| Literature DB >> 29971481 |
Kathrin Doll1, Anton Rückel1, Peter Kämpf1, Maximilian Wende1, Dirk Weuster-Botz2.
Abstract
Microbial batch production of alcohols by fermentation of CO-rich gases with Clostridia is limited by low volumetric productivities due to the need for formation of organic acids first (acidogenic phase) followed by re-consumption of the acids to form alcohols (solventogenic phase). Continuous autotrophic production of alcohols was made possible with C. carboxidivorans by use of two continuously operated stirred-tank bioreactors in series without cell retention. The pH in the first reactor was controlled to pH 6.0 for continuous growth of the cells. Steady-state concentrations of 3.0 g L-1 acetate and 0.1 g L-1 butyrate were measured at a mean hydraulic residence time of 8.3 h. The pH in the second reactor was controlled to pH 5.0 for enhancing continuous formation of alcohols resulting in steady-state concentrations of 6.1 g L-1 ethanol, 0.7 g L-1 butanol, and 0.1 g L-1 hexanol at a mean hydraulic residence time of 12.5 h. Continuous formation of alcohols from CO was already observed in the first stirred-tank reactor parallel to the formation of acids, whereas re-consumption of acids as well as de-novo syntheses of alcohols from CO was shown in the second stirred-tank reactor. Thus, high final alcohol-to-acid ratios of 3.9 gethanol gacetate-1 and 4.4 gbutanol gbutyrate-1 were achieved in the continuous syngas-fermentation process with C. carboxidivorans.Entities:
Keywords: Acidogenesis and solventogenesis; C. carboxidivorans; Carbon monoxide; Continuous syngas fermentation; Stirred-tank bioreactors in series
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Year: 2018 PMID: 29971481 DOI: 10.1007/s00449-018-1969-1
Source DB: PubMed Journal: Bioprocess Biosyst Eng ISSN: 1615-7591 Impact factor: 3.210