Preparation of mixed matrix adsorber membranes for protein recovery

被引:86
作者
Avramescu, ME [1 ]
Gironès, M [1 ]
Borneman, Z [1 ]
Wessling, M [1 ]
机构
[1] Univ Twente, Fac Sci & Technol, Membrane Technol Grp, NL-7500 AE Enschede, Netherlands
关键词
EVAL; mixed matrix adsorber membranes; bovine serum albumin (BSA); ion exchange particles; protein recovery;
D O I
10.1016/S0376-7388(03)00178-9
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper presents a generic technology allowing the incorporation of functional entities into a porous substrate. Various ion exchange particles were incorporated into an ethylene vinyl alcohol (EVAL) copolymer porous matrix by an immersion phase separation process and a heterogeneous matrix, composed of solid particles surrounded by a polymeric film, was formed. The developed concept is flexible and offers the possibility to easily adjust the geometry, the adsorption capacity, as well as the functionality of the structure. A series of fibers as well as flat membranes bearing an adsorptive function and high protein binding capacities were prepared. The membranes were characterized with respect to their morphology, porosity, permeability and adsorption capacity. High values of the protein adsorption capacity (40-45 mg bovine serum albumin (BSA)/ml membrane) were obtained by static adsorption experiments. In a sequential desorption step by changing the pH and/or the ionic strength of the eluent, up to 90% protein recovery can be obtained. Dynamic capacity experiments were performed by flowing the protein solution through a stack of 10 membranes. The protein mass adsorbed per unit of membrane bed was calculated at a breakthrough concentration 10% of the feed concentration. The adsorber membranes can be reused in multiple adsorption/desorption cycles without significant loss of performance. (C) 2003 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:219 / 233
页数:15
相关论文
共 32 条
[1]   Equilibrium and simulation of the operation for the adsorption of albumin proteins in an iminodiacetic-Cu bounded ion exchange resin (IMAC) [J].
Arévalo, E ;
Rendueles, M ;
Fernández, A ;
Díaz, M .
SEPARATION AND PURIFICATION TECHNOLOGY, 2000, 18 (03) :217-225
[2]  
AVGRAMESCU ME, 2003, IN PRESS J CHROMAT A
[3]   Preparation of ethylene vinylalcohol copolymer membranes suitable for ligand coupling in affinity separation [J].
Avramescu, ME ;
Sager, WFC ;
Mulder, MHV ;
Wessling, M .
JOURNAL OF MEMBRANE SCIENCE, 2002, 210 (01) :155-173
[4]  
BOGGS DR, 2000, Patent No. 0002638
[5]   THE KINETICS OF PROTEIN ADSORPTION ON SYNTHETICS AND MODIFIED NATURAL SURFACES [J].
BORNZIN, GA ;
MILLER, IF .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 1982, 86 (02) :539-558
[6]  
BRADFORD MM, 1976, ANAL BIOCHEM, V72, P248, DOI 10.1016/0003-2697(76)90527-3
[7]  
Crank J., 1979, MATH DIFFUSION
[8]  
DAMME HSV, 1990, THESIS U TWENTE
[9]   Characterization of protein adsorption by composite silica-polyacrylamide gel anion exchangers .2. Mass transfer in packed columns and predictability of breakthrough behavior [J].
Fernandez, MA ;
Laughinghouse, WS ;
Carta, G .
JOURNAL OF CHROMATOGRAPHY A, 1996, 746 (02) :185-198
[10]   Cellulose as a (bio)affinity carrier:: properties, design and applications [J].
Gemeiner, P ;
Polakovic, M ;
Mislovicová, D ;
Stefuca, V .
JOURNAL OF CHROMATOGRAPHY B-ANALYTICAL TECHNOLOGIES IN THE BIOMEDICAL AND LIFE SCIENCES, 1998, 715 (01) :245-271