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The medium cycle bioreactor (MCB): Monoclonal antibody production in a new economic production system

机译:中周期生物反应器(MCB):新型经济生产系统中的单克隆抗体生产

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The perfusion mode of a continuous cell culture bioreactor was modified to establish a closed loop system. Eighty percent of the spent medium was re-used twice. The medium cycle bioreactor unit was operated sterile and uncomplicated without a technical retention system for the high molecular weight substances. Therefore, only 20% of the actual medium was necessary to run the recycling process. During seven days culture time in a two liter scale 5 grams of IgG1 type monoclonal antibody was produced. During that period the cell specific productivity was constant. Renewal of proteins was omitted because the protein content in the system persisted at a high level. Therefore, self-conditioning substances of the cells were retained in the system as well as the expensive medium components (proteins with catalytic or stimulating function). Seventy to 80% of medium costs and medium quantity were saved for each medium recycling step. Only cheap metabolites that are consumed by the cells had to be supplemented. Uptake rates of glucose and amino acids were calculated to establish a suitable supplementation mixture for the recirculated medium.
机译:修改了连续细胞培养生物反应器的灌注模式以建立闭环系统。 80%的用过的培养基被重复使用了两次。中周期生物反应器单元无菌操作,操作简单,没有用于高分子量物质的技术保留系统。因此,运行循环过程仅需要实际介质的20%。在两天的培养时间内的七天中,产生了5克IgG1型单克隆抗体。在此期间,电池的单位生产率是恒定的。省略了蛋白质更新,因为系统中的蛋白质含量持续较高水平。因此,细胞的自我调节物质以及昂贵的培养基成分(具有催化或刺激功能的蛋白质)都保留在系统中。每个介质回收步骤节省了70%至80%的介质成本和介质数量。仅需补充细胞消耗的廉价代谢物。计算葡萄糖和氨基酸的摄取速率以建立用于再循环培养基的合适的补充混合物。

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