锥形烧瓶
生化工程
工艺工程
生物反应器
过程(计算)
混合(物理)
生物量(生态学)
放大
生产(经济)
悬挂(拓扑)
比例(比率)
悬浮培养
计算机科学
环境科学
工程类
数学
细胞培养
化学
生物
生态学
色谱法
植物
物理
宏观经济学
量子力学
经典力学
同伦
纯数学
经济
操作系统
遗传学
作者
Rüdiger W. Maschke,Stefan Seidel,Thomas Bley,Regine Eibl,Dieter Eibl
标识
DOI:10.1016/j.bej.2021.108224
摘要
Processes involving mammalian cell cultures - especially CHO suspension cells - dominate biopharmaceutical manufacturing. These processes are usually developed in small scale orbitally shaken cultivation systems, and thoroughly characterizing these cultivation systems is crucial to their application in research and the subsequent scale-up to production processes. With the knowledge of process engineering parameters such as oxygen transfer rate, mixing time, and power input, in combination with the demands set by the biological production system, biomass growth and product yields can be anticipated and even increased. However, the available data sources for orbitally shaken cultivation systems are often incomplete and thus not sufficient enough to generate suitable cultivation requirements. Furthermore, process engineering knowledge is inapplicable if it is not linked to the physiological demands of the cells. In the current study, a simple yet comprehensive approach for the characterization and design space prediction of orbitally shaken single-use cultivation systems is presented, including the "classical" Erlenmeyer shake flask, the cylindrical TubeSpin bioreactor and the alternately designed Optimum Growth flask. Cultivations were performed inside and outside the design space to validate the defined culture conditions, so that cultivation success (desired specific growth rates and viable cell densities) could be achieved for each cultivation system.
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