted as the composite adsorbent, the separation effect on loropetalum chinense flower red pigment is good; the price is low, and the production period is short, and meanwhile the production cost is low, the production efficiency is high and the equipment investment is small as no complex equipment is needed.
Owner:CHANGSHA UNIVERSITY OF SCIENCE AND TECHNOLOGY

A method for extracting β-thymidine from fermentation broth

The invention discloses a method for extracting beta-thymidine from fermentation liquid. The method comprises the following steps: (1) preheating the fermentation liquid; (2) performing microfiltration on the fermentation liquid; (3) performing ultrafiltration on the microfiltration liquid; (4) performing electrodialysis on the ultrafiltration liquid; (5) concentrating the electrodialysis liquid; (6) performing chromatography on the concentrated liquid; and (7) concentrating and crystallizing the chromatography liquid. According to the method, a membrane separation technique, an electrodialysis technique and a chromatography separation technique are implemented in the extraction process of the beta-thymidine fermentation liquid, so that a good impurity removal effect can be achieved, and the process is simple, convenient and environment-friendly and high in automation degree. By adopting the extraction process disclosed by the invention, the purity of the liquid phase of a beta-thymidine product is greater than or equal to 98.5%, the external standard content is greater than or equal to 98.5, the total yield is greater than or equal to 70%, industrial application of extracting beta-thymidine from the fermentation liquid is achieved, and good economic benefits and industrial popularization prospects can be achieved.
Owner:NANCHANG UNIV

Liquid chromatography high pressure gradient valve and liquid chromatography inlet system

The invention discloses a liquid chromatography high pressure resistant gradient valve and a liquid chromatography liquid inlet system, wherein the liquid chromatography high pressure resistant gradient valve comprises: a valve body and at least two high pressure valves; the valve body is provided with a mixing outlet and at least two Each interface is connected to the mixing outlet; each interface is connected to a high-pressure valve, and the high-pressure valve includes: a shell, a valve core, an elastic retainer, and an electric control drive. The liquid inlet chamber has a liquid inlet, the liquid outlet chamber has a liquid outlet, and the liquid outlet is connected to the interface; the valve core is movably arranged in the liquid outlet chamber; the elastic holder is arranged in the liquid outlet chamber, The elastic retainer stops against the spool so that the spool is blocked in the communication cavity; the electric control drive is arranged on the casing and cooperates with the spool to drive the spool to move, and the electric control drive drives the spool when receiving the liquid inlet information. The spool opens the communication cavity. The liquid chromatography high pressure resistant gradient valve of the invention has the characteristics of high pressure resistance and gradient accuracy.
Owner:ANHUI WAYEE SCI & TECH CO LTD
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products