NADPH-dependent alcohol dehydrogenase (ADH) from Thermoanaerobacter sp. was kinetically characterized using reduction of acetophenone as a model. To achieve 98% conversion of acetophenone, cofactor regeneration by oxidation of 2-propanol with the same enzyme was used. The enzyme was stable in the batch reactor. It was enantioselective towards (S)-1-phenylethanol (ee>99.5%). Due to its high deactivation in continuously operated stirred tank reactor (kd=0.0141 min-1) there was no way to keep high conversion of acetophenone at 98%. The deactivation occurred in the repetitive batch as well. A mathematical model for the acetophenone reduction with cofactor regeneration describing the behaviour in a batch, repetitive-batch and continuously stirred tank reactor was developed.

In this work, a model describing the complete enzyme catalysed synthesis of N-acetylneuraminic acid (Neu5Ac) from N-acetyl-D-glucosamine (GlcNAc) is presented. It includes the combined reaction steps of epimerisation from GlcNAc to N-acetyl-D-mannosamine (ManNAc) and the aldol condensation of ManNAc with sodium pyruvate yielding Neu5Ac. The model is expedient to predict the reaction course for various initial and feed concentrations and therefore to calculate reaction times and yields. The equilibrium constants calculated from the kinetic constants via the Haldane relationship correspond with experimental values very well (0.26 calculated and 0.24 experimental value for the epimerisation, 27.4 l mol(-1) calculated and 28.7 l mol(-1) experimental for the aldol condensation). The actual relevance of the model is shown by a scale-up. Using the model, an optimisation of reaction conditions in consideration of different targets is possible. Exemplarily, it is presented how the optimal ratio of the two enzymes in the reaction can be determined and how the composition of the reaction solution in a fed-batch reactor can be designed to meet downstream processing needs.

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A new continuous production process has been developed for optically active pure (2R,5R)-hexanediol. The process uses resting whole cells of Lactobacillus kefir DSM 20587 as a biocatalyst. The reduction of (2,5)-hexanedione to (2R,5R)-hexanediol was carried out in a 2-L continuously operated membrane reactor. Conversion of (2,5)-hexanedione was nearly quantitative and the selectivity between product and intermediate was 78% for the product. Enantioselectivity and diastereoselectivity were >99% for the whole period. The productivity of L. kefir could be increased by factor 30. (2R,5R)-Hexanediol was continuously produced over 5 days with a space−time yield of 64 g·L-1·d-1.

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