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在填充床反应器中使用固定化生物催化剂连续生产手性1,3 - 丁二醇:具有不对称氢转移生物还原的有前景的生物催化方法。

Continuous production of chiral 1,3-butanediol using immobilized biocatalysts in a packed bed reactor: promising biocatalysis method with an asymmetric hydrogen-transfer bioreduction.

作者信息

Itoh Nobuya, Nakamura Masatoshi, Inoue Kousuke, Makino Yoshihide

机构信息

Department of Biotechnology, Faculty of Engineering (Biotechnology Research Center), Toyama Prefectural University, Kurokawa 5180, Imizu, Toyama 939-0398, Japan.

出版信息

Appl Microbiol Biotechnol. 2007 Jul;75(6):1249-56. doi: 10.1007/s00253-007-0957-1. Epub 2007 Apr 19.

Abstract

An asymmetric hydrogen-transfer biocatalyst consisting of mutated Rhodococcus phenylacetaldehyde reductase (PAR) or Leifsonia alcohol dehydrogenase (LSADH) was applied for some water-soluble ketone substrates. Among them, 4-hydroxy-2-butanone was reduced to (S)/(R)-1,3-butanediol, a useful intermediate for pharmaceuticals, with a high yield and stereoselectivity. Intact Escherichia coli cells overexpressing mutated PAR (Sar268) or LSADH were directly immobilized with polyethyleneimine or 1,6-diaminehexane and glutaraldehyde and evaluated in a batch reaction. This system produced (S)-1,3-butanediol [87% enantiomeric excess (e.e.)] with a space time yield (STY) of 12.5 mg h(-1) ml(-1) catalyst or (R)-1,3-butanediol (99% e.e.) with an STY of 60.3 mg h(-1) ml(-1) catalyst, respectively. The immobilized cells in a packed bed reactor continuously produced (R)-1,3-butanediol with a yield of 99% (about 49.5 g/l) from 5% (w/v) 4-hydroxy-2-butanoate over 500 h.

摘要

一种由突变的红球菌苯乙醛还原酶(PAR)或利夫森氏醇脱氢酶(LSADH)组成的不对称氢转移生物催化剂被应用于一些水溶性酮底物。其中,4-羟基-2-丁酮被还原为(S)/(R)-1,3-丁二醇,这是一种用于制药的有用中间体,产率和立体选择性都很高。将过表达突变PAR(Sar268)或LSADH的完整大肠杆菌细胞用聚乙烯亚胺或1,6-己二胺和戊二醛直接固定,并在分批反应中进行评估。该系统分别以12.5 mg h(-1) ml(-1)催化剂的时空产率(STY)产生(S)-1,3-丁二醇[对映体过量(e.e.)为87%]或以60.3 mg h(-1) ml(-1)催化剂的STY产生(R)-1,3-丁二醇(e.e.为99%)。填充床反应器中的固定化细胞在500多小时内从5%(w/v)的4-羟基-2-丁酸盐连续生产(R)-1,3-丁二醇,产率为99%(约49.5 g/l)。

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