Fidgett, Michael (1975). Mathematical Modelling of Tower Fermentation Processes. PHD thesis, Aston University.
Abstract
The Fermentation Industries are currently concerned with a number of large-scale processes, including single cell protein production, effluent treatment, and the production of alcoholic beverages. Successful design and optimisation of these new systems is becoming increasingly dependent upon the availability of mathematical models for use in simulation studies. The research described in the thesis has been concerned with the analysis and modelling of some of these microbial processes, in particular those involving tower fermenters. Because of the nature of such processes the work has involved considerable interaction between the basic disciplines of chemical engineering and microbiology. Models of specific aspects of tower fermentation processes are developed in the earlier sections of the thesis, including: (1) a model to describe liquid-phase mixing in bubble columns and tower fermenters; (2) an empirical method for predicting mixing parameters for both the backflow stirred tanks model and the axially-dispersed plug flow model; (3) a theoretical model describing oxygen mass transfer in bubble columns and tower fermentation systems; (4) a detailed review of deterministic kinetic models for microbial processes; (5) a brief review of continuous culture theory and mathematical descriptions of transient microbial behaviour; and (6) analysis and modelling of the batch beer fermentation process. The application of these concepts to the development of comprehensive models for tower fermentation systems is considered in the latter part of the thesis. First, a model describing a continuous beer fermenter is developed, and second, consideration is given to the design and modelling of aerobic tower systems. These models have been useful in: (1) directing current experimental programmes, and (2) high-lighting areas where more research effort is needed. It is hoped that ultimately the models will be suitable for the scale-up, design and optimisation of tower fermentation systems.
Divisions: | College of Engineering & Physical Sciences > School of Infrastructure and Sustainable Engineering > Chemical Engineering & Applied Chemistry |
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Additional Information: | Copyright © Michael Fidgett 1975. Michael Fidgett asserts their moral right to be identified as the author of this thesis. This copy of the thesis has been supplied on condition that anyone who consults it is understood to recognise that its copyright rests with its author and that no quotation from the thesis and no information derived from it may be published without appropriate permission or acknowledgement. If you have discovered material in Aston Publications Explorer which is unlawful e.g. breaches copyright, (either yours or that of a third party) or any other law, including but not limited to those relating to patent, trademark, confidentiality, data protection, obscenity, defamation, libel, then please read our Takedown Policy and contact the service immediately. |
Institution: | Aston University |
Uncontrolled Keywords: | Mathematical modelling,tower fermentation processes |
Last Modified: | 30 Sep 2024 07:23 |
Date Deposited: | 08 Dec 2010 10:25 |
Completed Date: | 1975-02 |
Authors: |
Fidgett, Michael
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