摘要：

The reduction of ethyl 3-oxobutanoate (EOB) to ethyl ( S)-3-hydroxybutanoate (( S)-EHB) by cell suspensions of baker's yeast ( Saccharomyces cerevisiae) in a continuously operated reactor with cell retention has been investigated. The continuous reductions were technically feasible and reproducible. High degrees of conversion (91–98%) and high extents of reduction (88–92%) were obtained. High product concentrations were not achievable due to impractical long residence times needed. In a continuously operated stirred-tank reactor containing 26–31 g dw l 1 of baker's yeast and achieving a product concentration of 20 mM, the overall reduction rate (0.14–0.17 mmol product g dw 1 h 1) remained constant in time indicating the robustness of baker's yeast as biocatalyst at the process conditions applied. The volumetric productivity, which was not optimized, was 0.64 g l 1 h 1. Due to the maintained low EOB concentration, the enantiomeric excess of ( S)-EHB remained high (>98%) during the first 24 h. However, in spite of the low residual EOB level, the enantiomeric excess value decreased slowly to 80–92% in a few days. This is probably due to an increasing level of intrinsic activity in the yeast towards the undesired ( R)-enantiomer. Long-term production of ( S)-EHB in a continuous process, therefore, seems to be hindered by this change in enantioselectivity of the biocatalyst.

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