On near-wall behavior of particles in a dilute turbulent gas-solid flow using kinetic theory of granular flows

被引:18
作者
Dehghan, Maziar [1 ]
Tabrizi, Hassan Basirat [1 ]
机构
[1] Amirkabir Univ Technol, Mech Eng Dept, Tehran, Iran
关键词
Granular temperature; Turbulent boundary layer; Kinetic theory; Two-fluid model; Near wall; Particle inertia; BOUNDARY-LAYER; NUMERICAL-SIMULATION; FLUIDIZED-BEDS; FLAT-PLATE; MODULATION; PHASE; PIPE;
D O I
10.1016/j.powtec.2012.03.003
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Motion of particles in a dilute turbulent boundary layer, near a flat wall is simulated numerically. Eulerian-Eulerian two-way coupled model is used. Closures for the particulate-phase equations are derived from the kinetic theory of granular flow. One equation model is used to model turbulence in the gas-phase. Effects of inertial parameters of solid-phase such as flow density, material density, particle diameter and free stream velocity are investigated. Furthermore, effects of granular temperature and particulate viscosity on motion of particles are discussed. Simulation results are compared with available numerical and experimental results. Results show that the granular temperature and solid-phase viscosity have a noticeable effect on simulation accuracy especially near the wall. Results are closer to experimental results when implementing the inlet granular temperature which is equal to area-weighted average of granular temperature in the boundary layer. Non-dimensional velocity profiles of solid-phase have a general trend and their dependence on location and free stream velocity is found very weak. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:273 / 280
页数:8
相关论文
共 22 条
[1]   INSTABILITIES AND THE FORMATION OF BUBBLES IN FLUIDIZED-BEDS [J].
ANDERSON, K ;
SUNDARESAN, S ;
JACKSON, R .
JOURNAL OF FLUID MECHANICS, 1995, 303 :327-366
[2]  
Arpaci VS., 1984, CONVECTIVE HEAT TRAN
[3]   Numerical simulation and validation of dilute turbulent gas-particle flow with inelastic collisions and turbulence modulation [J].
Benavides, Aldo ;
van Wachem, Berend .
POWDER TECHNOLOGY, 2008, 182 (02) :294-306
[4]   Simulation of particles and gas flow behavior in the riser section of a circulating fluidized bed using the kinetic theory approach for the particulate phase [J].
Benyahia, S ;
Arastoopour, H ;
Knowlton, TM ;
Massah, H .
POWDER TECHNOLOGY, 2000, 112 (1-2) :24-33
[5]  
Dartevelle S., 2003, THESIS MICHIGAN TU H
[6]   A BUBBLING FLUIDIZATION MODEL USING KINETIC-THEORY OF GRANULAR FLOW [J].
DING, J ;
GIDASPOW, D .
AICHE JOURNAL, 1990, 36 (04) :523-538
[7]  
Elghobashi S., 1994, APPL SCI RES, V52, P309
[8]  
Gidaspow D., 1994, Multiphase Flow and Fluidization, P1
[9]   PARTICLE MOTION IN A TURBULENT PIPE-FLOW [J].
GOVAN, AH ;
HEWITT, GF ;
NGAN, CF .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1989, 15 (03) :471-481
[10]   Numerical simulation of the Reynolds number effect on gas-phase turbulence modulation [J].
Hadinoto, Kunn ;
Curtis, Jennifer Sinclair .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2009, 35 (02) :129-141