Hostname: page-component-76fb5796d-9pm4c Total loading time: 0 Render date: 2024-04-29T14:53:16.796Z Has data issue: false hasContentIssue false

Marangoni effects of adsorption—desorption controlled surfactants on the leading end of an infinitely long bubble in a capillary

Published online by Cambridge University Press:  26 April 2006

K. J. Stebe
Affiliation:
Department of Chemical Engineering, The Johns Hopkins University, Baltimore, MD 21218, USA
D. Barthès-Biesel
Affiliation:
Université de Technologie de Compiègne URA 858, BP 649, 60206 Compiègne Cedex, France

Abstract

The leading end of an infinitely long gas bubble which displaces a viscous surfactant solution in a capillary tube is studied. The surfactant is present at elevated concentration and has sorption controlled mass transfer. The displaced fluid wets the wall, forming a continuous liquid film between the bubble and the capillary wall. Both the thickness of this film and the additional pressure required to aspirate the bubble depend upon the Marangoni stresses caused by non-uniform surfactant adsorption along the interface. The equations governing this flow are solved at asymptotically small capillary number for the case where the balances of momentum and mass transfer are coupled to leading order. As the Marangoni effect is increased over several orders of magnitude, the additional pressure and the wetting-layer thickness increase above the stress-free interface values found by Bretherton (1961) and approach an upper bound of 42/3 times the Bretherton values. Accompanying changes in the surface tension, Marangoni stress and surface velocity profiles as this upper bound is approached are described. Finally, surface viscosities that are intrinsic to the interfacial region are incorporated in the analysis. When small departures from surface equilibrium states are considered, the terms representing surface viscous effects have the same functional form as the Marangoni stresses and result in thicker films and higher additional pressures.

Type
Research Article
Copyright
© 1995 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

Agrawal, M. L. & Neuman, R. 1988 Surface diffusion in monomolecular films II. Experiment and theory. J. Colloid Interface Sci. 12, 366380.Google Scholar
Barthès-Biesel, D., Moulai-Mostefa, N. & Meister, E. 1986 Effect of surfactants on the flow of large gas bubbles in capillary tubes. Proc. Physicochem. Hydrodyn. NATO Conf. La Rabida, Spain (ed. M. Verlarde).
Borhan, A. & Mao, C.-F. 1992 Effect of surfactants on the motion of drops through circular tubes. Phys. Fluids A 4 (12), 26282640.Google Scholar
Bretherton, F. P. 1961 The motion of long bubbles in tubes. J. Fluid Mech. 10, 166168.Google Scholar
Chang, H. C. & Ratulowski, J. 1987 Bubble transport in capillaries AIChE Annual Meeting, 15–20 November, New York, paper 681.
Chen, J. D. 1985 Measuring the film thickness surrounding a bubble inside a capillary. J. Colloid Interface Sci. 109, 341349.Google Scholar
Djabbarah, N. F. & Wasan, D. T. 1982 Dilatational viscoelastic properties of fluid interfaces — III. Chem. Engng Sci. 37 (2), 175184.Google Scholar
Ginley, G. M. & Radke, C. J. 1989 The influence of soluble surfactants on the flow of long bubbles through a cylindrical capillary. ACS Symp. Series, 396, 480501.Google Scholar
Goldsmith, H. L. & Mason, S. G. 1963 The flow of suspensions through tubes II. Single larger bubbles. J. Colloid Interface Sci. 18, 237261.Google Scholar
Herbolzheimer, E. 1987 The effect of surfactant on the motion of a bubble in a capillary AIChE Annual Meeting, 15–20 November, New York, paper 68.
Hirasaki, G. & Lawson, J. B. 1986 Mechanism of foam flow in porous media: apparent viscosity in smooth capillaries. Soc. Petr. Engng J. 25, 176190.Google Scholar
Jiang, T.-T., Chen, J.-D. & Slattery, J. C. 1983 Nonlinear interfacial stress-deformation behavior measured with several interfacial viscometers. J. Colloid Interface Sci. 96, 719.Google Scholar
Levich, V. G. 1962 Physicochemical Hydrodynamics. Prentice Hall.
Marchessault, R. F. & Mason, S. G. 1960 Flow of entrapped bubbles through a capillary. Ind. Engng Chem. 52 (1), 7981.Google Scholar
Park, C. W. 1991 Effects of insoluble surfactants on dip coating. J. Colloid Interface Sci. 146, 382394.Google Scholar
Park, C. W. 1992 Influence of soluble surfactants on the motion of a finite bubble in a capillary tube. Phys. Fluids A 4 (11), 23352346.Google Scholar
Park, C. W. & Homsy, G. M. 1983 Two phase displacement in Hele-Shaw cells: Theory. J. Fluid Mech. 139, 291308.Google Scholar
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
Schwartz, L. W., Princen, H. M. & Kiss, A. D. 1986 On the motion of bubbles in capillary tubes. J. Fluid Mech. 172, 259275.Google Scholar
Scriven, L. E. 1960 Dynamics of a fluid interface equation of motion for Newtonian surface fluids. Chem. Engng Sci. 12, 98108.Google Scholar
Stebe, K. S., Lin, S. Y. & Maldarelli, C. 1991 Remobilizing surfactant retarded particle interfaces. I. Stress-free conditions at the interfaces of micellar solutions of surfactants with fast sorption kinetics. Phys. Fluids A 3 (1), 320.CrossRefGoogle Scholar
Wei, L. Y. & Slattery, J. C. 1976 Experimental study of nonlinear surface stress-deformation behavior with a deep channel viscometer. Colloid and Interface Science, vol. 4, pp. 399420. Academic.