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
酶
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 Lin Luo,Ruimei Hong,Juanjuan Wang,Chuanyang Shang,Zikun Wang,Zhuhong Yang,Yong Koy Bong,Thomas Daußmann
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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