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Improving bioreactor cultivation conditions for sensitive cell lines by dynamic membrane aeration

机译:通过动态膜通气改善敏感细胞系的生物反应器培养条件

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摘要

Although the importance of animal cell culture for the industrial (large scale) production of pharmaceutical products is continuously increasing, the sensibility of the cells towards their cultivation environment is still a challenging issue. In comparison to microbial cultures, cell cultures which are not protected by a cell wall are much more sensitive to shear stress and foam formation. Reactor design as well as the selection of ‘robust’ cell lines is particularly important for these circumstances. Nevertheless, even ‘sensitive’ cell lines are selected for certain pharmaceutical processes due to various reasons. These sensitive cell lines have even higher requirements regarding their cultivation environment. Important characteristics for the corresponding reactor design are a high (volumetric) gas mass transfer coefficient, low volumetric power input, low shear stress, low susceptibility to bio-fouling, the ability to cultivate sticky cells and sufficient mixing properties. Membrane aeration has been a long-known possibility to meet some of these requirements, but has not often been applied in recent years. The reasons lie mainly in low gas mass transfer rates, a limited installable volume-specific membrane surface area, restrictions in scalability and problems with membrane fouling. The dynamic membrane aeration bioreactor aeration is a simple concept for bubble-free oxygen supply of such sensitive cultures. It overcomes limitations and draw-backs of previous systems. Consisting of an oscillating, centrally arranged rotor (stirrer) that is wrapped with silicone membrane tubing, it enables doubling the gas mass transfer at the same shear stress in the investigated cultivation scales of 12, 20, 100, and 200 L. Continuous cultivation at these scales allows the same product output as fed-batch cultivation does at tremendously larger reactor volumes. Apart from introducing this novel technology, the presentation comprises selected cultivation results obtained for blood coagulation factor VIII in continuous mode and a therapeutic monoclonal antibody in fed-batch mode in comparison to reference trials.
机译:尽管动物细胞培养对于药物产品的工业化(大规模)生产的重要性不断提高,但是细胞对其培养环境的敏感性仍然是一个具有挑战性的问题。与微生物培养物相比,不受细胞壁保护的细胞培养物对剪切应力和泡沫形成更为敏感。在这些情况下,反应堆设计以及“坚固”细胞系的选择尤为重要。尽管如此,由于各种原因,即使对于某些制药工艺,甚至选择了“敏感”细胞系。这些敏感细胞系对其培养环境有更高的要求。相应反应器设计的重要特征是高(体积)气体传质系数,低体积功率输入,低剪切应力,对生物结垢的敏感性低,培养粘性细胞的能力和足够的混合特性。膜通气一直是满足其中一些要求的长久之久,但近年来却很少被应用。原因主要在于气体传质速率低,可安装的体积比有限的膜表面积,可扩展性受到限制以及膜结垢问题。动态膜曝气生物反应器曝气是为此类敏感培养物提供无气泡氧气的简单概念。它克服了以前系统的局限性和缺点。由振荡的,中心布置的转子(搅拌器)组成,该转子用硅胶膜管包裹,可以在研究的12、20、100和200 L的培养规模下,在相同的剪切应力下使气体质量传递增加一倍。这些规模使反应器体积大得多时,可以得到与补料分批培养相同的产品产量。除介绍这项新技术外,与参考试验相比,本报告还包括针对连续凝血模式凝血因子VIII和分批补给模式治疗性单克隆抗体的选定培养结果。

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