Technische Universität Berlin, Chair of Chemical and Process Engineering, Berlin, Germany.
Biotechnol J. 2010 Aug;5(8):813-21. doi: 10.1002/biot.201000130.
The screening of catalysts, substrates or conditions in the early stages of bioprocess development requires an enormous number of experiments and is a tedious, expensive and time-consuming task. Currently available screening systems can only be operated in batch or fed-batch mode, which can lead to severe misinterpretations of screening results. For example, catalysts that are inhibited by substrates or accumulating products will be excluded from further investigations in the early stages of process development despite the fact that they might be superior to other candidates in a different operational mode. Important and advantageous properties such as turnover stability can also be overshadowed by product inhibition. The aim of this study was to develop a novel screening system that enables continuous feeding of substrates and continuous removal of products. A prototype based on the membrane reactor concept was designed and operated for a model reaction, the hydrolysis of cellulose.
在生物工艺开发的早期阶段,对催化剂、底物或条件进行筛选需要进行大量的实验,这是一项繁琐、昂贵且耗时的任务。目前可用的筛选系统只能在分批或补料分批模式下运行,这可能会导致对筛选结果的严重误解。例如,在工艺开发的早期阶段,尽管某些催化剂可能在不同的操作模式下优于其他候选物,但那些受底物或积累产物抑制的催化剂可能会被排除在进一步研究之外。产物抑制也会掩盖一些重要且有利的性质,如周转率稳定性。本研究的目的是开发一种新型的筛选系统,能够连续进料和连续去除产物。基于膜反应器概念的原型被设计并用于模型反应,即纤维素的水解。