Characterization of a recombinant Escherichia coli TOP10 [pQR239] whole-cell biocatalyst for stereoselective Baeyer-Villiger oxidations

被引:64
作者
Doig, SD
Simpson, H
Alphand, V
Furstoss, R
Woodley, JM
机构
[1] UCL, Dept Biochem Engn, London WCIE 7JE, England
[2] CNRS, ESA 6111, Grp Biocatalyse & Chim Fine, F-13288 Marseille 9, France
关键词
recombinant biocatalyst; asymmetric Baeyer-Villiger oxidation; chiral lactone;
D O I
10.1016/S0141-0229(02)00317-4
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
This paper describes the kinetic characterization of a recombinant whole-cell biocatalyst for the stereoselective Baeyer-Villiger type oxidation of bicyclo[3.2.0]hept-2-en-6-one to its corresponding regio-isomeric lactones (-)-(1 S,5R)-2-oxabicyclo [3.3.0] oct-6-en-3 -one and (-)-(1R,5S)-3-oxabicyclo[3.3.0]oct-6-en-2-one. Escherichia coli TOP10 [pQR239], expressing cyclohexanone monooxygenase (CHMO) from Acinetobacter calcoaceticus (NCIMB 9871), was shown to be suitable for this biotransformation since it expressed CHMO at a high level, was simple to produce, contained no contaminating lactone hydrolase activity and allowed the intracellular recycle of NAD(P)H necessary for the biotransformation. A small-scale biotransformation reactor (20 ml) was developed to allow rapid collection of intrinsic kinetic data. In this system, the optimized whole-cell biocatalyst exhibited a significantly lower specific lactone production activity (55-60 mumol min(-1) g(-1) dry weight) than that of sonicated cells (500 mumol min(-1) g(-1) dry weight). It was shown that this shortfall was comprised of a difference in the pH optima of the two biocatalyst forms and mass transfer limitations of the reactant and/or product across the cell barrier. Both reactant and product inhibition were evident. The optimum ketone concentration was between 0.2 and 0.4 g 1(-1) and at product concentrations above 4.5-5 g 1(-1) the specific activity of the whole cells was zero. These results suggest that a reactant feeding strategy and in situ product removal should be considered in subsequent process design. (C) 2002 Elsevier Science Inc. All rights reserved.
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页码:347 / 355
页数:9
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