Regulation on both pore structure and pressure-resistant property of uniform agarose microspheres for high-resolution chromatography.

Agarose microspheres High-resolution chromatography Pore structure Pressure-resistant property Uniform

Journal

Journal of chromatography. A
ISSN: 1873-3778
Titre abrégé: J Chromatogr A
Pays: Netherlands
ID NLM: 9318488

Informations de publication

Date de publication:
11 Oct 2022
Historique:
received: 30 06 2022
revised: 21 08 2022
accepted: 29 08 2022
pubmed: 16 9 2022
medline: 24 9 2022
entrez: 15 9 2022
Statut: ppublish

Résumé

How to improve the performance of chromatographic media is very important in chromatography. Uniform agarose microspheres were successfully prepared using membrane emulsification method with a controllable particle size, followed by multi-step crosslinking and dextran-grafting, respectively. To obtain both fine pore structure and good pressure-resistant property, the effects of both dextran-grafting and crosslinking process were studied carefully and also, the preparation conditions were delicately adjusted. Inverse size-exclusion chromatography was used for determining the pore structure of these agarose microspheres. Uniform agarose microspheres with an average particle size of about 8 μm were obtained with regularly spherical, transparent and smooth appearance. By introducing a certain molecular weight of dextran or pentaerythritol glycidyl ether at different crosslinking steps, both the pressure-resistant and the chromatographic properties of microspheres were improved. Both the maximum flow velocity and the corresponding pressure drop increased with the decrease of the molecular weight of dextran, i.e., 99 cm/h and 3.22 MPa, respectively, using dextran T3 (3 kDa). The average pore size of agarose microspheres decreased from 6.04±0.56 nm to 2.50±0.12 nm with the increase of the molecular weight of dextran from dextran T3 (3 kDa) to dextran T100 (100 kDa), with a high resolution obtained for a certain molecular range of model proteins. Also, the pressure-resistant property was highly improved in multi-step crosslinking process, with a maximum flow velocity of 107 cm/h and a corresponding pressure drop of 3.62 MPa obtained after the whole crosslinking steps. The average pore size of agarose microspheres was 3.72±0.32, 3.90±0.21 and 3.60±0.27 nm for the introduction of pentaerythritol glycidyl ether as the crosslinking agent at different steps, respectively. These uniform dextran-grafted agarose microspheres have a finely controllable molecular range with a high resolution compared with traditional ones, which are beneficial for chromatographic selectivity. Therefore, they are very useful for high-resolution chromatography and have wide applications in downstream process.

Identifiants

pubmed: 36108352
pii: S0021-9673(22)00653-7
doi: 10.1016/j.chroma.2022.463461
pii:
doi:

Substances chimiques

Dextrans 0
Epoxy Compounds 0
Propylene Glycols 0
glycidyl ethers 0
Sepharose 9012-36-6
pentaerythritol SU420W1S6N

Types de publication

Journal Article

Langues

eng

Sous-ensembles de citation

IM

Pagination

463461

Informations de copyright

Copyright © 2022. Published by Elsevier B.V.

Déclaration de conflit d'intérêts

Declaration of Competing Interest The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

Auteurs

Lan Zhao (L)

State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China.

Xiangjing Che (X)

State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China; College of Environment and Chemical Engineering, Yanshan University, Hebei 066000, China.

Yongdong Huang (Y)

State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China. Electronic address: ydhuang@ipe.ac.cn.

Kai Zhu (K)

State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China.

Yuxiang Du (Y)

State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China; School of Chemical & Environmental Engineering, China University of Mining & Technology, Beijing 100083, China.

Jingwei Gao (J)

State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China; School of Chemical & Environmental Engineering, China University of Mining & Technology, Beijing 100083, China.

Rongyue Zhang (R)

Department of Applied Chemistry, Beijing Institute of Petrochemical Technology, Beijing 102617, China.

Yongqiang Zhang (Y)

College of Environment and Chemical Engineering, Yanshan University, Hebei 066000, China.

Guanghui Ma (G)

State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China; University of Chinese Academy of Sciences, Beijing 100049, China. Electronic address: ghma@ipe.ac.cn.

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