Steady-state simulation of core-annulus flow in a circulating fluidized bed (CFB) riser

被引:23
作者
Gao, Xi [1 ]
Wang, Li-Jun [1 ]
Wu, Cheng [1 ]
Cheng, You-Wei [1 ]
Li, Xi [1 ]
机构
[1] Zhejiang Univ, Dept Chem & Biol Engn, Hangzhou 310027, Peoples R China
关键词
Fluidization; Hydrodynamics; Multiphase flow; Particle; Turbulence; Steady-state; GAS-PARTICLE FLOW; KINETIC-THEORY APPROACH; NUMERICAL-SIMULATION; VERTICAL PIPE; 2-FLUID MODEL; SOLID FLOWS; TURBULENCE; HYDRODYNAMICS; STRESSES; REACTORS;
D O I
10.1016/j.ces.2012.03.030
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A steady-state multiphase CFD model is proposed for the simulation of core-annulus flow in a circulating fluidized bed (CFB) riser. A CFD model based on Eulerian-Eulerian approach is developed, which incorporates two mechanisms that result in the lateral profiles of solids: mixing of individual particles based on a kinetic theory treatment and mixing of clusters based on a modified k-epsilon turbulence model. The steady-state model can simulate the core-annulus flow more efficiently, which can eliminate the unrealistic sensitivity and need less computational resources comparing with other transient models. This model shows more potential for the simulation of commercial fluidized equipments. The sensitivity of the model predictions involving four parameters indicates that e(w) and phi have weak influence on the correctly prediction of core-annulus flow, while the model remains a certain of sensitivity to e(s) and C-s. The results predicted by the model show good agreement with experimental data under different operating conditions reported by Tartan and Gidaspow (2004). (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:98 / 110
页数:13
相关论文
共 42 条
  • [1] The role of meso-scale structures in rapid gas-solid flows
    Agrawal, K
    Loezos, PN
    Syamlal, M
    Sundaresan, S
    [J]. JOURNAL OF FLUID MECHANICS, 2001, 445 : 151 - 185
  • [2] [Anonymous], 2006, FLUENT 6 3 26
  • [3] Numerical simulation and validation of dilute turbulent gas-particle flow with inelastic collisions and turbulence modulation
    Benavides, Aldo
    van Wachem, Berend
    [J]. 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
    Benyahia, S
    Arastoopour, H
    Knowlton, TM
    Massah, H
    [J]. POWDER TECHNOLOGY, 2000, 112 (1-2) : 24 - 33
  • [5] A time-averaged model for gas-solids flow in a one-dimensional vertical channel
    Benyahia, Sofiane
    [J]. CHEMICAL ENGINEERING SCIENCE, 2008, 63 (09) : 2536 - 2547
  • [6] Study of the ability of multiphase continuum models to predict core-annulus flow
    Benyahia, Sofiane
    Syamlal, Madhava
    O'Brien, Thomas J.
    [J]. AICHE JOURNAL, 2007, 53 (10) : 2549 - 2568
  • [7] Modeling the hydrodynamics of downer reactors based on kinetic theory
    Cheng, Y
    Guo, YC
    Wei, F
    Jin, Y
    Lin, WY
    [J]. CHEMICAL ENGINEERING SCIENCE, 1999, 54 (13-14) : 2019 - 2027
  • [8] TURBULENT GAS-PARTICLE FLOW IN VERTICAL RISERS
    DASGUPTA, S
    JACKSON, R
    SUNDARESAN, S
    [J]. AICHE JOURNAL, 1994, 40 (02) : 215 - 228
  • [9] Hydrodynamics of turbulent fluidized beds of different diameters
    Ellis, N
    Bi, HT
    Lim, CJ
    Grace, JR
    [J]. POWDER TECHNOLOGY, 2004, 141 (1-2) : 124 - 136
  • [10] MEASUREMENTS OF THE COLLISION PROPERTIES OF SMALL SPHERES
    FOERSTER, SF
    LOUGE, MY
    CHANG, AH
    ALLIA, K
    [J]. PHYSICS OF FLUIDS, 1994, 6 (03) : 1108 - 1115