1983
DOI: 10.1016/s0017-9310(83)80106-9
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Fluid flow and transfer behavior of a drop translating in an electric field at intermediate Reynolds numbers

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Cited by 29 publications
(4 citation statements)
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“…Taking in account circulatory flows generated by an applied electric field, Morrison (1977) and Griffiths & Morrison (1979) evaluated transfer rate enhancement and found significant electroconvective effects for stationary drops. The numerical investigation of the electrohydrodynamic effects in transfer rate enhancement for spherical drops has been extended further to include both buoyancy-driven flows (Chang, Carleson & Berg 1982;Chang & Berg 1983) and interfacial tension gradients (Chang & Berg 1985). In the present work, we focus on the pure electrohydrodynamic effects on deformable drops under neutrally buoyant conditions, leaving other complications for future research.…”
Section: Introductionmentioning
confidence: 99%
“…Taking in account circulatory flows generated by an applied electric field, Morrison (1977) and Griffiths & Morrison (1979) evaluated transfer rate enhancement and found significant electroconvective effects for stationary drops. The numerical investigation of the electrohydrodynamic effects in transfer rate enhancement for spherical drops has been extended further to include both buoyancy-driven flows (Chang, Carleson & Berg 1982;Chang & Berg 1983) and interfacial tension gradients (Chang & Berg 1985). In the present work, we focus on the pure electrohydrodynamic effects on deformable drops under neutrally buoyant conditions, leaving other complications for future research.…”
Section: Introductionmentioning
confidence: 99%
“…Each distance corresponds to the effective travelling distance for the drops. This arrangement of electrodes was determined so as to obtain a uniform electric filed.16'17) The continuous phase of cyclohexane was supplied from a liquid reservoir [6] by a feed pump [7]. The dispersed phase of aqueous iodine solution was supplied from another liquid reservoir [4] to a stainless steel nozzle (0.1 cm o.d., 0.06cm i.d.)…”
Section: Methodsmentioning
confidence: 99%
“…higher droplet velocities resulting from EHD forces of repulsion exerted on the charged drops in the direction of motion (Thornton, 1968;Bailes, 1981;Takamatsu et al, 1983;Yamaguchi et al, 1985;Vu and Carleson, 1986); enhanced circulations inside and around droplets due to the tangential component of the EHD forces exerted on the droplet surface (Morrison, 1977;Griffiths and Morrison, 1979;Chang et al, 1982;Chang and Berg, 1983); induced droplet oscillations by electric field due to the droplet deformation effect (Thornton, 1976;Wham and Byers, 1987;Scott and Byers, 1989;Basaran et al, 1989;Scott et al, 1990;Yang and Carleson, 1991); interfacial-tension-induced flow by the local variations in the effective interfacial tension due to the presence of electrical charges (Austin et al, 1971;Iyer and Sawistowski, 1974;Carleson and Berg, 1984;Berg, 1985a, 1985b;Carleson and Fuller, 1987). The basic techniques to achieve electrically enhanced liquid-liquid extraction are briefly summarized in Table 1.…”
Section: Electric Fieldsmentioning
confidence: 99%