Drop Breakup in Turbulent Stirred Tank Contactors. Part I: Effect of Dispersed-Phase Viscosity.

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dc.contributor.authorCalabrese, Richard V.en_US
dc.contributor.authorChang, T.P.K.en_US
dc.contributor.authorDang, P.T.en_US
dc.contributor.departmentISRen_US
dc.date.accessioned2007-05-23T09:37:41Z
dc.date.available2007-05-23T09:37:41Z
dc.date.issued1987en_US
dc.description.abstractThe extent to which dispersed-phase viscosity influences equilibrium mean drop size and drop size distribution at constant interfacial tension is determined for dilute suspensions by dispersing silicone oils of various viscosity grades in water. A mechanistic model for mean drop size is developed which predicts the moderate-viscosity data and whose parameters correlate the high-viscosity results. Tends in the mean size data coincide with those for the drop size distribution, which broadens considerably as viscosity increases and suggests a dependency on breakage mechanism.en_US
dc.format.extent791133 bytes
dc.format.mimetypeapplication/pdf
dc.identifier.urihttp://hdl.handle.net/1903/4593
dc.language.isoen_USen_US
dc.relation.ispartofseriesISR; TR 1987-85en_US
dc.titleDrop Breakup in Turbulent Stirred Tank Contactors. Part I: Effect of Dispersed-Phase Viscosity.en_US
dc.typeTechnical Reporten_US

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