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A kind of cation exchange chimeric crystal gel separation medium and preparation method thereof

A technology of cation exchange and separation media, which is applied in the field of cation exchange chimeric crystal gel separation media and its preparation, and can solve the problems that the adsorption capacity and separation effect of crystal gel media are not fully exerted, there are no literature reports, and the pore level is single. , to achieve the effects of excellent biocompatibility, convenient operation and simple preparation method

Active Publication Date: 2018-02-27
ZHEJIANG UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Although scholars at home and abroad have successfully prepared different series of crystal colloidal media, the pore size of the existing crystal colloidal media is mainly concentrated in a few microns to about 100-200 microns, with small specific surface area, single pore level, and adsorption sites. Less, so that the adsorption capacity and separation effect of crystal gel media are not fully exerted
However, it is difficult to prepare a multi-level subporous crystal colloidal medium through the coupling method of conventional crystallization porosity and polymerization reaction.
At the same time, there are no reports in the literature on the crystal gel embedded composite crystal gel medium with cation exchange functional groups.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] 0.037M Na in 15.7mL 5 [Cu(HIO 6 ) 2 ] The solution is a catalyst, and the embedded cellulose microspheres polyhydroxyethyl methacrylate mosaic crystal gel matrix with a diameter of 10 mm and a height of 40 mm is used, and the embedded cellulose crystal gel microspheres have a particle size of 300 to 1900 μm. The average particle size is about 900 μm, accounting for 25% of the mass ratio of the crystal gel matrix skeleton; use 15.7 mL of 0.5 M 2-acrylamido-2-methyl-1-propanesulfonic acid aqueous solution at 45 °C to crystallize The gel matrix was grafted for 4 hours to obtain poly(hydroxyethyl methacrylate) matrix and cellulose-based cation-exchange chimeric crystal gel medium. The effective porosity was 84%, the maximum porosity was 95%, and the pore diameter was about 0.1-300 μm. , the adsorption capacity of lysozyme model protein is 1.10 mg / mL.

Embodiment 2

[0022] 0.06M K in 9 mL 5 [Cu(HIO 6 ) 2 The solution is used as a catalyst, and a poly(hydroxyethyl methacrylate) mosaic gel matrix embedded with cellulose microspheres with a diameter of 10 mm and a height of 38 mm is used. The particle size of the embedded cellulose crystal gel microspheres is 300-1900 μm. The average particle size is about 900 μm, accounting for 25% by mass of the crystal gel matrix skeleton; use 9 mL of 2 M 2-acrylamido-2-methyl-1-propanesulfonic acid aqueous solution at 55 °C to crystallize The gel matrix was grafted for 0.5 h to obtain poly(hydroxyethyl methacrylate) matrix and cellulose-based cation exchange chimeric crystal gel medium, with an effective porosity of 83%, a maximum porosity of 94%, and a pore size of about 0.1-300 μm, the saturated adsorption capacity for lysozyme model protein is 5 mg / mL.

Embodiment 3

[0024] 0.04M K in 30 mL 5 [Cu(HIO 6 ) 2 The solution is used as a catalyst, and a poly(hydroxyethyl methacrylate) mosaic gel matrix embedded with cellulose microspheres with a diameter of 10 mm and a height of 52 mm is used. The particle size of the embedded cellulose crystal gel microspheres is 300-1900 μm. The average particle size is about 900 μm, accounting for 30% of the matrix skeleton of crystal gel; use 20 mL of 1 M 2-acrylamido-2-methyl-1-propanesulfonic acid aqueous solution at 51 °C to crystallize The gel matrix was grafted for 2 hours to obtain poly(hydroxyethyl methacrylate) matrix and cellulose-based cation-exchange chimeric crystal gel medium, with an effective porosity of 80%, a maximum porosity of 94%, and a pore size of about 0.1-270 μm, the adsorption capacity of lysozyme model protein is 3.4 mg / mL.

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Abstract

The invention discloses a cation exchange chimeric cryogel separation medium and a preparation method thereof. The cation exchange chimeric cryogel separation medium is characterized in that the chimeric cryogel medium is obtained from grafting and modifying a poly hydroxyethyl methacrylate continuous bed medium with internally chimeric cellulose microspheres through 2-acrylamide-2-methyl-1-propanesulfonic acid, a pore diameter of the chimeric cryogel medium ranges from 0.1 mu m to 300 mu m, the porosity is 80%-95%, the chimeric cryogel medium has a sulfonic group cation exchange functional group, and the adsorption capacity of cryogel for lysozyme model protein is 1-5mg / mL. The pore diameter of the chimeric cryogel medium ranges from sub-micron dimension to micron dimension, the cryogel medium has multi-level pores including diffusion mass transfer small pores and convective mass transfer ultra-large pores, and accordingly, the specific surface area of the cryogel medium and adsorption sites after chemical modification are increased; meanwhile, a matrix material of the cryogel medium has good biocompatibility, is stable in a separation environment, can be repeatedly used, has good safety and has wide application prospect in the biochemical separation field.

Description

technical field [0001] The invention belongs to the technical field of chemical separation media, and in particular relates to a cation-exchange chimeric crystal colloid separation media and a preparation method thereof. Background technique [0002] Crystal gel medium is a new type of chromatographic separation medium that has appeared in recent years. Its medium skeleton has super large pores ranging in size from several microns to hundreds of microns, allowing microbial cells or cell fragments to pass through smoothly. Therefore, it is suitable for fermentation from microorganisms. Rapid separation of biomacromolecular substances in fluids, cell culture fluids, blood, and complex biological fluids containing other solid-phase impurities such as whey, milk, etc. The separation process has few steps, the mass transfer of biological macromolecules in the gel bed column is rapid, the separation time is short, and the separation efficiency is good, so it has important applicat...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J20/285B01J20/30
CPCB01J20/285B01J20/3085B01J2220/445
Inventor 贠军贤姚善泾林东强沈绍传姚克俭潘毛毛
Owner ZHEJIANG UNIV OF TECH
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