Utilization of the tricarboxylic acid cycle, a reactor design criterion for the microaerobic production of 2,3-butanediol |
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Authors: | Zeng A P Deckwer W D |
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Affiliation: | GBF-Gesellschaft für Biotechnologische Forschung mbH, Biochemical Engineering Division, Mascheroder Weg 1, W-3300 Braunschweig, Germany. |
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Abstract: | A new parameter, the relative utilization of tricarboxylic acid (TCA) cycle beta, is introduced to quantitatively account for the involvement of fermentation pathways and TCA cycle in the utilization of oxygen under oxygen-limiting (microaerobic) conditions. With the facultative anaerobe Enterobacter aerogenes, which produces 2,3-butanediol, a method is proposed to calculate beta from measurement of metabolites and exhaust gas. In continuous culture beta was found to be small under oxygen limitation, indicating that the fermentation pathways were preferred over the TCA cycle and oxygen was almost entirely consumed through oxidation of reduced nicotinamide adenine dinucleotide (NADH(2)) released by fermentation under these conditions. The increase of beta at high oxygen supply revealed a saturation of oxygen utilization through fermentation pathways. It could be concluded that, for the optimal performance of a microaerobic culture, oxygen uptake rate must be kept at such a level that as much NADH(2) as possible from fermentation pathways is oxidized by oxygen, and at the same time the utilization of TCA cycle is kept at a minimum. As the dynamics of the microaerobic culture can be fast, a significant effect of reactor hydrodynamics, i.e., mixing, on the overall performance can be expected. This was confirmed experimentally, and the parameter beta proved to be a useful reactor design criterium for the microaerobic cultivation. (c) 1992 John Wiley & Sons, Inc. |
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Keywords: | 2,3-butanediol microaerobic culture TCA cycle oxygen utilization reactor design mixing |
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