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Theory of surface deposition from boundary layers containing condensable vapour and particles

Published online by Cambridge University Press:  10 May 2009

J. C. NEU
Affiliation:
Department of Mathematics, University of California at Berkeley, Berkeley, CA 94720, USA
A. CARPIO
Affiliation:
Departamento de Matemática Aplicada, Universidad Complutense de Madrid, E-28040 Madrid, Spain
L. L. BONILLA*
Affiliation:
G. Millán Institute of Fluid Dynamics, Nanoscience and Industrial Mathematics, Universidad Carlos III de Madrid, 28911 Leganés, Spain
*
Email address for correspondence: [email protected]

Abstract

Heterogeneous condensation of vapours mixed with a carrier gas in the stagnation point boundary layer flow near a cold wall is considered in the presence of solid particles much larger than the mean free path of vapour particles. The supersaturated vapour condenses on the particles by diffusion, and particles and droplets are thermophoretically attracted to the wall. Assuming that the heat of vaporization is much larger than kB, where is the temperature far from the wall, vapour condensation occurs in a condensation layer (CL). The CL width and characteristics depend on the parameters of the problem, and a parameter R yielding the rate of vapour scavenging by solid particles is particularly important. Assuming that the CL is so narrow that temperature, particle density and velocity do not change appreciably inside it, an asymptotic theory is found, the δ-CL theory, that approximates very well the vapour and droplet profiles, the dew point shift and the deposition rates at the wall for wide ranges of the wall temperature w and the scavenging parameter R. This theory breaks down for w very close to the maximum temperature yielding non-zero droplet deposition rate, w, M. If the width of the CL is assumed to be zero (0-CL theory), the vapour density reaches local equilibrium with the condensate immediately after it enters the dew surface. The 0-CL theory yields appropriate profiles and deposition rates in the limit as R → ∞ and also for any R, provided w is very close to w, M. Nonlinear multiple scales also improve the 0-CL theory, providing good uniform approximations to the deposition rates and the profiles for large R or for moderate R and w very close to w, M, but it breaks down for other values of w and small R.

Type
Papers
Copyright
Copyright © Cambridge University Press 2009

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References

REFERENCES

Batchelor, G. K. & C. Shen, C. 1985 Thermophoretic deposition of particles in gas flowing over cold surfaces. J. Colloid Interface Sci. 107, 2137.CrossRefGoogle Scholar
Castillo, J. L. & Rosner, D. E. 1988 A nonequilibrium theory of surface deposition from particle-laden, dilute condensible vapour-containing laminar boundary layers. Intl J. Multiphase Flow 14, 99120.CrossRefGoogle Scholar
Castillo, J. L. & Rosner, D. E. 1989 Theory of surface deposition from a unary dilute vapour-containing steam, allowing for condensation within the laminar boundary layer. Chem. Engng Sci. 44, 925937.CrossRefGoogle Scholar
Davis, E. J. 1983 Transport phenomena with single aerosol particles. Aerosol Sci. Technol. 2, 121144.CrossRefGoogle Scholar
Delale, C. F. & Crighton, D. G. 1998 Prandtl–Meyer flows with homogeneous condensation. Part 1. Subcritical flows. J. Fluid Mech. 359, 2347.CrossRefGoogle Scholar
Filippov, A. V. 2003 Simultaneous particle and vapour deposition in a laminar boundary layer. J. Colloid Interface Sci. 257, 212.CrossRefGoogle Scholar
García Ybarra, P. L. & Castillo, J. L. 1997 Mass transfer dominated by thermal diffusion in laminar boundary layers. J. Fluid Mech. 336, 379409.CrossRefGoogle Scholar
Gökoglu, S. A. & Rosner, D. E. 1986 Thermophoretically augmented mass transfer rates to solid walls across laminar boundary layers. AIAA J. 24, 172179.CrossRefGoogle Scholar
Luo, X. S., Lamanna, G., Holten, A. P. C. & van Dongen, M. E. H. 2007 Effects of homogeneous condensation in compressible flows: Ludwieg-tube experiments and simulations. J. Fluid Mech. 572, 339366.CrossRefGoogle Scholar
Paoli, R., Helie, J. & Poinsot, T. 2004 Contrail formation in aircraft wakes. J. Fluid Mech. 502, 361373.CrossRefGoogle Scholar
Peeters, P., Luijten, C. C. M. & van Dongen, M. E. H. 2001 Transport phenomena with single aerosol particles. Intl J. Heat Mass Transfer 44, 181193.CrossRefGoogle Scholar
Pyykönen, J. & Jokiniemi, J. 2003 Modelling alkali chloride superheater deposition and its implications. Fuel Process. Technol. 80, 225262.CrossRefGoogle Scholar
Rosner, D. E. 2000 Transport Processes in Chemically Reacting Flow Systems. Dover.Google Scholar
Schlichting, H. & Gersten, K. 2000 Boundary Layer Theory, 8th edn.Springer.CrossRefGoogle Scholar
Tandon, P. & Murtagh, M. 2005 Particle vapour interaction in deposition systems: influence on deposit morphology. Chem. Engng Sci. 60, 16851699.CrossRefGoogle Scholar
Zheng, F. 2002 Thermophoresis of spherical and non-spherical particles: a review of theories and experiments. Adv. Colloid Interface Sci. 97, 253276.CrossRefGoogle ScholarPubMed