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dc.contributor.authorPanneerselvam, R-
dc.contributor.authorSavithri, S-
dc.contributor.authorSurender, G D-
dc.date.accessioned2014-01-08T04:50:43Z-
dc.date.available2014-01-08T04:50:43Z-
dc.date.issued2009-
dc.identifier.citationIndustrial & Engineering Chemistry Research 48(3):1608-1620;04 Feb 2009en_US
dc.identifier.issn0888-5885-
dc.identifier.urihttp://ir.niist.res.in:8080/jspui/handle/123456789/1019-
dc.description.abstractIn the present study, computational fluid dynamics (CFD) simulations have been carried out to characterize a solid suspension in a gas-liquid-solid mechanically agitated contactor using the Eulerian multifluid approach with a standard k-epsilon turbulence model. A steady state method of 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 (Guha et al. Chem. Eng. Sci. 2007, 62, 6143; Spidla et al. Chem. Eng. J. 2005, 113, 73; Aubin et al. Erp. Therm. Fluid Sci. 2004, 28, 447) and quantitatively with our experimental data. Also the effect of different types of impellers (disk turbine and pitched blade turbine with downward pumping), impeller speed, particle size (125-230 mu m), and gas flow rate (0-1 vvm) on the critical impeller speed for solid suspension in a gas-liquid-solid mechanically agitated contactor is investigated. The values predicted by CFD simulation agree well with experimental data for various operating conditionsen_US
dc.language.isoenen_US
dc.publisherAmerican Chemical Societyen_US
dc.subjectCritical impeller speeden_US
dc.subjectStirred slurry reactoren_US
dc.subjectParticle distributionen_US
dc.subjectCFD simulationsen_US
dc.subjectVesselen_US
dc.subjectTurbineen_US
dc.titleComputational fluid dynamics simulation of solid suspension in a gas-liquid-solid mechanically agitated contactoren_US
dc.typeArticleen_US
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