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Motion of a particle generated by chemical gradients Part 1. Non-electrolytes

Published online by Cambridge University Press:  20 April 2006

J. L. Anderson
Affiliation:
Department of Chemical Engineering, Carnegie-Mellon University, Pittsburgh, PA 15213, U.S.A.
M. E. Lowell
Affiliation:
Department of Chemical Engineering, Carnegie-Mellon University, Pittsburgh, PA 15213, U.S.A.
D. C. Prieve
Affiliation:
Department of Chemical Engineering, Carnegie-Mellon University, Pittsburgh, PA 15213, U.S.A.

Abstract

When a particle is placed in a fluid in which there is a non-uniform concentration of solute, it will move toward higher or lower concentration depending on whether the solute is attracted to or repelled from the particle surface. A quantitative understanding of this phenomenon requires that the equations representing conservation of mass and momentum within the fluid in the vicinity of the particle are solved. This is accomplished using a method of matched asymptotic expansions in a small parameter L/a, where a is the particle radius and L is the length scale characteristic of the physical interaction between solute and particle surface. This analysis yields an expression for particle velocity, valid in the limit L/a → 0, that agrees with the expression obtained by previous researchers. The result is cast into a more useful algebraic form by relating various integrals involving the solute/particle interaction energy to a measurable thermodynamic property, the Gibbs surface excess of solute Γ. An important result is that the correction for finite L/a is actually O(Γ/Ca), where C is the bulk concentration of solute, and could be O(1) even when L/a is orders of magnitude smaller.

Type
Research Article
Copyright
© 1982 Cambridge University Press

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References

Adamson, A. W. 1967 Physical Chemistry of Surfaces. Wiley Interscience.
Anderson, J. L. 1981 Configurational effects on the reflection coefficient for rigid solutes in capillary pores. J. Theor. Biol. 90, 405.Google Scholar
Anderson, J. L. & Malone, D. M. 1974 Mechanism of osmotic flow in porous membranes. Biophys. J. 14, 957.Google Scholar
Berg, J. C. 1972 Interfacial phenomena in fluid phase separation processes. In Recent Developments in Separation Science (ed. N. N. Li), vol. 2, p. 3. Chemical Rubber Company.
Brenner, H. & Leal, L. G. 1977 A model of surface diffusion on solids. J. Colloid Interface Sci. 62, 238.Google Scholar
Brenner, H. & Leal, L. G. 1978 A micromechanical derivation of Fick's law for interfacial diffusion of surfactant molecules. J. Colloid Interface Sci. 65, 191.Google Scholar
Derjaguin, B. V. & Dukhin, S. S. 1971 Application of thermodynamics of irreversible processes to the electrodiffusion theory of electrokinetic effects. In Research in Surface Forces (ed. B. V. Derjaguin), vol. 3, p. 269. Consultants Bureau.
Derjaguin, B. V., Dukhin, S. S. & Koptelova, M. M. 1972 Capillary osmosis through porous partitions and properties of boundary layers of solutions. J. Colloid Interface Sci. 38, 584.Google Scholar
Derjaguin, B. V., Dukhin, S. S. & Korotkova, A. A. 1961 Diffusiophoresis in electrolyte solutions and its role in the mechanism of film-formation from rubber latexes by the method of ionic deposition. Kolloidn. Zh. 23, 53.Google Scholar
Dukhin, S. S. & Derjaguin, B. V. 1974 Electrokinetic phenomena. In Surface and Colloid Science, (ed. E. Matijevic), vol. 7, p. 322. Wiley.
Happel, J. & Brenner, H. 1965 Low Reynolds Number Hydrodynamics. Prentice-Hall.
Morrison, F. A. 1970 Electrophoresis of a particle of arbitrary shape. J. Colloid Interface Sci. 34, 210.Google Scholar
Prieve, D. C., Smith, R. E., Sander, R. A. & Gerhart, H. L. 1979 Chemiphoresis: acceleration of hydrosol deposition by ionic surface reactions. J. Colloid Interface Sci. 71, 267.Google Scholar
Ruckenstein, E. 1964 Influence of Marangoni effect on the mass transfer coefficient. Chem. Engng Sci. 19, 505.Google Scholar
Ruckenstein, E. 1981 Can phoretic motion be treated as interfacial tension gradient driven phenomena? J. Colloid Interface Sci. 83, 77.Google Scholar
Van Dyke, M. 1964 Perturbation Methods in Fluid Mechanics. Academic.
Young, N. O., Goldstein, J. S. & Block, M. J. 1959 The motion of bubbles in a vertical temperature gradient. J. Fluid Mech. 6, 350.Google Scholar