1985
DOI: 10.1002/aic.690310118
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Electroconvective enhancement of mass or heat exchange between a drop or bubble and surroundings in the presence of an interfacial tension gradient

Abstract: a = CD(NRe,t)' = functional form in Eq. 7 = porosity t P = density P = viscosity P NOTATION = drag coefficient = particle diameter = a function appearing in Eq. 4 = acceleration resulting from gravity = Reynolds number defined by Eq. 2 = Reynolds number for a suspension defined by Eq. 9 = Reynolds number based on terminal velocity, defined . = Pm/Pe by Eq. 6 = Ps/Pe = superficial liquid velocity = o r / ut = terminal velocity of a particle in an infinite medium = relative velocity between liquid and particles … Show more

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Cited by 12 publications
(2 citation statements)
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“…Circulation inside a drop or a bubble suspended in a continuous phase, induced by an electric field, was first reported by Taylor (1966) and later by many researchers including Chang and co‐workers (Chang and Berg, 1985a,b). However, in all these studies, the emphasis was on the role of interfacial tension on the circulation flow and in turn on heat and mass transfer.…”
Section: Resultsmentioning
confidence: 95%
“…Circulation inside a drop or a bubble suspended in a continuous phase, induced by an electric field, was first reported by Taylor (1966) and later by many researchers including Chang and co‐workers (Chang and Berg, 1985a,b). However, in all these studies, the emphasis was on the role of interfacial tension on the circulation flow and in turn on heat and mass transfer.…”
Section: Resultsmentioning
confidence: 95%
“…Diffusivities of salts were obtained from Chang and Myerson (1985), and were measured at 25°C. Solubilities at 0°C for gases were calculated using Henry’s law constants (Sanders, 1999), and for salts obtained from Haynes (2012) .…”
Section: Resultsmentioning
confidence: 99%