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

被引:42
作者
Mols, B [1 ]
Oliemans, RVA [1 ]
机构
[1] Delft Univ Technol, Lab Aero & Hydrodynam, JM Burgers Ctr Fluid Mech, Delft, Netherlands
关键词
particle deposition; particle dispersion; deposition rate; turbulent diffusion; annular flow; horizontal flow;
D O I
10.1016/S0301-9322(97)00043-8
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
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. (C) 1997 Elsevier Science Ltd.
引用
收藏
页码:55 / 75
页数:21
相关论文
共 23 条
[1]   CIRCUMFERENTIAL VARIATION OF INTERCHANGE IN HORIZONTAL ANNULAR 2-PHASE FLOW [J].
ANDERSON, RJ ;
RUSSELL, TWF .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1970, 9 (03) :340-&
[2]   USE OF LAGRANGIAN-METHODS TO DESCRIBE DROP DEPOSITION AND DISTRIBUTION IN HORIZONTAL GAS-LIQUID ANNULAR FLOWS [J].
BINDER, JL ;
HANRATTY, TJ .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1992, 18 (06) :803-820
[3]  
Chesters A. K., 1975, International Journal of Multiphase Flow, V2, P191, DOI 10.1016/0301-9322(75)90008-7
[4]  
CSANADY GT, 1963, J ATMOS SCI, V20, P201, DOI 10.1175/1520-0469(1963)020<0201:TDOHPI>2.0.CO
[5]  
2
[6]   DEPOSITION OF SUSPENDED PARTICLES FROM TURBULENT GAS STREAMS [J].
FRIEDLANDER, SK ;
JOHNSTONE, HF .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1957, 49 (07) :1151-1156
[7]   PREDICTION OF THE CIRCUMFERENTIAL DISTRIBUTION OF FILM THICKNESS IN HORIZONTAL AND NEAR-HORIZONTAL GAS-LIQUID ANNULAR FLOWS [J].
FUKANO, T ;
OUSAKA, A .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1989, 15 (03) :403-419
[8]   Relation of deposition to drop size when the rate law is nonlinear [J].
Hay, KJ ;
Liu, ZC ;
Hanratty, TJ .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1996, 22 (05) :829-848
[9]  
Hinze J. O, 1975, TURBULENCE
[10]   DEVELOPMENTS IN THE MODELING OF HORIZONTAL ANNULAR 2-PHASE FLOW [J].
JAMES, PW ;
WILKES, NS ;
CONKIE, W ;
BURNS, A .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1987, 13 (02) :173-198