Numerical study of the near-wall behaviour of particles in turbulent pipe flows

被引:70
作者
Portela, LM
Cota, P
Oliemans, RVA
机构
[1] Delft Univ Technol, JM Burgersctr Fluid Mech, Kramers Lab Fys Technol, NL-2628 BW Delft, Netherlands
[2] Delft Univ Technol, JM Burgersctr Fluid Mech, Lab Aero & Hydrodynam, NL-2628 CA Delft, Netherlands
关键词
particles; near wall; turbulent pipe flow; direct numerical simulation;
D O I
10.1016/S0032-5910(01)00501-0
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The near-wall behaviour of particles is important in terms of predicting both the particle-deposition and the near-wall particle-concentration. In this paper, we study the near-wall behaviour of elastic-bouncing small heavy spheric particles in fully developed turbulent pipe flows without gravity, using direct numerical simulations (DNS) with a one-way point-particle approach. The particle-concentration is assumed to be small enough such that the influence of the particles on the fluid and interparticle interactions can be neglected. The focus of the paper is on: (i) the understanding of the differences between elastic-bouncing and absorbing walls, and (ii) the evaluation of simple "local-equilibrium" models. Our results show that the near-wall behaviour of elastic-bouncing walls is very different from absorbing walls. The absence of a mean radial particle-velocity leads to a much higher particle-concentration near the wall than in the case of absorbing walls. This can be explained by the absence of a "mean drag force": the "turbophoretic effect", due to the gradient in the particle-velocity fluctuation in the radial direction, is balanced only by the "drift-velocity", due to a gradient in the particle-concentration. Our results indicate that, from a pragmatic perspective, simple "local-equilibrium" models for the "turbophoretic effect", assuming a proportionality between the particle and fluid "Reynolds-stresses", are adequate, except very close to the wall, where the reduction in the radial fluid-velocity fluctuation is not accompanied by an equivalent reduction in the radial particle-velocity fluctuation. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:149 / 157
页数:9
相关论文
共 16 条
[1]   INTERACTION OF SOLID OR LIQUID PARTICLES AND TURBULENT FLUID-FLOW FIELDS - NUMERICAL-SIMULATION [J].
BROWN, DJ ;
HUTCHINSON, P .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 1979, 101 (02) :265-269
[2]  
COTA P, 1999, MEAH187 DELFT U TECH
[3]   Numerical models for two-phase turbulent flows [J].
Crowe, CT ;
Troutt, TR ;
Chung, JN .
ANNUAL REVIEW OF FLUID MECHANICS, 1996, 28 :11-43
[4]  
Eggels J.G.M., 1994, THESIS DELFT U TECHN
[5]   FULLY-DEVELOPED TURBULENT PIPE-FLOW - A COMPARISON BETWEEN DIRECT NUMERICAL-SIMULATION AND EXPERIMENT [J].
EGGELS, JGM ;
UNGER, F ;
WEISS, MH ;
WESTERWEEL, J ;
ADRIAN, RJ ;
FRIEDRICH, R ;
NIEUWSTADT, FTM .
JOURNAL OF FLUID MECHANICS, 1994, 268 :175-209
[6]  
Ferziger J.H., 2019, Computational Methods for Fluid Dynamics
[8]  
Hinze J. O, 1975, TURBULENCE
[9]   NUMERICAL COMPUTATION OF PARTICLES-TURBULENCE INTERACTION [J].
MCLAUGHLIN, JB .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1994, 20 :211-232
[10]   Review - The transient equation of motion for particles, bubbles, and droplets [J].
Michaelides, EE .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 1997, 119 (02) :233-247