Development of a fed-batch culture process for enhanced production of recombinant human antithrombin by Chinese hamster ovary cells

中国仓鼠卵巢细胞 谷氨酰胺 生物化学 细胞培养 生物 氨基酸 抗凝血酶 补料分批培养 重组DNA 谷氨酰胺合成酶 蛋白酶 分子生物学 肝素 发酵 受体 基因 遗传学
作者
Shinobu Kuwae,Toyoo Ohda,Hiroshi Tamashima,Hajime Miki,Kaoru Kobayashi
出处
期刊:Journal of Bioscience and Bioengineering [Elsevier]
卷期号:100 (5): 502-510 被引量:48
标识
DOI:10.1263/jbb.100.502
摘要

Antithrombin is a serine protease inhibitor that inactivates several coagulation proteases, primarily thrombin and factor Xa. The Chinese hamster ovary (CHO) cell line transfected with a vector expressing recombinant human antithrombin (rAT) and a selectable marker, glutamine synthetase (GS), was cultivated in a 2-l fed-batch culture process using serum-free, glutamine-free medium. To maximize the rAT yield, effects of culture pH, balanced amino acid feeding, and an increased glutamate concentration on cell metabolism and rAT production were investigated. When cells were grown at pH values of 6.6, 6.8, 7.0, and 7.2, the maximum cell density and maximum lactate concentration decreased with decreasing pH. The highest production level of rAT was obtained at culture pH 6.8 due to the extended culture lifetime. Compared to the imbalanced amino acid feeding at culture pH 6.8, the balanced amino acid feeding increased the amount of rAT activity by 30% as a result of an increased viable cell number. A decrease in the specific glucose consumption rate (qGlc) with increasing culture time was observed in all the above-mentioned experiments, while the glucose concentration was maintained above 0.7 g l−1. In addition, a decrease in the specific rAT production rate (qrAT) was observed after the depletion of lactate in the late cultivation stage. Taken together, these results suggest that the reduced availability of cellular energy caused by the decrease in qGlc and depletion of lactate led to the decrease in qrAT. This decrease in qrAT was partially prevented by increasing the residual glutamate concentration from 1 mM to 7 mM, thus resulting in an additional 30% increase in the amount of rAT activity. The optimized fed-batch culture process yielded 1.0 g l−1 rAT at 287 h of cultivation.
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