1976
DOI: 10.1002/aic.690220411
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The effect of surfactant on the terminal and interfacial velocities of a bubble or drop

Abstract: y y = wall-shearrate A , = eigenvalue = dimensionless mixing cup solute concentration + = distance transverse t o flow = volume fraction of particles Stream functions are derived for a spherical droplet in creeping flow with an arbitrary surface tension gradient a t its interface. The stream functions are used to show theoretically that the terminal velocity is reduced and that the interfacial velocitv is retarded, emeciallv near the rear of the M. DOUGLAS LEVAN and JOHN NEWMAN , I droplet, when a trace of… Show more

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Cited by 97 publications
(53 citation statements)
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“…The specialization of this solution for the boundary conditions given in Eqs. 10,12 and 13 and suitable boundedness conditions already has been performed in another context by Levan and Newman (1976), who were interested in the slow buoyant migration of a fluid droplet in a continuous medium with a uniform concentration of surfactant far away from the droplet. Thus, the interested reader is referred to their article for details.…”
mentioning
confidence: 97%
“…The specialization of this solution for the boundary conditions given in Eqs. 10,12 and 13 and suitable boundedness conditions already has been performed in another context by Levan and Newman (1976), who were interested in the slow buoyant migration of a fluid droplet in a continuous medium with a uniform concentration of surfactant far away from the droplet. Thus, the interested reader is referred to their article for details.…”
mentioning
confidence: 97%
“…1 (b). For this geometry there exists a solution of the Stokes equation for the fluid flow field inside and outside of the droplet as well as the fluid velocity at the interface [35,36]. The solution at the interface is given in terms of the surface tension gradient:…”
Section: Diffusion-advection-reaction Equationmentioning
confidence: 99%
“…(6) as additional boundary condition to the general polynomial solutions an expression for the interfacial velocity reads [19,23] …”
Section: Flow Field Near a Dropletmentioning
confidence: 99%
“…This surface (Marangoni) stress has to be balanced by viscous stresses which are caused by a Marangoni flow tangential to the droplet surface. Thus the continuity of the tangential stress between the outer and inner bulk fluids in presence of Marangoni stresses at the surface has to be replaced by [18][19][20] …”
Section: Flow Field Near a Dropletmentioning
confidence: 99%