Separation of immunoglobulin G precipitate from contaminating proteins using microfiltration

被引:10
作者
Neal, G
Francis, R
Shamlou, PA
Keshavarz-Moore, E
机构
[1] UCL, Dept Biochem Engn, Adv Ctr Biochem Engn, London WC1E 7JE, England
[2] Prother UK Ltd, Ceredigion SA44 5JT, Wales
关键词
microfiltration; process options; scale down; stirred cell;
D O I
10.1042/BA20030129
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
A small-scale stirred-cell device was used to separate an antivenom antibody precipitate from a suspension containing contaminating soluble proteins. The device has a total volume of 200 ml and is equipped with a filter membrane with a cut-off size of 3 mum. About 90% of the anti body-precipitate particles in the feed were 29 mum or smaller, and the concentration of solids was 12 % (w/w). The microfiltration cell was operated in a constant-volume (continuous/diafiltration) mode, and its performance was compared with an industrial disc-stack centrifuge currently used in the manufacture of antibody precipitate. In terms of product purity, the separation performance of the microfiltration operation was found to be comparable with the disc-stack centrifuge, whereas the overall yield was 10% better than that obtained from the centrifuge. This was attributed to the ability of microfiltration to reduce material losses by integrating a number of operations in a single piece of equipment. These included separation, concentration and buffer exchange, as well as dissolution and final recovery of the antibody in an appropriate buffer. The results obtained from the stirred cell are potentially scaleable, and dynamic microfiltration is shown to be an attractive process option.
引用
收藏
页码:241 / 248
页数:8
相关论文
共 32 条
[1]   FACTORS AFFECTING FLUX IN CROSS-FLOW FILTRATION [J].
BAKER, RJ ;
FANE, AG ;
FELL, CJD ;
YOO, BH .
DESALINATION, 1985, 53 (1-3) :81-93
[2]   THE BEHAVIOR OF SUSPENSIONS AND MACROMOLECULAR SOLUTIONS IN CROSS-FLOW MICROFILTRATION [J].
BELFORT, G ;
DAVIS, RH ;
ZYDNEY, AL .
JOURNAL OF MEMBRANE SCIENCE, 1994, 96 (1-2) :1-58
[3]  
BLATT WF, 1970, MEMBRANE SCI TECHNOL, P73
[4]   Ultra scaledown to predict filtering centrifugation of secreted antibody fragments from fungal broth [J].
Boulding, N ;
Yim, SSS ;
Keshavarz-Moore, E ;
Shamlou, PA ;
Berry, M .
BIOTECHNOLOGY AND BIOENGINEERING, 2002, 79 (04) :381-388
[5]   Characterization of flow intensity in continuous centrifuges for the development of laboratory mimics [J].
Boychyn, M ;
Yim, SSS ;
Shamlou, PA ;
Bulmer, M ;
More, J ;
Hoare, A .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (16) :4759-4770
[6]  
BRADFORD MM, 1976, ANAL BIOCHEM, V72, P248, DOI 10.1016/0003-2697(76)90527-3
[7]   Particle deposition during membrane filtration of colloids: Transition between concentration polarization and cake formation [J].
Chen, V ;
Fane, AG ;
Madaeni, S ;
Wenten, IG .
JOURNAL OF MEMBRANE SCIENCE, 1997, 125 (01) :109-122
[8]  
CORCORAN RM, 1977, CLIN CHEM, V23, P765
[9]  
Davies JL, 2000, BIOTECHNOL BIOENG, V69, P429
[10]   CRITICAL FLUX CONCEPT FOR MICROFILTRATION FOULING [J].
FIELD, RW ;
WU, D ;
HOWELL, JA ;
GUPTA, BB .
JOURNAL OF MEMBRANE SCIENCE, 1995, 100 (03) :259-272