1072results about "Amphoteric ion-exchangers" patented technology

The invention provides a method for immobilizing phosphonic acid betaine and phosphonic acid on polystyrene, which comprises the following steps: taking quaternary ammonium cation containing glycidyl ether as a spacer arm, carrying out ring-opening reaction on phosphite ester and glycidyl ether connected with the side chain of polystyrene in the presence of an alkali reagent catalyst, grafting phosphonate on polystyrene, and then carrying out acid catalytic hydrolysis on phosphonate to obtain the phosphonic acid betaine and phosphonic acid immobilized on polystyrene. The phosphonic acid and the phosphonic acid group betaine are immobilized on the surface of the polystyrene. The effect of introducing phosphonic acid and phosphonic acid betaine on polystyrene is generated; the adsorbent can be used for adsorption, enrichment and separation of rare earth ions and heavy metal ions, and also has an anion exchange function.

Described herein are methods of recovering lithium from dilute lithium sources. The methods include extracting lithium from an extraction feed using direct lithium extraction in an extraction stage to yield a lithium intermediate, performing one or more concentration operations, each concentration operation concentrating an input stream to yield an output feed, wherein the input stream is obtained from the lithium intermediate and / or the extraction feed is obtained from the output feed. At least one of the concentration operations includes a membrane separation operation having a plurality of reactors in series each having a semi-permeable membrane, such as a counter-flow reverse osmosis operation. Methods may also include generating a low TDS stream as a permeate from any of the one or more concentration operations, wherein the low TDS stream is recycled or used as fresh water.

Described herein are membrane assemblies for use in generating hydrogen and oxygen. The membrane assemblies include a cation exchange membrane, an anion exchange membrane, and a hydrophilic layer disposed between the anion exchange membrane and the cation exchange membrane.

The invention relates to a strong cation exchange chromatographic filler as well as a preparation method and application thereof. The strong cation exchange chromatographic filler comprises sulfonated poly (glycidyl methacrylate)-divinyl benzene microspheres. The strong cation exchange chromatographic filler provided by the invention can simultaneously show excellent separation selectivity on rare earth elements, and also has long-term stability and excellent cycle performance, so that the economic cost is reduced, and the strong cation exchange chromatographic filler has relatively high economic benefits and is green and environment-friendly.

A method is provided, comprising: obtaining, for a chromatography machine including a first dispersed plug flow reactor (DPFR) and a continuous stirred tank reactor (CSTR) prior to a column, and a second DPFR after the column, geometric measurements associated with the second DPFR; generating, by a processor, transport model parameters for a transport model associated with the second DPFR based on the geometric measurements; feeding a tracer molecule into the chromatography machine; capturing one or more tracer molecule measurements based on the tracer molecule traveling through the chromatography machine; and estimating, by the processor, based on the transport model associated with the second DPFR and the one or more tracer molecule measurements based on the tracer molecule traveling through the chromatography machine, one or more transport model parameters for a transport model associated with the first DPFR and the CSTR.

The present invention relates to the process to prepare recombinant lectin having amino acid sequence of SEQ ID NO:1, wherein the process comprises fed-batch fermentation of a clone in a host cell at specific feeding rate with carbon to Nitrogen ratio of 3:1 to 6:1. The invention also relates to the process of purification of recombinant lectin having amino acid sequence of SEQ ID NO: 1.

The invention discloses a human albumin binding peptide 1E3 and application of the human albumin binding peptide 1E3 in promoting purification of human albumin, and belongs to the technical field of polypeptides. The human albumin binding peptide comprises an amino acid sequence as shown in SEQ ID NO. 1; and / or an amino acid sequence of a fusion protein with the same function, which is obtained by connecting tag protein to the N terminal and / or C terminal of the amino acid sequence as shown in SEQ ID NO.1. The human albumin binding peptide has extremely high affinity with human albumin and can be used for separating and purifying a human albumin solution, and the purity of the purified human albumin far exceeds the pharmacopoeia standard and can reach 99.99% or above. The method is good in safety and stable in process, and has a wide application prospect in the aspect of separation and purification of the human albumin.

The invention relates to the technical field of pharmaceutical separation, and discloses a device, method and application of ursodeoxycholic acid preparation and purification. The device comprises a separation tank, wherein a batching center cylinder is rotatably installed inside the separation tank, and a plurality of elution tubes are arranged around the batching center cylinder. The batching center cylinder rotates forward, and centrifugal force is used to load adsorption resin into each elution tube. Then, the batching center cylinder rotates reversely, and the volume of each elution tube is poured out by anti-centrifugal force, so as to achieve a more convenient effect of replacing the adsorption resin. The replaced adsorption resin is cleaned outside the device and reused. The purification method and application thereof realize column loading, sample loading and elution in the separation tank in sequence without stopping the machine for operation, and simplify the column loading and column replacement operations, so as to solve the problem that the separation and purification process in the prior art is complicated and not suitable for batch production, so as to meet the industrial production requirements of solvent recycling.

The present invention relates to a system for capturing carbon dioxide from an air stream. The system includes a carbon dioxide capturing unit that includes a humidity / temperature adjusting unit with an evaporative cooling unit and a CO2 adsorbing unit. The CO2 adsorbing unit includes a sorbent column made of polyamine-Cu (II) complex resin. The humidity / temperature adjusting unit receives air stream from ambient atmosphere and process the air stream to obtain a humidity-adjusted air stream. The CO2 adsorbing unit receives the humidity-adjusted air stream to pass through the sorbent column. The sorbent column selectively adsorbs the CO2 from the humidity-adjusted air stream. The sorbent column is regenerated using an alkaline stream to separate the adsorbed CO2 from the sorbent column.

The invention belongs to the technical field of radioactive isotope separation and purification, and particularly relates to a device for separating and purifying carrier-free lutetium 177. Comprising a mounting rack, a salt transfer assembly arranged in the middle of the front side of the mounting rack, a valve assembly arranged in the middle of the rear side of the mounting rack, a separation and purification column arranged on one side of the salt transfer assembly, a sample injection system arranged on one side of the valve assembly, a fraction assembly arranged above the mounting rack and a waste liquid assembly arranged on one side of the mounting rack, the control terminal is used for controlling the sampling system and the on-off of valves in the valve assembly so as to control the flowing of liquid in the separation and purification device, so that the functions of ytterbium and lutetium separation, lutetium-to-salt concentration and ytterbium-to-salt recovery in the separation and purification device are realized. The problems that in the prior art, an overall device for separating and purifying carrier-free lutetium-177 is large in size and occupied area, the requirement for the automation control degree is high, and the service life of parts is short are solved.

Disclosed herein are methods and systems for the use of extraction chromatography resins to concentrate Ac from dilute solutions that may contain Th isotopes and / or other isotopes, such as Ra. As disclosed herein, at least some extraction chromatography resins strongly retain trivalent actinides between 4 and 6 M HNO3 that can be recovered in good yields with small volumes of dilute acids. These small volumes of acid eluents result in significant concentration of the solution of the trivalent / certain tetravalent ions, such that they can be further processed without requiring lengthy evaporation steps that are utilized in standard Ac concentration methods.

The invention discloses a method for extracting a target product from a milk raw material, and relates to the technical field of food processing. According to the method, before strong anion exchange chromatography is carried out, a synergistic pretreatment step of ultrafiltration and conductivity adjustment is introduced, so that acceleration, synergism, quality improvement and cost reduction of the chromatography process are realized, and the technical bottlenecks of low speed, easiness in pollution, instability and the like of the traditional ion exchange chromatography during treatment of milk raw materials are overcome; and a solution is provided for high-efficiency, high-purity and large-scale production of the beta-lactoglobulin and the alpha-lactalbumin. According to the method, strong anion exchange chromatography and weak anion exchange chromatography can be combined, so that the extraction purity of beta-lactoglobulin and alpha-lactalbumin can be further improved; in addition, the method can synchronously realize high-efficiency extraction of various target substances such as casein micelles, lactose and milk mineral salts, so that the additional value and resource utilization efficiency of milk source byproducts are greatly improved.

The invention relates to a high-purity isopropanol purification method based on modified resin, which comprises the following steps: adding activated carbon into an isopropanol mixed solution, decolorizing the isopropanol mixed solution, carrying out primary impurity adsorption, and removing particulate matters and macromolecular impurities meeting activated carbon adsorption conditions in the isopropanol mixed solution. The method comprises the following steps: carrying out primary dehydration through a 4A molecular sieve, adding hydrogen-type strong-acid cation exchange resin and hydrogen-oxygen type strong-base anion exchange resin into an isopropanol mixed solution, and removing positive ions and negative ions in the isopropanol mixed solution; the macroporous alkalescence anion exchange resin of the styrene-divinylbenzene copolymer is added, so that the content of residual acid and alkali is lower than 10ppb. The ionic liquid is fixed on hydrogen type strong-acid cation exchange resin and hydrogen-oxygen type strong-base anion exchange resin, and alcohol, ketone and organic acid impurities are removed. And carrying out fractional rectification on the isopropanol mixed solution, and removing light and heavy components to obtain isopropanol with the purity not lower than 99.999%.

The invention discloses a PGMEA rectification and purification system and method, and the system comprises a precipitation kettle which is used for storing a recovered PGMEA solution until solid impurities in the PGMEA solution precipitate in an upper layer separation suspension liquid; a filter; a condenser; and a dehydrating tower. According to the PGMEA rectification purification system and the rectification purification method, a PGMEA product containing high-content metal ions and a mixture are mixed by a dehydrating tower and then transferred into the dehydrating tower to be dehydrated, the dehydrated product is transferred into rectification equipment through a circulating pump, in the tower, PGMEA migrates upwards, and in the rectification tower, the PGMEA product is separated from the mixture; the heavy components and the metal ions return to the main tower through mass transfer separation and are discharged from the tower kettle for re-rectification, a high-concentration product is extracted from the tower top, and the extracted product enters an ion exchange resin bed to further remove the metal ions, so that a PGMEA product with low metal ion content can be obtained.

The invention discloses a parameter differential separation process, and relates to the technical field of separation. The defects in the prior art are overcome. The method specifically comprises the following steps: carrying out a generalized separation process by using a parameter differential moving bed, and operating the generalized separation process to eliminate a displacement zone in chromatographic sequential operation; the method comprises the following steps: contacting a mobile-phase liquid feeding solution with solid-phase resin / adsorbent filler through a novel mass transfer equilibrium contact method, and starting to obtain a characteristic separation curve; the multiple components contained in the mobile phase liquid feed solution are separated by a new mass transfer equilibrium contact process such that at least one component contained in the mobile phase liquid feed solution can be adsorbed onto the resin / adsorbent. The method realizes final separation of a large-scale production separation system, improves the maximum mass transfer efficiency, can also be used for a binary separation system in the separation process of glucose and fructose, reduces the consumption of washing liquid, and reduces the final power consumption.

The invention relates to the technical field of filler preparation, and discloses an analysis filler for separating glycosylated hemoglobin and a preparation method thereof.The analysis filler for separating glycosylated hemoglobin is obtained by synthesizing nonporous Polymer microspheres of 5 micrometers through a dispersion polymerization method, conducting hydrophilic treatment on the surfaces of the Polymer microspheres to obtain Polymer base balls and finally introducing ion exchange groups to the Polymer base balls. The hydrophilicity of the surface of the matrix is enhanced through hydrophilization treatment, non-specific adsorption is reduced, meanwhile, the swelling property of the filler in water is not affected, and the mechanical strength is not affected. The glycosylated hemoglobin analysis filler which is uniform in granularity, good in separation effect and long in service life can be obtained through the preparation method of the analysis filler.

The present invention provides a kit and a detection method for synchronously detecting catecholamines and their metabolites, which relates to the technical field of analytical detection. The kit contains a diluent, a solid-phase extraction reagent, an LC-MS / MS detection reagent, a solid-phase extraction device, and a solid-phase extraction packing material. Among them, the solid-phase extraction packing material creatively adopts zwitterionic exchange microspheres containing both carboxyl and quaternary ammonium groups. The kit can not only synchronously and efficiently separate and detect 8 kinds of catecholamines and their metabolites in urine samples, but also separate and detect 6 kinds of amino-containing catecholamines and their metabolites in blood samples. When the above kit is used to separate and detect catecholamines and their metabolites, the extraction recovery rate is relatively high, and the linear range covers the reference value range of normal detection, which can significantly shorten the detection time of urine samples, improve the detection efficiency of mass spectrometry, and is conducive to popularization and application in clinical detection.

The present disclosure provides various characteristics for treating tail brine extracted from a bromine plant, when said brine contains residual bromine and chlorine with low pH and high ORP values that will be used in a lithium extraction production facility. The method conditions the extracted tail brine by adding either sodium hydroxide or ammonium hydroxide to bring its pH levels to between 5.5 and 6.5. The conditioned tail brine then gets pre-treated with hydrazine in either less than 70 ppm if used in combination with sodium hydroxide; or 195 ppm if used with ammonium hydroxide until the ORP levels have reached to below 100 mV. The extracted tail brine is then processed through DLE processing device having four groups of adsorption columns filled with lithium adsorption resins that, after treating the extracted tail brine, discharges the raw eluate solution to an effluent tail brine tank using an effluent tail brine pump connected to the DLE processing device.

A full solid-waste micro-expansive concrete and its preparation method are provided, and relate to the field of concrete material technologies. The full solid-waste micro-expansive concrete includes the following components in parts by weight: 920-1060 parts of a coarse aggregate, 460-582 parts of a fine aggregate, 11-19 parts of an expansive agent, 389-512 parts of a modified solid-waste-based cementitious material, and 231-268 parts of water. The coarse aggregate is coal gangue. The fine aggregate is waste ceramic. The modified solid-waste-based cementitious material includes a solid-waste-based clinker, modified polyvinyl alcohol, and a modified anion exchange resin. The solid-waste-based clinker is prepared from the coal gangue, carbide slag, and desulfurization gypsum. The expansive agent is obtained by calcining the carbide slag. The concrete prepared can ensure the initial strength of the concrete, and guarantee continuous micro-expansion in the later stage, compensating for shrinkage and thereby increasing the overall strength of the concrete.

The preparation method comprises the following steps: by taking a seed ball matrix as a base ball, preparing monodisperse porous polymer microspheres through one-step swelling polymerization, then converting residual double bonds on the surfaces of the polymer microspheres into epoxy groups by adopting an oxidation reaction, then grafting a dextran hydrophilic layer to completely cover hydrophobic sites on the surfaces, and then carrying out chemical modification and ligand bonding by utilizing hydroxyl on dextran, so as to obtain the polymer microspheres. The prepared ion exchange polymer filler is porous, high in hydrophilicity and high in exchange capacity and is successfully applied to protein separation and purification. Therefore, the ion exchange purification filler prepared by the method has a good application prospect.

The present invention discloses an acid-sugar separation resin and a preparation method thereof, belonging to separation resin technology. The resin is formed by modifying sodium styrene sulfonate and a chloride ion type strong alkaline anion exchange resin, and then heating and polymerizing with an azo compound water-soluble free radical initiator. The acid-sugar separation resin provided by the present invention is an amphoteric ion exchange resin, and the functional groups contained in the resin structure: quaternary ammonium salt groups, so that the resin obtains excellent acid-sugar separation effect and improves the acid-sugar separation rate; the sulfonate groups contained can avoid the sulfuric acid tailing phenomenon, avoid the sulfuric acid tailing phenomenon to reduce the concentration of recovered sulfuric acid, thereby increasing the cost of subsequent sulfuric acid concentration.

Systems and methods are provided for multiplexed extraction of target minerals from a variety of separate or combined desalination brines and / or wastewater sources. The use of multiple pretreatment, extraction, and posttreatment apparatuses with intelligent, directed flow control can allow for a single system to extract multiple target minerals. Improved extraction methods including zwitterionic simulated moving bed chromatography with target-specific zwitterions can allow for improved extraction efficiency and recovery rates with a dramatically reduced environmental footprint compared to existing methods.

Systems and methods for generating radionuclides, such as radium-224. Systems herein may include a first cartridge having a first opening, a second opening, and a chamber therebetween having a first resin having affinity for thorium-228 and bismuth-212; a second cartridge having a first opening, a second opening, and a chamber therebetween having a second resin having affinity for thorium-228 and bismuth-212, a third cartridge having a first opening, a second opening, and a chamber therebetween comprising a third resin having affinity for thorium-228 and bismuth-212, a fourth cartridge having a first opening, a second opening, and a chamber therebetween having a third resin having affinity for lead-212; wherein a continuous flow path is formed from a top of the first cartridge though the second cartridge, through the third cartridge, and to a bottom of the fourth cartridge during system use.

The invention relates to the technical field of biomacromolecule separation and purification engineering, and discloses a chromatographic separation method for removing endotoxin in a vaccine preparation, which comprises the following steps: preparing an equilibrium buffer solution containing citrate with specific concentration and L-arginine hydrochloride; providing a mixed mode chromatography medium with hydrophobic and ion exchange complex ligands and balancing with a buffer; according to the method, through the synergistic effect of 8.0-12.0 mmol / L of citrate and 150-250 mmol / L of L-arginine hydrochloride, the endotoxin micelle structure is destroyed and is induced to be dissociated into monomers, and meanwhile, L-arginine is used for inhibiting monomer aggregation, so that the monomers are diffused into inner holes of the medium in a small size to be adsorbed, and the endotoxin micelle structure is separated into the medium. Therefore, the problem of separation caused by size overlapping of endotoxin micelles and antigens is solved, and double breakthrough of deep removal of endotoxin and high recovery rate of antigens is realized.

The invention provides a production process of SEMI-G5-grade high-purity NMP (N-Methyl Pyrrolidone), which is characterized in that metal ions, magnetic foreign / non-magnetic foreign particulate matters and the like of conventional industrial-grade NMP are completely removed by adopting a multi-section rectification, resin adsorption and precise filtration process, so that the SEMI-G5-grade NMP reaches the SEMI-G5 grade in an ultra-clean high-purity reagent; and the use requirements on the ultra-clean high-purity NMP in the fields of semiconductors, integrated circuits and novel display are met.

The invention belongs to the technical field of separation resin, and relates to amphoteric ion exchange resin as well as a preparation method and application thereof. The amphoteric ion exchange resin is obtained by introducing a monomer 3-[N, N-dimethyl-[2-(2-methylpropane-2-enoyloxy) ethyl] ammonium] propane-1-sulfonic acid inner salt and a monomer methacryloyloxyethyl trimethyl ammonium chloride into chloromethylated polystyrene resin through an atom transfer radical polymerization reaction. Quaternary ammonium salt groups exposed on 3-[N, N-dimethyl-[2-(2-methylpropyl-2-enoyloxy) ethyl] ammonium] propane-1-sulfonic acid inner salt and methacryloyloxyethyl trimethyl ammonium chloride in the amphoteric ion exchange resin can improve the separation rate of acid and sugar; and meanwhile, during elution, sulfonate groups on 3-[N, N-dimethyl-[2-(2-methylpropane-2-enoyloxy) ethyl] ammonium] propane-1-sulfonic acid inner salt in the resin can effectively weaken the sulfuric acid tailing phenomenon by virtue of the sulfonate groups on the 3-[N, N-dimethyl-[2-(2-methylpropane-2-enoyloxy) ethyl] ammonium] propane-1-sulfonic acid inner salt.

The invention discloses a strongly acidic cation exchange chromatography material and a preparation method thereof. The chromatography material takes microspheres as a matrix material, and takes halogenated alkyl sodium benzenesulfonate and hydroxyl-containing halogenated alkyl sodium sulfonate as functional groups. The preparation method comprises the following steps: epoxy activation: dispersing microspheres in a continuous phase, adding a reducing agent, an alkaline solution and a grafting reagent, and reacting to obtain epoxy activated microspheres; preliminary sulfonation: enabling the epoxy activated microspheres to react with hydroxyl-containing halogenated alkyl sodium sulfonate serving as a first sulfonating agent under an alkaline condition to obtain preliminarily sulfonated microspheres; deep sulfonation: enabling the preliminarily sulfonated microspheres to react with halogenated sodium alkyl benzene sulfonate serving as a second sulfonating agent to obtain a target product. The strongly acidic cation exchange chromatography material provided by the invention can achieve the effects of high protein adsorption capacity and high ion exchange site density.

The invention provides a kit for synchronously detecting catecholamine and metabolites thereof and a detection method, and relates to the technical field of analysis and detection. The kit comprises a diluent, a solid-phase extraction reagent, an LC-MS / MS detection reagent, a solid-phase extraction device and a solid-phase extraction filler. Wherein the solid-phase extraction filler creatively adopts an amphiphilic ion exchange microsphere containing two functional groups, namely carboxyl and quaternary ammonium at the same time. The kit can be used for synchronously and efficiently separating and detecting eight catecholamines and metabolites thereof in a urine sample; and 6 kinds of catecholamines containing amino groups and metabolites thereof in a blood sample can be separated and detected. When the kit is used for separating and detecting catecholamine and metabolites thereof, the extraction and recovery rate is high, the linear range covers the reference value range of normal detection, the detection time of a urine sample can be remarkably shortened, the detection efficiency of mass spectrum is improved, and popularization and application in clinical detection are facilitated.

Provided herein are integrated continuous biomanufacturing processes for producing a therapeutic protein drug substance. Also provided are systems that are capable of continuously producing a therapeutic protein drug substance.

The invention provides a continuous fluid separation system for recovering lithium from mirabilite, and relates to the technical field of continuous fluid separation. A continuous fluid separation system for recovering lithium from mirabilite comprises a plurality of treatment subsystems, each treatment subsystem comprises an exchange area, a material washing area and an acid regeneration analysis area which are arranged in sequence, and each separation unit of the treatment subsystems is filled with a titanium adsorbent filler; the exchange area adopts a three-parallel two-serial feeding mode; gradient washing is carried out in a three-string mode in the material washing area; and the acid regeneration analysis area adopts a three-parallel analysis mode. According to the continuous fluid separation system for recovering lithium from mirabilite, the recovery rate of lithium can exceed 90%, continuous operation is achieved, product components and concentration are kept stable, and the use amount of washing water and an acid regenerant is greatly reduced.