Wellenbeck Wenzel, Mampel Jörg, Naumer Christian, Knepper Andreas, Neubauer Peter
BRAIN AG (Biotechnology Research and Information Network) Zwingenberg Germany.
Bioprocess Engineering Department of Biotechnology Technische Universität Berlin Berlin Germany.
Eng Life Sci. 2016 Nov 21;17(11):1185-1194. doi: 10.1002/elsc.201600031. eCollection 2017 Nov.
The time-to-market challenge is key to success for consumer goods affiliated industries. In recent years, the dairy industry faces a fast and constantly growing demand for enzymatically produced lactose-free milk products, mainly driven by emerging markets in South America and Asia. In order to take advantage of this opportunity, we developed a fermentation process for lactase (β-galactosidase) from within short time. Here, we describe the process of stepwise increasing the level of control over relevant process parameters during scale-up that established a highly efficient and stable production system. Process development started with evolutionary engineering to generate catabolite-derepressed variants of the wild-type strain. A high-throughput screening mimicking fed-batch cultivation identified a constitutive lactase overproducer with 260-fold improved activity of 4.4 U per milligram dry cell weight when cultivated in glucose minimal medium. During scale-up, process control was progressively increased up to the level of conventional, fully controlled fed-batch cultivations by simulating glucose feed, applying and dissolved oxygen tension -sensor technology to small scale, and by the use of a milliliter stirred tank bioreactor. Additionally, process development was assisted by design-of-experiments optimization of the growth medium employing the response surface methodology.
上市时间挑战是消费品附属行业成功的关键。近年来,乳制品行业面临着对酶法生产的无乳糖乳制品快速且持续增长的需求,这主要由南美和亚洲的新兴市场推动。为了利用这一机遇,我们在短时间内开发了一种乳糖酶(β-半乳糖苷酶)发酵工艺。在此,我们描述了在放大过程中逐步提高对相关工艺参数控制水平的过程,该过程建立了一个高效且稳定的生产系统。工艺开发始于进化工程,以产生野生型菌株的分解代谢物阻遏解除变体。一种模拟补料分批培养的高通量筛选方法鉴定出一种组成型乳糖酶高产菌株,当在葡萄糖基本培养基中培养时,其活性提高了260倍,达到每毫克干细胞重量4.4单位。在放大过程中,通过模拟葡萄糖补料、将溶解氧张力传感器技术应用于小规模培养以及使用毫升搅拌罐生物反应器,逐步将过程控制提高到传统的、完全控制的补料分批培养水平。此外,通过采用响应面方法对生长培养基进行实验设计优化,辅助了工艺开发。