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Bioprocess development for the production of mouse-human chimeric anti-epidermal growth factor receptor vIII antibody C12 by suspension culture of recombinant Chinese hamster ovary cells

机译:通过悬浮培养中国仓鼠卵巢细胞生产小鼠-人嵌合抗表皮生长因子受体vIII抗体C12的生物工艺开发

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摘要

The mouse-human chimeric anti-epidermal growth factor receptor vIII (EGFRvIII) antibody C12 is a promising candidate for the diagnosis of hepatocellular carcinoma (HCC). In this study, 3 processes were successfully developed to produce C12 by cultivation of recombinant Chinese hamster ovary (CHO-DG44) cells in serum-free medium. The effect of inoculum density was evaluated in batch cultures of shaker flasks to obtain the optimal inoculum density of 5 × 105 cells/mL. Then, the basic metabolic characteristics of CHO-C12 cells were studied in stirred bioreactor batch cultures. The results showed that the limiting concentrations of glucose and glutamine were 6 and 1 mM, respectively. The culture process consumed significant amounts of aspartate, glutamate, asparagine, serine, isoleucine, leucine, and lysine. Aspartate, glutamate, asparagine, and serine were particularly exhausted in the early growth stage, thus limiting cell growth and antibody synthesis. Based on these findings, fed-batch and perfusion processes in the bioreactor were successfully developed with a balanced amino acid feed strategy. Fed-batch and especially perfusion culture effectively maintained high cell viability to prolong the culture process. Furthermore, perfusion cultures maximized the efficiency of nutrient utilization; the mean yield coefficient of antibody to consumed glucose was 44.72 mg/g and the mean yield coefficient of glutamine to antibody was 721.40 mg/g. Finally, in small-scale bioreactor culture, the highest total amount of C12 antibody (1,854 mg) was realized in perfusion cultures. Therefore, perfusion culture appears to be the optimal process for small-scale production of C12 antibody by rCHO-C12 cells.
机译:小鼠-人类嵌合抗表皮生长因子受体vIII(EGFRvIII)抗体C12是诊断肝细胞癌(HCC)的有前途的候选药物。在这项研究中,成功​​开发了通过在无血清培养基中培养重组中国仓鼠卵巢(CHO-DG44)细胞来生产C12的3种方法。在摇瓶的分批培养中评估接种密度的影响,以获得5×10 5 细胞/ mL的最佳接种密度。然后,在搅拌生物反应器分批培养中研究了CHO-C12细胞的基本代谢特征。结果表明,葡萄糖和谷氨酰胺的极限浓度分别为6和1 mM。培养过程中消耗了大量的天冬氨酸,谷氨酸,天冬酰胺,丝氨酸,异亮氨酸,亮氨酸和赖氨酸。天冬氨酸,谷氨酸,天冬酰胺和丝氨酸在早期生长阶段特别枯竭,因此限制了细胞生长和抗体合成。基于这些发现,采用平衡氨基酸进料策略成功开发了生物反应器中的补料分批和灌注过程。分批补料尤其是灌注培养有效地维持了高细胞活力,从而延长了培养过程。此外,灌注培养可以最大程度地利用养分。抗体对消耗葡萄糖的平均产量系数为44.72 mg / g,谷氨酰胺对抗体的平均产量系数为721.40 mg / g。最后,在小型生物反应器培养中,在灌注培养中实现了最高的C12抗体总量(1,854 mg)。因此,灌注培养似乎是rCHO-C12细胞小规模生产C12抗体的最佳方法。

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