Optimal model-based design of the twin-column CaptureSMB process improves capacity utilization and productivity in protein A affinity capture

被引:69
作者
Baur, Daniel [1 ]
Angarita, Monica [1 ]
Mueller-Spaeth, Thomas [1 ,2 ]
Morbidelli, Massimo [1 ]
机构
[1] Swiss Fed Inst Technol, Dept Chem & Appl Biosci, CH-8093 Zurich, Switzerland
[2] ChromaCon AG, Zurich, Switzerland
关键词
Model based optimization; Monoclonal antibody; Periodic counter-current chromatography; Protein A affinity chromatography; Sequential capture; GRADIENT PURIFICATION MCSGP; ION-EXCHANGE CHROMATOGRAPHY; ANTIBODY-CAPTURE; MASS-TRANSFER; ADSORPTION; OPTIMIZATION; SEPARATIONS; SIMULATION; SORBENTS; MIXTURE;
D O I
10.1002/biot.201500223
中图分类号
Q5 [生物化学];
学科分类号
071010 ; 081704 ;
摘要
Multi-column chromatographic processes have recently been developed for protein A affinity chromatography to efficiently capture monoclonal antibodies from cell culture supernatant. In this work, the novel twin-column CaptureSMB process was compared to a batch capture process with dual loading flow rate to identify performance gains. As a case study, the isolation of a monoclonal antibody with the Amsphere JWT-203 protein A resin was investigated. Using model based optimization, both processes were optimized and compared over a wide range of operating conditions. A trade-off between productivity and capacity utilization was found, and the resulting pareto-curves showed that CaptureSMB dominates batch, except at very low productivity values. With a feed titer of 1.2 mg mL(-1), CaptureSMB could reach a productivity of up to 19.5 mg mL(-1) h(-1) experimentally, while maintaining relatively high capacity utilization of 63.8%. On the other hand, at maximum capacity utilization of 95.5%, a productivity of 10.2 mg mL(-1) h(-1) could be reached. This corresponds to a performance improvement with respect batch operation of about 25% in capacity utilization and 40% in productivity, for given yield and purity. CaptureSMB therefore offers a greatly increased performance over batch capture.
引用
收藏
页码:135 / 145
页数:11
相关论文
共 34 条
[1]   Two-fraction and three-fraction continuous simulated moving bed separation of nucleosides [J].
Abel, S ;
Bäbler, MU ;
Arpagaus, C ;
Mazzotti, M ;
Stadler, J .
JOURNAL OF CHROMATOGRAPHY A, 2004, 1043 (02) :201-210
[2]   Twin-column CaptureSMB: A novel cyclic process for protein A affinity chromatography [J].
Angarita, Monica ;
Mueller-Spaeth, Thomas ;
Baur, Daniel ;
Lievrouw, Roel ;
Lissens, Geert ;
Morbidelli, Massimo .
JOURNAL OF CHROMATOGRAPHY A, 2015, 1389 :85-95
[3]   A continuous multicolumn countercurrent solvent gradient purification (MCSGP) process [J].
Aumann, Lars ;
Morbidelli, Massimo .
BIOTECHNOLOGY AND BIOENGINEERING, 2007, 98 (05) :1043-1055
[4]   STERIC MASS-ACTION ION-EXCHANGE - DISPLACEMENT PROFILES AND INDUCED SALT GRADIENTS [J].
BROOKS, CA ;
CRAMER, SM .
AICHE JOURNAL, 1992, 38 (12) :1969-1978
[5]  
Carta G., 2010, PROTEIN CHROMATOGRAP, P125, DOI 10.1002/9783527630158.ch4
[6]   Analysis of diffusion models for protein adsorption to porous anion-exchange adsorbent [J].
Chen, WD ;
Dong, XY ;
Sun, Y .
JOURNAL OF CHROMATOGRAPHY A, 2002, 962 (1-2) :29-40
[7]   Simulation of porosity decrease with protein adsorption using the distributed pore model [J].
de Neuville, Bertrand Coquebert ;
Thomas, Helen ;
Morbidelli, Massimo .
JOURNAL OF CHROMATOGRAPHY A, 2013, 1314 :77-85
[8]  
Fahrner RL, 1999, BIOTECHNOL APPL BIOC, V30, P121
[9]   Chromatographic behavior of a polyclonal antibody mixture on a strong cation exchanger column. Part I: Adsorption characterization [J].
Forrer, Nicola ;
Butte, Alessandro ;
Morbidelli, Massimo .
JOURNAL OF CHROMATOGRAPHY A, 2008, 1214 (1-2) :59-70
[10]   Optimization of preparative ion-exchange chromatography of proteins: Linear gradient separations [J].
Gallant, SR ;
Vunnum, S ;
Cramer, SM .
JOURNAL OF CHROMATOGRAPHY A, 1996, 725 (02) :295-314