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One-line monitoring, state and parameter estimation, adaptive/computer control and dynamic optimization of a continuous bioreactor

dc.contributor.advisorHill, Gordon A.en_US
dc.contributor.advisorRohani, Sohraben_US
dc.contributor.committeeMemberPostlethwaite, Johnen_US
dc.contributor.committeeMemberEsmail, Mohameden_US
dc.creatorThatipamala, Ramakrishnaiahen_US
dc.date.accessioned2008-09-23T09:17:31Zen_US
dc.date.accessioned2013-01-04T04:59:44Z
dc.date.available2009-09-29T08:00:00Zen_US
dc.date.available2013-01-04T04:59:44Z
dc.date.created1993en_US
dc.date.issued1993en_US
dc.date.submitted1993en_US
dc.description.abstractIn this research program, various important aspects for computer-based adaptive control and optimization strategy for a continuous bioreactor, have been investigated. The study was carried out in the following four phases: (a) development of a new method for on-line monitoring of biomass concentration; (b) measurement of kinetics of growth of S.cerevisiae; (c) dynamic bioreactor simulation studies; and (d) experimental control of a continuous bioreactor. An interesting observation was made in absorption of light by yeast cells at "high" concentrations leading to a new equation: log (T/T0) = K log (C/C0), while developing a suitable method for on-line monitoring of yeast cell concentrations. A consistent theoretical explanation was developed starting from the fundamental assumptions of Beer-Lambert's law. This equation was shown to be valid for several optically sensitive solutions [with negative deviations] and thus has the potential of becoming a law. The underlying reasoning behind this phenomenon may improve our present day understanding about absorption of electromagnetic radiation by various substances. Based on this new concept, a novel spectrophotometric technique has been developed and successfully implemented for on-line monitoring of a wide range of yeast cell concentrations in a continuous bioreactor [which has been considered a difficult task in the literature due to lack of reliable instrumentation]. To the author's knowledge, this is the first successful method for on-line monitoring of "high" biomass concentrations which could be implemented for process control applications. This approach may lead to a new generation of instruments in spectroscopy. Extensive batch and continuous experiments were carried out on a well-defined medium using S. cerevisiae at different initial glucose concentrations. The biomass yield was found to be a function of the inhibitory environment of the bioreactor. Four new correlations have been proposed to explain the inhibitory kinetics of ethanol fermentation. These experimental results are expected to have a significant influence in formulating the fermenter design variables and control strategy for optimizing the productivity of ethanol fermentation process. Based on extensive simulation studies, an algorithm [called the SE algorithm] was successfully formulated using state equations: (a) for on-line estimation of important unmeasurable states and critical time-varying parameters; and (b) for adaptive control and dynamic optimization of a bioprocess. Based on simulation studies, a numerical technique was also developed to improve the convergence of the extended Kalman filter algorithm. The SE algorithm was implemented for on-line state estimation and dynamic optimization of a lab-scale [450 mL working volume] continuous ethanol fermenter. An IBM PC along with an OPTO board were used for on-line data acquisition and for execution of the optimization algorithm. A number of experiments were carried out to verify the performance and true adaptive nature of the algorithm. The experimental results clearly illustrate the successful development and implementation of computer-based adaptive control and dynamic optimization strategies to a continuous bioprocess.en_US
dc.identifier.urihttp://hdl.handle.net/10388/etd-09232008-091731en_US
dc.language.isoen_USen_US
dc.titleOne-line monitoring, state and parameter estimation, adaptive/computer control and dynamic optimization of a continuous bioreactoren_US
dc.type.genreThesisen_US
dc.type.materialtexten_US
thesis.degree.departmentChemical Engineeringen_US
thesis.degree.disciplineChemical Engineeringen_US
thesis.degree.grantorUniversity of Saskatchewanen_US
thesis.degree.levelDoctoralen_US
thesis.degree.nameDoctor of Philosophy (Ph.D.)en_US

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