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Please use this identifier to cite or link to this item: http://repository.iitr.ac.in/handle/123456789/1979
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dc.contributor.authorPrasad, Basheshwar Rajendra-
dc.contributor.authorMishra I.M.-
dc.date.accessioned2020-10-06T14:08:13Z-
dc.date.available2020-10-06T14:08:13Z-
dc.date.issued1995-
dc.identifier.citationBioresource Technology (1995), 53(3): 269-275-
dc.identifier.issn9608524-
dc.identifier.urihttps://doi.org/10.1016/0960-8524(95)00096-W-
dc.identifier.urihttp://repository.iitr.ac.in/handle/123456789/1979-
dc.description.abstractA model for growth-associated fermentations is presented for batch cultures of immobilized whole cells. The model encompasses exponential and steady-state growth phases and the effectiveness of the biocatalyst. Based on the model equations, experimental methods have been developed for the determination of the kinetic parameters: maximum specific growth rate (?max), Monod constant (Km) and effectiveness factor (?). These methods are illustrated by ethanol fermentations using Saccharomyces cerevisiae cells entrapped in alginate beads. The kinetic parameters obtained show consistency with those determined for free-cell systems. © 1995.-
dc.language.isoen_US-
dc.relation.ispartofBioresource Technology-
dc.subjectbiomass yield factor-
dc.subjecteffectiveness factor-
dc.subjectexponential growth phase-
dc.subjectGaden type I fermentations-
dc.subjectImmobilized whole cells-
dc.subjectsteady-state growth phase-
dc.titleOn the kinetics and effectiveness of immobilized whole-cell batch cultures-
dc.typeArticle-
dc.scopusid15838004000-
dc.scopusid23668474600-
dc.affiliationPrasad, B., Alternate Hydro Energy Centre, University of Roorkee, Roorkee, 247 667, India-
dc.affiliationMishra, I.M., Department of Chemical Engineering, University of Roorkee, Roorkee, 247 667, India-
dc.description.correspondingauthorPrasad, B.; Alternate Hydro Energy Centre, University of Roorkee, Roorkee, 247 667, India-
Appears in Collections:Journal Publications [CH]

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