Fractionation of HSA and IgG by gas sparged ultrafiltration

被引:53
作者
Li, QY
Cui, ZF
Pepper, DS
机构
[1] UNIV OXFORD,DEPT ENGN SCI,OXFORD OX1 3PJ,ENGLAND
[2] SCOTTISH NATL BLOOD TRANSFUS SERV,NATL SCI LAB,EDINBURGH EH1 2QN,MIDLOTHIAN,SCOTLAND
基金
英国生物技术与生命科学研究理事会;
关键词
protein fractionation; ultrafiltration; gas sparging; human serum albumin; immunoglobulin G;
D O I
10.1016/S0376-7388(97)00159-2
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The poor selectivity of membranes has been regarded as one of the critical factors limiting the application of membrane systems to protein fractionation. This study demonstrates that ultrafiltration enhanced by gas sparging, together with proper adjustment of solution conditions, can dramatically improve the selectivity of a commercially available tubular PVDF membrane (MWCO 100 kD) for the fractionation of the HSA/IgG mixture, as well as significantly increase permeate flux. For the system studied, the optimal solution condition was found to be at pH 8 and salt concentration of 40 mM. In this system the transmission of IgG was much higher than that of HSA, i.e. a. reversed selectivity was observed. The results were explained on the basis of the balance of the hydrodynamic and electrostatic forces acting on the molecules when they approach and enter the membrane pores. The effect of other operating parameters, including TMP, air and liquid flowrates and protein feed concentration, were also investigated and the optimal conditions were identified. With gas sparged ultrafiltration under those conditions, almost complete separation of the two proteins was achieved. Finally, the possible damage to proteins induced by air bubbles was studied and it was concluded that the damage was negligible under the selected operation conditions.
引用
收藏
页码:181 / 190
页数:10
相关论文
共 33 条
[1]   Protein fractionation in a vortex flow filter .2. Separation of simulated mixtures [J].
Balakrishnan, M ;
Agarwal, GP .
JOURNAL OF MEMBRANE SCIENCE, 1996, 112 (01) :75-84
[2]  
Bellhouse B J, 1994, Bioseparation, V4, P127
[3]   The hydrodynamic and electrostatic interactions on the approach and entry of a charged spherical particle to a charged cylindrical pore in a charged planar surface with implications for membrane separation processes [J].
Bowen, WR ;
Sharif, AO .
PROCEEDINGS OF THE ROYAL SOCIETY A-MATHEMATICAL PHYSICAL AND ENGINEERING SCIENCES, 1996, 452 (1952) :2121-2140
[4]   SEPARATION OF PROTEINS FROM POLYELECTROLYTES BY ULTRAFILTRATION [J].
BOZZANO, AG ;
GLATZ, CE .
JOURNAL OF MEMBRANE SCIENCE, 1991, 55 (1-2) :181-198
[5]   DEAN VORTICES WITH WALL FLUX IN A CURVED CHANNEL MEMBRANE SYSTEM .1. A NEW APPROACH TO MEMBRANE MODULE DESIGN [J].
BREWSTER, ME ;
CHUNG, KY ;
BELFORT, G .
JOURNAL OF MEMBRANE SCIENCE, 1993, 81 (1-2) :127-137
[6]   Flux enhancements with gas sparging in downwards crossflow ultrafiltration: Performance and mechanism [J].
Cui, ZF ;
Wright, KIT .
JOURNAL OF MEMBRANE SCIENCE, 1996, 117 (1-2) :109-116
[7]   GAS-LIQUID 2-PHASE CROSS-FLOW ULTRAFILTRATION OF BSA AND DEXTRAN SOLUTIONS [J].
CUI, ZF ;
WRIGHT, KIT .
JOURNAL OF MEMBRANE SCIENCE, 1994, 90 (1-2) :183-189
[8]  
DING L, 1991, INT J ARTIF ORGANS, V4, P61
[9]  
EHSANI N, 1994, ENG MEMBRANE PROCESS, V2
[10]  
FINNIGAN SM, 1989, CHEM ENG RES DES, V67, P278