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Other titre : Modélisation mathématique de la production de cellulase dans un réacteur airlift

dc.contributor.advisorProulx, Pierrefr
dc.contributor.authorBannari, Rachidfr
dc.date.accessioned2014-05-15T12:41:19Z
dc.date.available2014-05-15T12:41:19Z
dc.date.created2009fr
dc.date.issued2009fr
dc.identifier.isbn9780494642245fr
dc.identifier.urihttp://savoirs.usherbrooke.ca/handle/11143/1930
dc.description.abstractFossil fuel is an important energy source, but is unavoidabiy running out. Since the cellulosic material is the most abundant source of organic matter, the ethanol, which is produced from cellulosic waste materials, is gaining more and more attention. These materials are cheap, renewable and their availability makes them superior compared to other raw materials. The cellulose must be hydrolyzed to glucose before it can be fermented to ethanol. The enzymatic hydrolysis of cellulose using cellulase enzymes is the most widely used method. The production cost of cellulase enzymes is the major cost in ethanol manufacture. To optimize the cost of ethanol production, enzyme stability needs to be improved through maintaining the activity of the enzymes and by optimizing the production of the cellulase. The aim of researchers, engineers and industrials is to get more biomass for the same cost. The filamentous fungus Trichoderma reesei has a long history in the production of the cellulase enzymes. This production can be influenced strongly by varying the growth media and culture conditions (pH, temperature, DO, agitation,... ). At present, it is my opinion that no modelling study has included both the hydrodynamic and kinetic aspects to investigate the effect of shear and mass transfer on the morphology of microorganisms that influence the rheology of the broth and production of cellulase. This thesis presents the development of a mathematical model for cellulase production and the growth of biomass in an airlift bioreactor. The kinetic model is coupled with the methodology of two-phase flow using mathematical models based on the bubble break-up and coalescence to predict mass transfer rate, which is one of the critical factor in the fermentation. A comparison between the results obtained by the developed model and the experimental data is given and discussed. The design proposed for the airlift geometry by Ahamed and Vermette enables us to get a high mass transfer and production rate. The results are very promising with respect to the potential of such a model for industrial use as a prediction tool, and even for design.fr
dc.language.isoengfr
dc.publisherUniversité de Sherbrookefr
dc.rights© Rachid Bannarifr
dc.subjectOpenFOAMfr
dc.subjectAirliftfr
dc.subjectTrichoderma reeseifr
dc.subjectKineticsfr
dc.subjectMass transferfr
dc.subjectInterfacial areafr
dc.subjectFermentationfr
dc.subjectBiomassfr
dc.subjectLactosefr
dc.subjectCellulasefr
dc.subjectCellulosefr
dc.subjectCFDfr
dc.subjectComputational fluid dynamicsfr
dc.subjectMass transferfr
dc.subjectBreak-upfr
dc.subjectCoalescencefr
dc.subjectPopulation balance equationfr
dc.titleMathematical modeling of cellulase production in an airlift bioreactorfr
dc.title.alternativeModélisation mathématique de la production de cellulase dans un réacteur airliftfr
dc.typeThèsefr
tme.degree.disciplineGénie chimiquefr
tme.degree.grantorFaculté de géniefr
tme.degree.levelDoctoratfr
tme.degree.namePh.D.fr


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