Transaminase Engineering and Process Development for a Whole-Cell Neat Organic Process to Produce (R)-α-Phenylethylamine

转氨酶 苯乙酮 产量(工程) 异丙胺 生物催化 化学 胺气处理 有机化学 组合化学 催化作用 材料科学 反应机理 冶金
作者
Baoqin Cai,Jiyong Wang,Hu Hu,Sitong Liu,Chengxiao Zhang,Ying Zhu,Marco Bocola,Lei Sun,Yaoyao Ji,Ameng Zhou,Kuifang He,Qinli Peng,Xiao Luo,Ruimei Hong,Juanjuan Wang,Chuanyang Shang,Zikun Wang,Zhuhong Yang,Yong Koy Bong,Thomas Daußmann
出处
期刊:Organic Process Research & Development [American Chemical Society]
卷期号:26 (7): 2004-2012 被引量:6
标识
DOI:10.1021/acs.oprd.1c00409
摘要

The production of (R)-α-phenylethylamine ((R)-α-PEA) from acetophenone is a classic reaction for the characterization of transaminases. However, developing a commercially viable transaminase process to manufacture (R)-α-PEA usually suffers from two drawbacks. One is related to the biocatalyst itself, since transaminases are easily inhibited by (R)-α-PEA at low concentrations. The other drawback is a common low space-time yield of typical transaminase processes, because the reaction equilibrium greatly favors the formation of acetophenone over (R)-α-PEA. In this study, an (R)-selective amine transaminase (TA) from Aspergillus fumigatus Af293 was engineered by a directed evolution for an efficient process to produce (R)-α-PEA. The evolved variant showed an over 3000-fold increase in activity and a tolerance with 2.0 M isopropylamine as well as the complete absence of inhibition by (R)-α-PEA. At the same time, using this evolved TA variant, a continuous neat organic process using whole-cells was developed where the biocatalyst and remaining acetophenone can be efficiently separated from (R)-α-PEA and reused repetitively. This not only decreases the overall cost and waste generation but also achieves a very high space-time yield of up to 168 g L–1 d–1 of (R)-α-PEA in an industrial pilot scale setup.
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