Protein separation using plate-and-frame modules with ion-exchange membranes

被引:26
作者
Lin, SY [1 ]
Suen, SY [1 ]
机构
[1] Natl Chung Hsing Univ, Dept Chem Engn, Taichung 402, Taiwan
关键词
plate-and-frame module; ion-exchange membrane; mixed-mode; breakthrough curve; adsorption;
D O I
10.1016/S0376-7388(02)00015-7
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The separation performance using plate-and-frame modules with ion-exchange membranes was investigated in this study. The proteins employed were lysozyme, BSA and gamma-globulin. In the batch adsorption, the adsorption behaviors of lysozyme onto cation-exchange membranes and BSA onto anion-exchange membranes, both showing the heterogeneous adsorption, could be described more appropriately with the Suen model than the Langmuir model. In the flow process using a single plate-and-frame module. operating conditions greatly influenced the separation performance. At the elution stage, a better performance was achieved by using the cross-flow mode. Other operating conditions such as the number of membranes in a stack. the pH value at adsorption, and the mixed mode in the membrane stack also affected the separation performance. As to the two-module experiments, two different operation designs were tested: connection in tandem and connection in parallel. The tandem design resulted in a better protein recovery than the parallel design when only one kind of ion-exchange membrane was adopted. Regarding the mixed-mode effect in the tandem design, when the ion-exchange membranes suitable for the target protein were placed in the second module, the target protein could gain a longer time for adsorption and, hence. a better recovery was accomplished. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:37 / 51
页数:15
相关论文
共 11 条
[1]   EFFECTS OF LIGAND CONCENTRATION ON PROTEIN ADSORPTION IN DYE LIGAND ADSORBENTS [J].
BOYER, PM ;
HSU, JT .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (01) :241-251
[2]   MEMBRANE-BASED AFFINITY TECHNOLOGY FOR COMMERCIAL SCALE PURIFICATIONS [J].
BRANDT, S ;
GOFFE, RA ;
KESSLER, SB ;
OCONNOR, JL ;
ZALE, SE .
BIO-TECHNOLOGY, 1988, 6 (07) :779-782
[3]  
Charcosset C, 1998, J CHEM TECHNOL BIOT, V71, P95, DOI 10.1002/(SICI)1097-4660(199802)71:2<95::AID-JCTB823>3.0.CO
[4]  
2-J
[5]   Controlled mixed-mode interaction chromatography on membrane adsorbers [J].
Freitag, R ;
Splitt, H ;
Reif, OW .
JOURNAL OF CHROMATOGRAPHY A, 1996, 728 (1-2) :129-137
[6]  
Horvath C., 1986, J CHROMATOGR, V359, P255
[7]   SEPARATION OF BIOMOLECULES USING ADSORPTIVE MEMBRANES [J].
ROPER, DK ;
LIGHTFOOT, EN .
JOURNAL OF CHROMATOGRAPHY A, 1995, 702 (1-2) :3-26
[8]   SORPTION KINETICS AND BREAKTHROUGH CURVES FOR PEPSIN AND CHYMOSIN USING PEPSTATIN-A AFFINITY MEMBRANES [J].
SUEN, SY ;
ETZEL, MR .
JOURNAL OF CHROMATOGRAPHY A, 1994, 686 (02) :179-192
[9]  
Suen SY, 1998, J CHIN INST CHEM ENG, V29, P307
[10]   MIXED-MODE RETENTION OF PEPTIDES ON PHOSPHATE-MODIFIED POLYBUTADIENE-COATED ZIRCONIA [J].
SUN, LF ;
CARR, PW .
ANALYTICAL CHEMISTRY, 1995, 67 (15) :2517-2523