Pilot scale recovery of monoclonal antibodies by expanded bed ion exchange adsorption

被引:32
作者
Ameskamp, N [1 ]
Priesner, C [1 ]
Lehmann, J [1 ]
Lütkemeyer, D [1 ]
机构
[1] Univ Bielefeld, Fac Technol, Inst Cell Culture Technol, D-33501 Bielefeld, Germany
关键词
cation exchange chromatography; dynamic binding capacity; expanded bed adsorption; feed viscosity; monoclonal antibody; pilot scale;
D O I
10.1023/A:1008063626294
中图分类号
Q5 [生物化学];
学科分类号
071010 ; 081704 ;
摘要
The aim of the investigations was to estimate the scale up properties of an efficient chromatographic first capture step for the recovery of murine IgG(1) from undiluted and unclarified hybridoma cell culture broth using an ion exchange matrix in expanded bed mode. The tested new sulfopropyl-based ion exchange matrix (Streamline(TM) SP XL, Amersham Pharmacia Biotech) stands out due to its enhanced capacity compared to its precursor (Streamline(TM) SP). Defining the working pH in preliminary electrophoretic analyses (titration curve, SDS-PAGE) and small-scaled chromatographic binding studies showed, that the optimal value for the IgG purification was pH 4.6, where a co-chromatography of the medium supplement albumin (500 mg l(-1), pI = 4.8) could not be avoided. Further scouting experiments dealt with the dynamic capacity of the matrix, which was evaluated by frontal adsorption analysis. In packed bed mode no break-through of the target protein was achieved even after 6.5 mg IgG per ml matrix were applied. These results could not be reproduced in expanded bed mode with cell-free supernatant, where the dynamic capacity was found to be only 1.5 mg IgG/ml SP XL. Processing cell-containing broth resulted in an additional decrease of the value down to 0.5 mg ml(-1), presumably caused by the remarkable biomass adsorption to the matrix. The search for the reasons led to the examination of the hydrodynamic conditions. Buffer experiments with a tracer substance (acetone) pointed out, that the flow in expanded bed was significantly more influenced by back-mixing effects and channel formations than in packed bed. These effects could be compensated with an enhanced viscosity of the liquid phase, which was achieved by the addition of glucose. As a result of the improved hydrodynamic conditions in the expanded bed, the dynamic capacity could be increased from 0.5 to more than 4.5 mg IgG/ml matrix for the processing of cell culture broth with 400 mM glucose. Finally, the scale up from a Streamline(TM) 25 to a Streamline(TM) 200 column was performed under conditions, which proved to be optimal: 100 L of unclarified hybridoma broth were concentrated with a binding rate of 95% in less than 3.5 hours. Loading the column no break-through of the target protein was achieved. However, the eluate still contained debris and cells, which points out the major disadvantage of the method: the biomass attachment to the matrix.
引用
收藏
页码:169 / 188
页数:20
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