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Department of Chemical Engineering

Modelling of batch and fed-batch ethanol fermentation

Abstract

dc:description.abstract

Two series of batch and fed-batch fermentations were carried out using S.cerevisiae in a semi-defined medium containing 200 gl-1 glucose as limiting substrate. Growth rates were calculated and the data used to test the applicability of eight empirical kinetic models. The form proposed by Levenspiel, combining the concept of a limiting ethanol concentration with a power-law form, gave the best results with these data. Glucose concentration was found to have a far smaller, though not negligible, effect on growth rate under these conditions. It was also observed that in fed-batch fermentations the total substrate uptake rate of the broth became constant soon after commencement of feeding, without cessation of growth. It is suggested that ethanol inhibits the synthesis of a rate-controlling enzyme in the glycolyti·c chain, but no previous work could be found to support or refute this explanation. A quasi-mechanistic model of growth under the condition of constant substrate consumption rate is formulated and discussed.

Degree

thesis:*
Grantor dc:publisher.institution
Department of Chemical Engineering
Year dc:date.issued
1989

Author and committee

dc:creator, dc:contributor.*
Author dc:creator
  • Glyn, Julian E H
Advisor dc:contributor.advisor
  • Hansford, Geoffrey Spearing

Rights

Language dc:language.iso
eng

Identifiers

dc:identifier.*
Handle dc:identifier.uri
http://hdl.handle.net/11427/21832
OAI identifier oai:identifier
oai:open.uct.ac.za:11427/21832

Chain of custody

source
Harvested from
University of Cape Town
Base URL
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Last updated
2026-07-22
Source record
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citation

Glyn, Julian E H. Modelling of batch and fed-batch ethanol fermentation. Department of Chemical Engineering, 1989. http://hdl.handle.net/11427/21832