Protein adsorption on novel acrylamido-based polymeric ion exchangers II. Adsorption rates and column behavior

被引:64
作者
Hunter, AK [1 ]
Carta, G [1 ]
机构
[1] Univ Virginia, Dept Chem Engn, Charlottesville, VA 22903 USA
基金
美国国家科学基金会;
关键词
diffusion; ion exchangers; polymeric gels; adsorption; stationary phases; LC; proteins;
D O I
10.1016/S0021-9673(00)00865-7
中图分类号
Q5 [生物化学];
学科分类号
071010 ; 081704 ;
摘要
Uptake kinetics and breakthrough behavior were determined for bovine serum albumin (BSA) and alpha -chymotrypsinogen (alpha CHY) in new polymeric ion-exchange media based on acrylamido monomers. Two anion exchangers and a cation exchanger were investigated. As shown in Part I of this work, the two anion exchangers have different morphologies. The first one, BRX-Q, comprises a low-density gel with a matrix of denser polymeric aggregates. While this material has a very low size-exclusion limit for neutral probes, it exhibits an extremely high binding capacity for BSA. The second anion exchanger, BRX-QP, comprises large open pores but has a very low binding capacity. The cation exchanger, BRX-S, also comprises large open pores but exhibits an intermediate capacity; likely as a result of the presence of smaller pores. Dynamic protein uptake experiments showed that the highest mass transfer rates are obtained with BRX-Q. The apparent diffusivity is also highest for this material and increases substantially as the protein concentration is reduced. For these particles, the external film resistance is dominant at very low protein concentrations. Much lower rates and apparent diffusivities are obtained for BRX-QP. Finally intermediate rates and apparent diffusivities are found with BRX-S. The concentration dependence of the apparent pore diffusivity is much less pronounced in this case. The apparently paradoxical result that mass transfer rates are highest for the material with the smallest neutral-probe size-exclusion limit can be explained in terms of a general conceptual model where parallel pore and adsorbed-phase diffusion paths exist in these particles. In the first case, adsorbed phase diffusion in gel pores is dominant, while in the second transport is dominated by diffusion in a macroporous network. In the third case, both contributions are important. The conceptual model provides an accurate prediction of the breakthrough behavior of columns packed with these media using independently determined rate parameters. Dynamic binding capacities of 80-140 mg/ml were observed for BSA on BRX-Q in ca. 1.5 cm columns operated at 300-900 cm/h in agreement with theoretical predictions. (C) 2000 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:81 / 97
页数:17
相关论文
共 33 条
[2]   MODELING AND ANALYSIS OF BIOSPECIFIC ADSORPTION IN A FINITE BATH [J].
ARVE, BH ;
LIAPIS, AI .
AICHE JOURNAL, 1987, 33 (02) :179-193
[3]   SEPARATION OF PROTEIN MIXTURES BY CONTINUOUS ANNULAR CHROMATOGRAPHY WITH STEP ELUTION [J].
BLOOMINGBURG, GF ;
CARTA, G .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1994, 55 (1-2) :B19-B27
[4]   Temperature effects on equilibrium and mass transfer of phenylalanine in cation exchangers [J].
Borst, CL ;
Grzegorczyk, DS ;
Strand, SJ ;
Carta, G .
REACTIVE & FUNCTIONAL POLYMERS, 1997, 32 (01) :25-41
[5]   DIFFUSION AND CONVECTION IN CHROMATOGRAPHIC PROCESSES USING PERMEABLE SUPPORTS WITH A BIDISPERSE PORE STRUCTURE [J].
CARTA, G ;
RODRIGUES, AE .
CHEMICAL ENGINEERING SCIENCE, 1993, 48 (23) :3927-3935
[6]   LINEAR DRIVING-FORCE APPROXIMATION FOR INTRAPARTICLE DIFFUSION AND CONVECTION IN PERMEABLE SUPPORTS [J].
CARTA, G .
CHEMICAL ENGINEERING SCIENCE, 1995, 50 (05) :887-889
[7]  
CARTA G, 1992, SEPAR TECHNOL, V2, P62, DOI DOI 10.1016/0956-9618(92)80008-2
[8]   Comparison of protein adsorption isotherms and uptake rates in preparative cation-exchange materials [J].
Chang, C ;
Lenhoff, AM .
JOURNAL OF CHROMATOGRAPHY A, 1998, 827 (02) :281-293
[9]   HINDERED TRANSPORT OF LARGE MOLECULES IN LIQUID-FILLED PORES [J].
DEEN, WM .
AICHE JOURNAL, 1987, 33 (09) :1409-1425
[10]   Characterization of protein adsorption by composite silica-polyacrylamide gel anion exchangers .1. Equilibrium and mass transfer in agitated contactors [J].
Fernandez, MA ;
Carta, G .
JOURNAL OF CHROMATOGRAPHY A, 1996, 746 (02) :169-183