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dc.contributor.authorPanneerselvam, R-
dc.contributor.authorSavithri, S-
dc.contributor.authorSurender, G D-
dc.date.accessioned2015-08-27T08:05:51Z-
dc.date.available2015-08-27T08:05:51Z-
dc.date.issued2008-
dc.identifier.citationChemical Engineering Research & Design 86(12A):1331-1344;Dec 2008en_US
dc.identifier.issn0263-8762-
dc.identifier.urihttp://ir.niist.res.in:8080/jspui/handle/123456789/1992-
dc.description.abstractIn the present work, CFD simulations have been carried out to study solid suspension in gas-liquid-solid mechanically agitated contactor using Eulerian-Eulerian multifluid approach along with standard k - epsilon turbulence model. A multiple frame of reference (MFR) has been used to model the impeller and tank region. The CFD model predictions are compared qualitatively with the literature experimental data and quantitatively with our experimental data. The present study also involves the effects of impeller design, particle size and gas flow rate on the critical impeller speed for solid suspension in gas-liquid-solid mechanically agitated contactor. The values predicted by CFD simulation for critical impeller speed agrees well with experimental data for various operating conditions.en_US
dc.language.isoenen_US
dc.publisherInstitution of Chemical Engineers/ Elsevieren_US
dc.subjectStirred tanken_US
dc.subjectCFDen_US
dc.subjectEulerian-Eulerianen_US
dc.subjectGas-liquid-soliden_US
dc.subjectStirred slurry reactoren_US
dc.subjectCritical impeller speeden_US
dc.titleCFD modeling of gas-liquid-solid mechanically agitated contactoren_US
dc.typeArticleen_US
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