Granular temperature and rotational characteristic analysis of a gas-solid bubbling fluidized bed under different gravities using discrete hard sphere model

被引:14
作者
Wang, Tianyu [1 ]
He, Yurong [1 ]
Kim, Dong Rip [2 ]
机构
[1] Harbin Inst Technol, Dept Power Engn, Harbin, Peoples R China
[2] Hanyang Univ, Dept Mech Engn, Seoul 133791, South Korea
基金
中国国家自然科学基金;
关键词
Granular temperature; Rotational characteristic; Discrete hard sphere model; Different gravities; EULER-EULER; SPOUTED BED; CFD-DEM; SIMULATION; HYDRODYNAMICS; BEHAVIOR; FLOWS; ENVIRONMENTS; VERIFICATION; PRESSURE;
D O I
10.1016/j.powtec.2014.11.005
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A gas-solid bubbling fluidized bed was analyzed by using a discrete hard sphere particle model (DPM). Simulation results were validated by matching them to the results of the previous study. Particle translational and rotational characteristics were investigated in terms of gravities to find out their influences on the particle behaviors. The gravity did not significantly affect the particle macro-scale characteristics, such as particle translational velocity and rotational velocity, but acted an important role in particle micro-scale characteristics like granular temperatures. Particularly, the change of gravity affected the change of the bubble behavior and the particles' pulsation movement, which could lead to the transformation of the overall fluidized state. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:35 / 48
页数:14
相关论文
共 28 条
  • [1] Comparison of the standard Euler-Euler and hybrid Euler-Lagrange approaches for modeling particle transport in a pilot-scale circulating fluidized bed
    Adamczyk, Wojciech P.
    Klimanek, Adam
    Bialecki, Ryszard A.
    Wecel, Gabriel
    Kozolub, Pawel
    Czakiert, Tomasz
    [J]. PARTICUOLOGY, 2014, 15 : 129 - 137
  • [2] A comparative study on the influence of the gas flow rate on the hydrodynamics of a gas-solid spouted fluidized bed using Euler-Euler and Euler-Lagrange/DEM models
    Almohammed, Naser
    Alobaid, Falah
    Breuer, Michael
    Epple, Bernd
    [J]. POWDER TECHNOLOGY, 2014, 264 : 343 - 364
  • [3] Drag force of intermediate Reynolds number flow past mono- and bidisperse arrays of spheres
    Beetstra, R.
    van der Hoef, M. A.
    Kuipers, J. A. M.
    [J]. AICHE JOURNAL, 2007, 53 (02) : 489 - 501
  • [4] Numerical study of segregation using a new drag force correlation for polydisperse systems derived from lattice-Boltzmann simulations
    Beetstra, R.
    van der Hoef, M. A.
    Kuipers, J. A. M.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2007, 62 (1-2) : 246 - 255
  • [5] Beetstra R, 2005, DRAG FORCE RANDOM AR
  • [6] Numerical studies of solid-solid mixing behaviors in a downer reactor for coal pyrolysis
    Chen, Yongpan
    Zhang, Wenbiao
    Guan, Guoqing
    Fushimi, Chihiro
    Tsutsumi, Atsushi
    Wang, Chi-Hwa
    [J]. POWDER TECHNOLOGY, 2014, 253 : 722 - 732
  • [7] Verification of scaling criteria for bubbling fluidized beds by DEM-CFD simulation
    Di Maio, Francesco Paolo
    Di Renzo, Alberto
    [J]. POWDER TECHNOLOGY, 2013, 248 : 161 - 171
  • [8] On the relationship between operating pressure and granular temperature: A discrete particle simulation study
    Godlieb, W.
    Deen, N. G.
    Kuipers, J. A. M.
    [J]. POWDER TECHNOLOGY, 2008, 182 (02) : 250 - 256
  • [9] HIGH-VELOCITY FLUIDIZED-BED REACTORS
    GRACE, JR
    [J]. CHEMICAL ENGINEERING SCIENCE, 1990, 45 (08) : 1953 - 1966
  • [10] CONTACTING MODES AND BEHAVIOR CLASSIFICATION OF GAS - SOLID AND OTHER 2-PHASE SUSPENSIONS
    GRACE, JR
    [J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1986, 64 (03) : 353 - 363