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dc.contributor.authorJena, H M-
dc.contributor.authorRoy, G K-
dc.contributor.authorMeikap, B C-
dc.identifier.citationChemical Engineering and Processing: Process Intesification (Acceped Post-Print)en
dc.descriptionCopyright for the published version belongs to Elsevieren
dc.description.abstractThe hydrodynamic characteristics viz. the pressure drop, bed expansion and phase holdup profile of a co-current three-phase fluidized bed with an antenna type air sparger have been determined. Correlations for minimum liquid fluidization velocity, bed voidage and gas holdup have been developed. The bed voidage is found to increase with the increase of both liquid and gas velocities. The gas holdup increases with gas Froude number, but decreases with liquid Reynolds number. The gas holdup is a strong function of the Froude number. The experimental values have been found to agree well the correlations.en
dc.format.extent640413 bytes-
dc.subjectGas-liquid-solid fluidizationen
dc.subjectPressure dropen
dc.subjectMinimum fluidization velocityen
dc.subjectBed voidageen
dc.subjectGas holdupen
dc.subjectHollow cylindrical particlesen
dc.titleHydrodynamics of a Gas-Liquid-Solid Fluidized Bed with Hollow Cylindrical Particlesen
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