Mixing and solid-liquid mass transfer characteristics in a three phase pulsed plate column with packed bed of solids in interplate spaces-a novel aerobic immobilized cell bioreactor

dc.contributor.authorShetty K, V.S.
dc.contributor.authorSrinikethan, G.
dc.date.accessioned2026-02-05T09:35:39Z
dc.date.issued2011
dc.description.abstractBackground: The pulsed plate column (PPC) with packed bed of solids in the interplate spaces finds use as a three phase aerobic bioreactor and is a potential heterogeneous catalytic reactor. Good knowledge of the extent of mixing in the liquid phase and solid-liquid mass transfer coefficient are essential for modeling, design and optimization of these columns. The present work aims at the study of liquid phase mixing and solid-liquid mass transfer characteristics in a three phase PPC. Results: Residence time distribution studies were performed. Dispersion number was found to increase with increase in liquid superficial velocities, frequency of pulsation, amplitude of pulsation and the vibrational velocities. Increase in frequency and amplitude of pulsation, and hence increase in vibrational velocity, resulted in increase of the solid-liquid mass transfer coefficient. Conclusions: The mixing behaviour in this contactor approximated a mixed flow behaviour. The three phase PPC was found to outperform many other kinds of three phase contactors in terms of solid liquid mass transfer characteristics. Empirical correlations developed can be used for the determination of solid-liquid mass transfer coefficients for three phase PPC and hence can facilitate the design, scale-up and modeling of these columns, when used as chemical or biochemical reactors. © 2011 Society of Chemical Industry.
dc.identifier.citationJournal of Chemical Technology and Biotechnology, 2011, 86, 10, pp. 1310-1320
dc.identifier.issn2682575
dc.identifier.urihttps://doi.org/10.1002/jctb.2674
dc.identifier.urihttps://idr.nitk.ac.in/handle/123456789/27178
dc.subjectAerobic bioreactors
dc.subjectBiochemical reactors
dc.subjectCatalytic reactor
dc.subjectDesign and optimization
dc.subjectDispersion number
dc.subjectEmpirical correlations
dc.subjectImmobilized cells
dc.subjectLiquid Phase
dc.subjectLiquid superficial velocities
dc.subjectLiquid-phase mixing
dc.subjectMixed flows
dc.subjectMixing behaviour
dc.subjectPlate columns
dc.subjectResidence time distribution
dc.subjectResidence time distributions
dc.subjectScale-up
dc.subjectSolid-liquid mass transfer
dc.subjectSolid-liquid mass transfer coefficient
dc.subjectThree phase
dc.subjectBioconversion
dc.subjectBioreactors
dc.subjectCell culture
dc.subjectDispersions
dc.subjectMass transfer
dc.subjectMixing
dc.subjectPacked beds
dc.subjectVibrations (mechanical)
dc.subjectLiquids
dc.subjectbenzoic acid
dc.subjectarticle
dc.subjectbioreactor
dc.subjectchemical parameters
dc.subjectchemical procedures
dc.subjectdispersion
dc.subjectflow rate
dc.subjectliquid phase mixing
dc.subjectpulsed plate column
dc.subjectsolid liquid mass transfer coefficient
dc.titleMixing and solid-liquid mass transfer characteristics in a three phase pulsed plate column with packed bed of solids in interplate spaces-a novel aerobic immobilized cell bioreactor

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