Solid-liquid mass transfer in agitated newtonian and non-newtonian fluids

dc.contributor.author	Lal P.; Kumar S.; Upadhyay S.N.; Upadhya Y.D.
dc.date.accessioned	2025-05-24T09:56:26Z
dc.description.abstract	Diffusional mass-transfer rates were experimentally measured by following the rate of dissolution of benzoic acid pellets and spheres (diameter 0.513-2.008 cm) suspended in agitated Newtonian (water, ethylene glycol, and 60% aqueous propylene glycol solution) and in non-Newtonian (1.0%, 2.0%, and 3.0% aqueous (carboxymethyl)cellulose (CMC) solutions) fluids in baffled and unbaffled vessels of diameter 14.5-25.0 cm using disk turbine, plane turbine, and propeller agitators. The influences of various operating and physicochemical parameters were investigated. The results are correlated in terms of dimensionless groups. © 1988, American Chemical Society. All rights reserved.
dc.identifier.doi	https://doi.org/10.1021/ie00079a027
dc.identifier.uri	http://172.23.0.11:4000/handle/123456789/21015
dc.relation.ispartofseries	Industrial and Engineering Chemistry Research
dc.title	Solid-liquid mass transfer in agitated newtonian and non-newtonian fluids

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