dc.contributorOtto von Guericke University
dc.contributorUniversidade Estadual Paulista (Unesp)
dc.date.accessioned2018-12-11T16:40:16Z
dc.date.available2018-12-11T16:40:16Z
dc.date.created2018-12-11T16:40:16Z
dc.date.issued2015-01-01
dc.identifierProcedia Engineering, v. 102, p. 362-371.
dc.identifier1877-7058
dc.identifierhttp://hdl.handle.net/11449/168214
dc.identifier10.1016/j.proeng.2015.01.163
dc.identifier2-s2.0-84950119863
dc.description.abstractSolid-state fermentation is gaining increasing importance for the production of high-added value products, for instance enzymes, from agro-industrial by-products. The main difficulty in operating this process in packed-bed bioreactors is the development of temperature and moisture gradients along the reactor length which decrease the overall productivity. In this work a practically relevant feedback control scheme is developed that allows influencing and equalizing the moisture and temperature distributions along the packed-bed bioreactor during solid-state fermentation. This prevents locally critical process conditions which may necessitate the shutdown of the operation of the bioreactor.
dc.languageeng
dc.relationProcedia Engineering
dc.relation0,282
dc.rightsAcesso aberto
dc.sourceScopus
dc.subjectdistributed parameter system
dc.subjectdrying
dc.subjectfeedback control
dc.subjectheat and mass transfer
dc.subjectsolid-state fermentation
dc.titleModel-based control of enzyme yield in solid-state fermentation
dc.typeActas de congresos


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