Full Text Available

Note: Clicking the button above will open the full text document at the original institutional repository in a new window.

Modelling of batch and fed-batch ethanol fermentation

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,...

Full description

Saved in:
Bibliographic Details
Main Author: Glyn, Julian E H
Other Authors: Hansford, Geoffrey Spearing
Format: Thesis
Language:English
Published: Department of Chemical Engineering 2016
Subjects:
Tags: Add Tag
No Tags, Be the first to tag this record!
_version_ 1867613206714777600
access_status_str Open Access
author Glyn, Julian E H
author2 Hansford, Geoffrey Spearing
author_browse Glyn, Julian E H
Hansford, Geoffrey Spearing
author_facet Hansford, Geoffrey Spearing
Glyn, Julian E H
author_sort Glyn, Julian E H
collection Thesis
description 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.
format Thesis
id oai:open.uct.ac.za:11427/21832
institution University of Cape Town (South Africa)
language eng
last_indexed 2026-06-10T12:32:27.580Z
license_str Not specified — see source repository
provenance_str_mv Harvested via OAI-PMH from UCTD — University of Cape Town Open Access Repository
publishDate 2016
publishDateRange 2016
publishDateSort 2016
publisher Department of Chemical Engineering
publisherStr Department of Chemical Engineering
record_format dspace
source_str UCTD — University of Cape Town Open Access Repository
spelling oai:open.uct.ac.za:11427/21832 Modelling of batch and fed-batch ethanol fermentation Glyn, Julian E H Hansford, Geoffrey Spearing Fermentation Alcohol Chemical Engineering 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. 2016-09-20T12:31:41Z 2016-09-20T12:31:41Z 1989 Master Thesis Masters MSc (Eng) http://hdl.handle.net/11427/21832 eng application/pdf Department of Chemical Engineering Faculty of Engineering and the Built Environment University of Cape Town
spellingShingle Fermentation
Alcohol
Chemical Engineering
Glyn, Julian E H
Modelling of batch and fed-batch ethanol fermentation
thesis_degree_str Master's
title Modelling of batch and fed-batch ethanol fermentation
title_full Modelling of batch and fed-batch ethanol fermentation
title_fullStr Modelling of batch and fed-batch ethanol fermentation
title_full_unstemmed Modelling of batch and fed-batch ethanol fermentation
title_short Modelling of batch and fed-batch ethanol fermentation
title_sort modelling of batch and fed batch ethanol fermentation
topic Fermentation
Alcohol
Chemical Engineering
url http://hdl.handle.net/11427/21832
work_keys_str_mv AT glynjulianeh modellingofbatchandfedbatchethanolfermentation