A turbulent diffusion model for particle dispersion and deposition in horizontal tube flow

Abstract Particle dispersion and deposition in a horizontal turbulent tube flow have been studied with a Turbulent Diffusion Model. Dispersion and deposition are modelled as the combined process of turbulent diffusion and gravitational settling fluxes. The particle diffusion coefficient is expressed in terms of the fluid diffusivity, taking into account the inertial effect and the crossing trajectories effect. The analytical solution for the particle concentration in a one-dimensional problem between two horizontal plates is found, and is used to calculate the relative deposition between the top and the bottom wall. It is investigated how this relative deposition depends on the particle diameter, the height of the channel and the Froude number. The one-dimensional analytical solution is used to predict the two-dimensional deposition flux in a tube, and it is investigated how this depends on the particle diameter and the Froude number. The expression for the deposition flux contains the characteristic physical parameters of the deposition problem that have not been recognized in earlier work.

[1]  S. Friedlander,et al.  Deposition of Suspended Particles from Turbulent Gas Streams , 1957 .

[2]  T. W. F. Russell,et al.  Circumferential Variation of Interchange in Horizontal Annular Two-Phase Flow , 1970 .

[3]  T. J. Hanratty,et al.  Relation of deposition to drop size when the rate law is nonlinear , 1996 .

[4]  W. Uijttewaal,et al.  Particle dispersion and deposition in direct numerical and large eddy simulations of vertical pipe flows , 1996 .

[5]  N. S. Wilkes,et al.  Developments in the modelling of horizontal annular two-phase flow , 1987 .

[6]  P. Morse,et al.  Methods of theoretical physics , 1955 .

[7]  S. Paras,et al.  Droplet entrainment and deposition in horizontal annular flow , 1991 .

[8]  A. Ousaka,et al.  Prediction of the circumferential distribution of film thickness in horizontal and near-horizontal gas-liquid annular flows , 1989 .

[9]  M. Reeks,et al.  PARTICLE DEPOSITION FROM A TURBULENT FLOW. I: A STEADY-STATE MODEL FOR HIGH INERTIA PARTICLES , 1994 .

[10]  G. Csanady Turbulent Diffusion of Heavy Particles in the Atmosphere , 1963 .

[11]  M. Reeks On the continuum equations for dispersed particles in nonuniform flows , 1992 .

[12]  A. K. Chesters The applicability of dynamic-similarity criteria to isothermal, liquid-gas, two-phase flows without mass transfer , 1975 .

[13]  M. Reeks The transport of discrete particles in inhomogeneous turbulence , 1983 .

[14]  Geoffrey Ingram Taylor,et al.  Diffusion by Continuous Movements , 1922 .

[15]  T. J. Hanratty,et al.  Droplet flux distributions and entrainment in horizontal gas-liquid flows , 1996 .

[16]  M. Reeks On a kinetic equation for the transport of particles in turbulent flows , 1991 .

[17]  M. Reeks,et al.  A numerical simulation of particle deposition in turbulent boundary layers , 1989 .

[18]  T. J. Hanratty,et al.  Use of lagrangian methods to describe drop deposition and distribution in horizontal gas-liquid annular flows , 1992 .