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A simulation model for the continuous production of acetoin and butanediol using Bacillus subtilis with integrated pervaporation separation
Author(s) -
Dettwiler B.,
Dunn I. J.,
Heinzle E.,
Prenosil J. E.
Publication year - 1993
Publication title -
biotechnology and bioengineering
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 1.136
H-Index - 189
eISSN - 1097-0290
pISSN - 0006-3592
DOI - 10.1002/bit.260410805
Subject(s) - acetoin , chemostat , chemistry , bacillus subtilis , 2,3 butanediol , product inhibition , biomass (ecology) , membrane , pervaporation , chromatography , dilution , fermentation , biochemistry , thermodynamics , non competitive inhibition , biology , permeation , physics , bacteria , genetics , enzyme , agronomy
The potential for producing acetoin and butanediol with a Bacillus subtilis strain was investigated with continuous culture using molasses as carbon substrate. The steady‐state results were influenced by both oxygen and undetermined limiting compounds. Employing the known metabolic pathways, four overall stoichiometry relations were used with an energetic assumption on the energy requirements for biomass formation to establish a linear relations were used with an energetic assumption on the energy requirements for biomass formation to establish a linear relation between the overall rates, whose parameters were determined by linear regression. This provided a relationship for the product formation rate. The chemostat culture data were described with a growth kinetics model, which included limitation by molasses and oxygen as well as diauxic effects and product inhibition. The biokinetics model was combined with an experimentally verified model for the membrane Pervaporation. From this combined model were determined the influence of the membrane characteristics (enrichment factors and membrane area) and the dilution rate on the performance of the integrated process. Simulations revealed that an increase of the enrichment factor, possible by membrane improvement, would have counteracting influences, owing to decreased product inhibition but with lower biomass concentration. © 1993 Wiley & Sons, Inc.