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CHO 细胞中单克隆抗体生产的高通量预测性缩小模型。

A predictive high-throughput scale-down model of monoclonal antibody production in CHO cells.

机构信息

Seahorse Bioscience Inc., Billerica, Massachusetts 01862, USA.

出版信息

Biotechnol Bioeng. 2009 Dec 15;104(6):1107-20. doi: 10.1002/bit.22474.

Abstract

Multi-factorial experimentation is essential in understanding the link between mammalian cell culture conditions and the glycoprotein product of any biomanufacturing process. This understanding is increasingly demanded as bioprocess development is influenced by the Quality by Design paradigm. We have developed a system that allows hundreds of micro-bioreactors to be run in parallel under controlled conditions, enabling factorial experiments of much larger scope than is possible with traditional systems. A high-throughput analytics workflow was also developed using commercially available instruments to obtain product quality information for each cell culture condition. The micro-bioreactor system was tested by executing a factorial experiment varying four process parameters: pH, dissolved oxygen, feed supplement rate, and reduced glutathione level. A total of 180 micro-bioreactors were run for 2 weeks during this DOE experiment to assess this scaled down micro-bioreactor system as a high-throughput tool for process development. Online measurements of pH, dissolved oxygen, and optical density were complemented by offline measurements of glucose, viability, titer, and product quality. Model accuracy was assessed by regressing the micro-bioreactor results with those obtained in conventional 3 L bioreactors. Excellent agreement was observed between the micro-bioreactor and the bench-top bioreactor. The micro-bioreactor results were further analyzed to link parameter manipulations to process outcomes via leverage plots, and to examine the interactions between process parameters. The results show that feed supplement rate has a significant effect (P < 0.05) on all performance metrics with higher feed rates resulting in greater cell mass and product titer. Culture pH impacted terminal integrated viable cell concentration, titer and intact immunoglobulin G titer, with better results obtained at the lower pH set point. The results demonstrate that a micro-scale system can be an excellent model of larger scale systems, while providing data sets broader and deeper than are available by traditional methods.

摘要

多因素实验对于理解哺乳动物细胞培养条件与任何生物制造过程的糖蛋白产物之间的关系至关重要。随着生物工艺开发受到质量源于设计理念的影响,这种理解的需求日益增加。我们开发了一种系统,该系统允许在受控条件下并行运行数百个微生物反应器,从而能够进行比传统系统范围更大的因子实验。还开发了一种高通量分析工作流程,使用市售仪器获取每个细胞培养条件的产品质量信息。通过执行一个因子实验来测试微生物反应器系统,该实验改变了四个过程参数:pH 值、溶解氧、进料补充率和还原型谷胱甘肽水平。在这个 DOE 实验中,总共运行了 180 个微生物反应器两周,以评估这种缩小规模的微生物反应器系统作为高通量工艺开发工具的性能。在线测量 pH 值、溶解氧和光密度,并通过离线测量葡萄糖、活力、滴度和产品质量进行补充。通过将微生物反应器的结果与在传统 3 L 生物反应器中获得的结果进行回归来评估模型的准确性。在微生物反应器和台式生物反应器之间观察到了极好的一致性。进一步分析微生物反应器的结果,通过杠杆图将参数操作与工艺结果联系起来,并检查工艺参数之间的相互作用。结果表明,进料补充率对所有性能指标都有显著影响(P < 0.05),较高的进料速率导致细胞质量和产物滴度增加。培养 pH 值影响终末整合活细胞浓度、滴度和完整免疫球蛋白 G 滴度,较低的 pH 值设定点获得更好的结果。结果表明,微尺度系统可以成为更大规模系统的优秀模型,同时提供比传统方法更广泛和更深入的数据。

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