Hostname: page-component-cd9895bd7-q99xh Total loading time: 0 Render date: 2024-12-19T02:56:36.811Z Has data issue: false hasContentIssue false

The influence of surfactant adsorption on the motion of a fluid sphere in a tube. Part 1. Uniform retardation controlled by sorption kinetics

Published online by Cambridge University Press:  26 April 2006

Zunqing He
Affiliation:
Levich Institute for Physicochemical Hydrodynamics, Department of Chemical Engineering, City College of New York, New York, NY 10031, USA
Zeev Dagan
Affiliation:
Department of Mechanical Engineering, City College of New York, New York, NY 10031, USA
Charles Maldarelli
Affiliation:
Levich Institute for Physicochemical Hydrodynamics, Department of Chemical Engineering, City College of New York, New York, NY 10031, USA

Abstract

This paper presents a study of the steady, axisymmetric, creeping translation of a fluid sphere in a tube for the case in which surfactant is adsorbed onto the fluid sphere interface. Marangoni stresses caused by the convective redistribution of surfactant are computed perturbatively in the limit of sorption-controlled uniform retardation, and fully converged numerical solutions of the creeping-flow equations including the Marangoni stress are obtained by a collocation technique.

The results indicate that when the fluid sphere moves in a liquid which is at rest at infinity, the Marangoni stress retards the particle velocity. This retardation generally increases with the sphere to tube diameter ratio up to a value of approximately 0.6, whereupon the retardation begins to level off or even become reduced. When the sphere is suspended in a Poiseuille flow, stagnation rings develop on the sphere surface, and the Marangoni stresses that derive from this surface convection pattern can accelerate the fluid particle when the particle velocity is small with respect to the Poiseuille centreline velocity, but in the same direction as that velocity.

Type
Research Article
Copyright
© 1991 Cambridge University Press

Access options

Get access to the full version of this content by using one of the access options below. (Log in options will check for institutional or personal access. Content may require purchase if you do not have access.)

References

Bleys, G. & Joos, P., 1985 Adsorption kinetics of bolaform surfactants at the air/water interface. J. Phys. Chem. 89, 10271032.Google Scholar
Brenner, H.: 1970 Pressure drop due to the motion of neutrally buoyant particles in duct flows. J. Fluid Mech. 43, 641660.Google Scholar
Brenner, H.: 1971 Pressure drop due to the motion of neutrally buoyant particles in duct flows. II. Spherical droplets and bubbles. Indust. Engng Chem. Fundam. 10, 537543.Google Scholar
Bretherton, F.: 1961 The motion of long bubbles in tubes. J. Fluid Mech. 10, 166188.Google Scholar
Davis, R. E. & Acrivos, A., 1966 The influence of surfactants on the creeping motion of bubbles. Chem. Engng Sci. 21, 681685.Google Scholar
Frumkin, A. & Levich, V., 1947 Zh. Fiz. Khim. 21, 1183.
Ginley, G. M. & Radke, C. J., 1989 The influence of soluble surfactants on the flow of a long bubble through a cylindrical capillary. Am. Chem. Soc. Symp. Series 96, 480501.Google Scholar
Goldsmith, H. & Mason, S., 1963 The flow of suspensions through tubes. II. Single large bubbles. J. Colloid Interface Sci. 35, 183199.Google Scholar
Haberman, W. L. & Sayre, R. M., 1958 Motion of rigid and fluid spheres in stationary and moving liquids inside cylindrical tubes. David W. Taylor Model Basin Rep. 1143. US Navy Dept.
Happel, J. & Brenner, H., 1973 Low Reynolds Number Hydrodynamics, 2nd edn. Noordhoff.
Harper, J. F.: 1973 On bubbles with small immobile adsorbed films rising in liquids at low Reynolds numbers. J. Fluid Mech. 58, 539545.Google Scholar
Harper, J. F.: 1982 Surface activity and bubble motion. Appl. Sci. Res. 38, 343351.Google Scholar
He, Z., Dagan, Z. & Maldarelli, C., 1990 The influence of surfactant on the motion of a fluid sphere in a tube. Part 2. The stagnant cap regime. J. Fluid Mech. (submitted).Google Scholar
Herbolzheimer, E.: 1987 The effect of surfactant on the motion of a bubble in a capillary. AIChE Annual Meeting, Nov. 15–20, NY, Paper 68j.Google Scholar
Hirasaki, G. J. & Lawson, J. B., 1985 Mechanisms of foam flow in porous media: Apparent viscosity in smooth capillaries. Soc. Petrol. Engrs J. 25, 176190.Google Scholar
Holbrook, J. A. & Levan, M. D., 1983a Retardation of droplet motions by surfactant. Part 1 Theoretical development and asymptotic solutions. Chem. Engng Commun. 20, 191207.Google Scholar
Holbrook, J. A. & Levan, M. D., 19836 Retardation of droplet motion by surfactant. Part 2 Numerical solutions for exterior diffusion, surface diffusion and adsorption kinetics. Chem. Engng Commun. 20, 273290.Google Scholar
Hommelen, J. R.: 1959 The elimination of errors due to evaporation of the solute in the determination of surface forces. J. Colloid Sci. 14, 385400.Google Scholar
Hyman, W. A. & Skalak, R., 1969 Tech. Rep. 3, Proj. No. NR 062–393, Dept. Civil Engng and Engng Mech., Columbia University.
Hyman, W. A. & Skalak, R., 1970 Tech. Rep. 5, Proj. No. NR 062–393, Dept. Civil Engng and Engng Mech., Columbia University.
Joos, P. & Sebrien, G., 1989 Adsorption kinetics of lower alkanols at the air-water interface: Effect of structure makers and structure breakers. 127, 97103.
Leichtberg, S., Pfeffer, R. & Wainbaum, S., 1976 Stokes flow past finite coaxial clusters of spheres in a circular cylinder. Intl J. Multiphase Flow 3, 147169.Google Scholar
Levan, M. D. & Newman, J., 1976 The effect of surfactant on the terminal and interfacial velocities of a bubble or drop. AIChE J. 22, 695.Google Scholar
Levan, M. D. & Holbrook, J., 1989 Motion of a droplet containing surfactant. J. Colloid Interface Sci. 131, 242251.Google Scholar
Levich, V. G.: 1962 Physicochemical Hydrodynamics. Prentice-Hall.
Martinez, M. & Udell, K., 1989 Boundary integral analysis of the creeping flow of long bubbles in capillaries. Tram. ASME E: J. Appl. Mech. 56, 211217.Google Scholar
Martinez, M. & Udell, K., 1990 Axisymmetric creeping motion of drops through circular tubes. J. Fluid Mech. 210, 565591.Google Scholar
Moulai-Mostefa, N., Meister, E. & Bahthes-Biesel, D. 1986 Effect of surfactant on the flow of large gas bubbles in capillary tubes. Physicochemical Hydrodynamics: Interfacial Phenomena. NATO conference, LaRabida, Espagne, July 11–15, 1986.Google Scholar
Newman, J.: 1967 Retardation of falling drops. Chem. Engng Sci. 22, 8385.Google Scholar
Park, C.-W. & Homsy, G. M. 1984 Two phase displacement in Hele-Shaw cells: theory. J. Fluid Mech. 39, 291308.Google Scholar
Probstein, R.: 1989 Physicochemical Hydrodynamics: An Introduction pp. 308311. Butterworths.
Ratulowski, J. & Chang, H.-C. 1990 Marangoni effects of trace impurities on the motion of long gas bubbles in capillaries. J. Fluid Mech. 210, 303328.Google Scholar
Reinelt, D. & Saffman, P., 1985 The penetration of a finger into a viscous liquid in a channel and tube. 8IAM J. Sci. Statist. Comput. 6, 542561.Google Scholar
Sadhal, S. S. & Johnson, R. E., 1982 Stokes flow past bubbles and drops partially coated with thin films. Part 1. Stagnant cap of surfactant film – exact solution. J. Fluid Mech. 126, 237250.Google Scholar
Savic, P.: 1953 Circulation and distortion of liquid drops falling through a viscous medium. Nat. Res. Counc. Can., Div. Mech. Engng Rep. MT-22.Google Scholar
Saville, D. A.: 1973 The effects of interfacial tension gradients and droplet behavior. Chem. Engng J. 5, 251259.Google Scholar
Schechter, R. S. & Farley, R. W., 1963 Interfacial tension gradients and droplet behavior. Can. J. Chem. Engng 41, 103.Google Scholar
Shen, E. I. & Udell, K. S., 1985 A finite element study of low Reynolds number two phase flow in cylindrical tubes. Trans. ASME E: J. Appl. Mech. 52, 253256.Google Scholar
Wang, H. & Skalak, R., 1969 Viscous flow in a cylindrical tube containing a line of spherical particles. J. Fluid Mech. 38, 7596.Google Scholar
Wasserman, M. L. & Slattery, J. C., 1969 Creeping flow past a fluid globule when a trace of surfactant is present. AIChE J. 15, 533548.Google Scholar
Westborg, H. & Hassager, O., 1989 Creeping motion of long bubbles and drops in capillary tubes. J. Colloid Interface Sci. 133, 135147.Google Scholar