Model-integrated process development demonstrated on the optimization of a robotic cation exchange step

被引:41
作者
Osberghaus, A. [1 ]
Drechsel, K. [1 ]
Hansen, S. [1 ]
Hepbildikler, S. K. [2 ]
Nath, S. [2 ]
Haindl, M. [2 ]
von Lieres, E. [3 ]
Hubbuch, J. [1 ]
机构
[1] Karlsruhe Inst Technol, Sect Biomol Separat Engn 4, Inst Proc Engn Life Sci, D-76131 Karlsruhe, Germany
[2] Roche Diagnost GmbH, Pharmaceut Biotech Prod, D-82377 Penzberg, Germany
[3] Forschungszentrum Julich, Inst Bio & Geosci 1, D-52425 Julich, Germany
关键词
Scale-up; Optimization; Simulation; Mathematical modeling; Chromatography; Downstream processing; MASS-ACTION MODEL; ION-EXCHANGE; CHROMATOGRAPHIC PROCESSES; PROTEIN; ADSORPTION; PREDICTION; DESIGN; PURIFICATION; SIMULATION; DISPLACERS;
D O I
10.1016/j.ces.2012.04.004
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A new concept for chromatography process development based on high-through put data and mechanistic modeling will be presented in this paper. The concept is established in close cooperation between experimentation, modeling and model-based experimental design and allows for robustness analyses and upscale predictions. It will be demonstrated based on a case study: the optimization of a multicomponent separation (lysozyme, ribonuclease A and cytochrome c on SP Sepharose FF (TM)), subject to pH conditions and optimal settings for the shape of the elution gradient. Peak resolution and a precise prediction of retention times were chosen as performance variables in the case study to demonstrate the flexibility of the concept. It was shown that the concept of model-integrated process development is simple to perform from miniaturized scale on. The data, derived from model-based optimally designed experiments, provided sufficient information for process development, the model was calibrated and predictions for optimal separation setups as well as for the upscale showed a high precision. Consequently, the accumulation of data from high-throughput screenings can be used profitably for model-based process optimization and upscale predictions. (c) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:129 / 139
页数:11
相关论文
共 44 条
[1]   Omics tools in accelerated purification process development: Multidimensional fractionation and characterization of crude protein mixtures [J].
Ahamed, Tangir ;
Nfor, Beckley K. ;
van der Wielen, Luuk A. M. ;
Verhaert, Peter D. E. M. ;
van Dedem, Gijs W. K. ;
Eppink, Michel H. M. ;
van de Sandt, Emile J. A. X. ;
Ottens, Marcel .
JOURNAL OF BIOSCIENCE AND BIOENGINEERING, 2009, 108 :S58-S58
[2]   Parameter estimation for the simulation of liquid chromatography [J].
Altenhoner, U ;
Meurer, M ;
Strube, J ;
SchmidtTraub, H .
JOURNAL OF CHROMATOGRAPHY A, 1997, 769 (01) :59-69
[3]  
[Anonymous], 1993, An introduction to the bootstrap
[4]  
[Anonymous], 2004, PAT FRAM INN PHARM
[5]  
[Anonymous], 1980, Multivariate Analysis
[6]  
Bandemer H., 1994, STAT VERSUCHSPLANUNG, V4
[7]   High throughput screening of chromatographic phases for rapid process development [J].
Bensch, M ;
Wierling, PS ;
von Lieres, E ;
Hubbuch, J .
CHEMICAL ENGINEERING & TECHNOLOGY, 2005, 28 (11) :1274-1284
[8]   High-throughput process development:: Determination of dynamic binding capacity using microtiter filter plates filled with chromatography resin [J].
Bergander, Tryggve ;
Nilsson-Vaelimaa, Kristina ;
Oberg, Katarina ;
Lacki, Karol M. .
BIOTECHNOLOGY PROGRESS, 2008, 24 (03) :632-639
[9]   STERIC MASS-ACTION ION-EXCHANGE - DISPLACEMENT PROFILES AND INDUCED SALT GRADIENTS [J].
BROOKS, CA ;
CRAMER, SM .
AICHE JOURNAL, 1992, 38 (12) :1969-1978
[10]   A systematic approach for modeling chromatographic processes - Application to protein purification [J].
Chan, Sharon ;
Titchener-Hooker, Nigel ;
Bracewell, Daniel G. ;
Sorensen, Eva .
AICHE JOURNAL, 2008, 54 (04) :965-977