Lawrence James, O'Sullivan Brian, Lye Gary J, Wohlgemuth Roland, Szita Nicolas
Department of Biochemical Engineering, University College London, Torrington Place, London WC1E 7JE, UK.
J Mol Catal B Enzym. 2013 Nov;95(100):111-117. doi: 10.1016/j.molcatb.2013.05.016.
Biocatalytic synthesis in continuous-flow microreactors is of increasing interest for the production of specialty chemicals. However, the yield of production achievable in these reactors can be limited by the adverse effects of high substrate concentration on the biocatalyst, including inhibition and denaturation. Fed-batch reactors have been developed in order to overcome this problem, but no continuous-flow solution exists. We present the design of a novel multi-input microfluidic reactor, capable of substrate feeding at multiple points, as a first step towards overcoming these problems in a continuous-flow setting. Using the transketolase-(TK) catalysed reaction of lithium hydroxypyruvate (HPA) and glycolaldehyde (GA) to l-erythrulose (ERY), we demonstrate the transposition of a fed-batch substrate feeding strategy to our microfluidic reactor. We obtained a 4.5-fold increase in output concentration and a 5-fold increase in throughput compared with a single input reactor.
连续流微反应器中的生物催化合成对于特种化学品的生产越来越受到关注。然而,这些反应器中可实现的产量可能会受到高底物浓度对生物催化剂的不利影响的限制,包括抑制和变性。为了克服这个问题,已经开发了补料分批反应器,但不存在连续流解决方案。我们提出了一种新型多输入微流控反应器的设计,该反应器能够在多个点进料底物,作为在连续流环境中克服这些问题的第一步。利用转酮醇酶(TK)催化的羟基丙酮酸锂(HPA)和乙醇醛(GA)反应生成赤藓酮糖(ERY),我们展示了补料分批底物进料策略在我们的微流控反应器中的转换。与单输入反应器相比,我们获得了4.5倍的输出浓度增加和5倍的通量增加。