Simulated pulsed flow of gas and particles in a horizontal oppose-pulsed gas jets of bubbling fluidized bed

被引:14
|
作者
Wang Lin [1 ]
Qi Guoli [2 ]
Tao Ming [1 ]
Liu Xuemin [2 ]
Hassan, Muhammad [3 ]
Lu Huilin [1 ]
机构
[1] Harbin Inst Technol, Sch Energy Sci & Engn, Harbin 150001, Heilongjiang, Peoples R China
[2] China Special Equipment Inspect & Res Inst, Beijing 100029, Peoples R China
[3] Univ Engn & Technol Peshawar, Ctr Adv Studies Energy, Peshawar 25000, Pakistan
关键词
Gas-particle flow; Oppose-pulsed gas jets; Fluidization; Computational fluid dynamics; Reynolds stress; NUMERICAL-SIMULATION; PENETRATION; COMPUTATION;
D O I
10.1016/j.apt.2018.09.035
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Flow behavior of gas and particles with a horizontal oppose-pulsed gas jets are simulated by means of a three dimensional Computational Fluid Dynamics (CFD) model with the kinetic theory of granular flow in a gas-particles bubbling fluidized bed. The effects of amplitudes and frequencies on the hydrodynamics of gas and particles are analyzed. The simulation results are presented in terms of phase velocity vector plot, volume fraction of phases, granular temperature, power spectrum and Reynolds stresses in the bed. Results show that the impingement caused by the oppose-pulsed gas jets oscillates with the variation of pulsed gas velocity. The impingement zone with the high solid volume fraction reciprocates from the left side to the right side through the bed center with the variation of pulsed jet gas velocities. The lateral velocity and gas turbulent kinetic energy, granular temperature and Reynolds stresses of gas and particles are larger near the pulsed gas jets than that at the center of the bed. The large dispersion coefficients of particles using the horizontal oppose-pulsed gas jets enhance the mixing of particles in gas-solid fluidized bed. (C) 2018 The Society of Powder Technology Japan. Published by Elsevier B.V. and The Society of Powder Technology Japan. All rights reserved.
引用
收藏
页码:3507 / 3519
页数:13
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