Biotechnology and Biochemical Engineering Group, Reading University, Whiteknights, PO Box 226, Reading, U.K.
Cytotechnology. 1999 May;29(3):177-205. doi: 10.1023/A:1008008021481.
The scale of operation of freely suspended animal cell culture has been increasing and in order to meet the demand for recombinant therapeutic products, this increase is likely to continue. The most common reactor types used are stirred tanks. Air lift fermenters are also used, albeit less commonly. No specific guidelines have been published for large scale (>/=10 000 L) animal cell culture and reactor designs are often based on those used for microbial systems. However, due to the large difference in energy inputs used for microbial and animal cell systems such designs may be far from optimal. In this review the importance of achieving a balance between mixing, mass transfer and shear effects is emphasised. The implications that meeting this balance has on design of vessels and operation, particularly in terms of strategies to ensure adequate mixing to achieve homogeneity in pH and dissolved gas concentrations are discussed.
自由悬浮动物细胞培养的规模一直在扩大,为了满足重组治疗产品的需求,这种增长可能会持续下去。最常用的反应器类型是搅拌罐。也使用气升式发酵罐,但使用较少。对于大规模(>=10000L)动物细胞培养尚未发布特定指南,反应器设计通常基于用于微生物系统的设计。然而,由于微生物和动物细胞系统所用能量输入的巨大差异,这种设计可能远非最佳。在这篇综述中,强调了在混合、质量传递和剪切效应之间取得平衡的重要性。讨论了满足这种平衡对容器设计和操作的影响,特别是在确保充分混合以实现 pH 和溶解气体浓度均匀性的策略方面。