Assessment of fed-batch cultivation strategies for an inducible CHO cell line

被引:9
|
作者
Mellahi, Kahina [1 ]
Brochu, Denis [2 ]
Gilbert, Michel [2 ]
Perrier, Michel [1 ]
Ansorge, Sven [3 ]
Durocher, Yves [3 ]
Henry, Olivier [1 ]
机构
[1] Ecole Polytech Montreal, Dept Chem Engn, POB 6079,Succ Ctr Ville, Montreal, PQ H3C 3A7, Canada
[2] Natl Res Council Canada, Human Hlth Therapeut Portfolio, Ottawa, ON, Canada
[3] Natl Res Council Canada, Human Hlth Therapeut Portfolio, Montreal, PQ, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Fed-batch culture; Biphasic process; Inducible CHO cells; Antibody production; Glycan distribution; HAMSTER OVARY CELLS; RECOMBINANT PROTEIN-PRODUCTION; ANTIBODY EFFECTOR FUNCTIONS; LOW GLUCOSE-CONCENTRATION; MONOCLONAL-ANTIBODY; CULTURE PROCESS; HYBRIDOMA CELLS; ERYTHROPOIETIN PRODUCTION; MULTIVARIATE-ANALYSIS; LACTATE CONSUMPTION;
D O I
10.1016/j.jbiotec.2019.04.005
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
In order to maximize cell growth and productivity for an inducible CHO cell line expressing rituximab, various fed-batch culture strategies were investigated. In each case, the performance was evaluated for cultures induced at moderate and high cell density conditions (4 x 10(6) and 10 x 10(6) cells/mL) to assess the impact of the timing of induction. We first demonstrate the importance of starting the feeding process during the growth phase, as this translated into significantly improved integral of viable cells and antibody concentration, when compared to post-induction feeding only. Secondly, we investigated the impact of the feed rate by maintaining different levels of glucose (25, 35 and 50 mM) via a dynamic feeding strategy. The highest antibody concentrations were achieved under a moderate feeding regime for both cell densities at induction, highlighting the risks of under-or over-feeding the cultures. We then evaluated the impact of performing a temperature shift at induction by testing different mild hypothermia conditions. At small-scale, the highest production yields (1.2 g/L) were achieved when the temperature was reduced from 37 to 30 degrees C during the production phase of a culture induced at high cell density. When the strategy was applied in bioreactor, the better controlled conditions led to even greater product concentrations (1.8 g/L). Furthermore, this production protocol was shown to promote a more galactosylated glycan profile than a bioreactor culture initiated at 34 degrees C during growth and downshifted to 30 degrees C during the production phase.
引用
收藏
页码:45 / 56
页数:12
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