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采用酶控葡萄糖补料系统实现从小试规模到中试规模的葡萄糖限制型高密度培养。

Glucose-limited high cell density cultivations from small to pilot plant scale using an enzyme-controlled glucose delivery system.

机构信息

Laboratory of Bioprocess Engineering, Department of Biotechnology, Technische Universität Berlin, Ackerstraße 71-76, ACK-24, D-13355 Berlin, Germany.

出版信息

N Biotechnol. 2012 Jan 15;29(2):235-42. doi: 10.1016/j.nbt.2011.11.004. Epub 2011 Nov 9.

DOI:10.1016/j.nbt.2011.11.004
PMID:22100433
Abstract

The enzyme controlled substrate delivery cultivation technology EnBase(®) Flo allows a fed-batch-like growth in batch cultures. It has been previously shown that this technology can be applied in small cultivation vessels such as micro- and deep well plates and also shake flasks. In these scales high cell densities and improved protein production for Escherichia coli cultures were demonstrated. This current study aims to evaluate the scalability of the controlled glucose release technique to pilot scale bioreactors. Throughout all scales, that is, deep well plates, 3 L bioreactor and 150 L bioreactor cultivations, the growth was very similar and the model protein, a recombinant alcohol dehydrogenase (ADH) was produced with a high yield in soluble form. Moreover, EnBase Flo also was successfully used as a controlled starter culture in high cell density fed-batch cultivations with external glucose feeding. Here the external feeding pump was started after overnight cultivation with EnBase Flo. Final optical densities in these cultivations reached 120 (corresponding to about 40 g L(-1) dry cell weight) and a high expression level of ADH was obtained. The EnBase cultivation technology ensures a controlled initial cultivation under fed-batch mode without the need for a feeding pump. Because of the linear cell growth under glucose limitation it provides optimal and robust starting conditions for traditional external feed-based processes.

摘要

酶控底物递加培养技术 EnBase(®) Flo 可实现分批培养中的补料分批式生长。先前的研究表明,该技术可应用于微载体和深孔板以及摇瓶等小型培养容器中。在这些规模下,大肠杆菌培养物的细胞密度和蛋白质产量都得到了提高。本研究旨在评估控制葡萄糖释放技术从小规模到中试规模生物反应器的可扩展性。在所有规模下,即深孔板、3 L 生物反应器和 150 L 生物反应器培养中,生长非常相似,模型蛋白重组醇脱氢酶(ADH)以可溶形式高产。此外,EnBase Flo 还成功用作高细胞密度补料分批培养中的控制起始培养物,进行外部葡萄糖补料。在此,外部进料泵在使用 EnBase Flo 过夜培养后开始运行。这些培养物的最终光密度达到 120(相当于约 40 g/L 干细胞重量),并获得了高表达水平的 ADH。EnBase 培养技术可确保在补料分批模式下进行受控初始培养,而无需进料泵。由于在葡萄糖限制下呈线性细胞生长,它为传统的基于外部进料的工艺提供了最佳和稳健的起始条件。

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