CFD studies on mass transfer of gas-to-particle cluster in a circulating fluidized bed

被引:26
|
作者
Wang, Shuyan [1 ]
Yang, Xu [1 ]
Lu, Huilin [1 ]
Yu, Long [2 ]
Wang, Shuai [1 ]
Ding, Yonlong [3 ]
机构
[1] Harbin Inst Technol, Sch Energy Sci & Engn, Harbin 150001, Peoples R China
[2] Harbin Boiler Co Ltd, Harbin 150046, Peoples R China
[3] Univ Leeds, Inst Particle Sci & Engn, Leeds LS2 9JT, W Yorkshire, England
关键词
Mass transfer; Particle cluster; Sherwood number; CFD; Circulating fluidized bed; TRANSFER COEFFICIENT; MESOSCALE STRUCTURES; PACKED-BED; RISER; HEAT; NUMBER; WALL;
D O I
10.1016/j.compchemeng.2008.10.020
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
Mass transfer of air to naphthalene particle cluster in a circulating fluidized bed (CFB) is investigated via computational fluid dynamic (CFD) approach. Distributions of naphthalene vapor concentration and velocity in the spherical cluster are numerically predicted. The computed results indicate that the mass transfer of air to particles in the cluster is reduced due to the particle clustering and increments of particle size and temperature. Influences of the porosity of the cluster, inlet gas velocity and temperature on mass transfer of air to the cluster are analyzed. The mass transfer coefficients of gas to cluster increase with the increase of porosity of the cluster and inlet air velocity, but decrease with the particle diameter. The down-moving cluster gives higher mass transfer than that of the upward moving cluster. The computed Sherwood numbers are compared with the estimated values from empirical equations reported in literature. (C) 2008 Published by Elsevier Ltd.
引用
收藏
页码:393 / 401
页数:9
相关论文
共 50 条
  • [31] Characteristics of gas-solid mass transfer in a cocurrent downflow circulating fluidized bed reactor
    Luo, Baolin
    Yan, Dong
    Ma, Ying L.
    Barghi, Shahzad
    Zhu, Jesse
    CHEMICAL ENGINEERING JOURNAL, 2007, 132 (1-3) : 9 - 15
  • [32] CFD modeling of gas-solid flow in an internally circulating fluidized bed
    Feng, Yuqing
    Swenser-Smith, Tim
    Witt, Peter J.
    Doblin, Christian
    Lim, Seng
    Schwarz, M. Phil
    POWDER TECHNOLOGY, 2012, 219 : 78 - 85
  • [33] Cluster and Bed-to-wall Heat Transfer Characteristics in a Dual Circulating Fluidized Bed
    Seo, Myung Won
    Suh, Young Ho
    Kim, Sang Done
    Park, Sunwon
    Lee, Dong Hyun
    Song, Byung Ho
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (04) : 2048 - 2061
  • [34] CFD Simulation of Mass Transfer around Spherical Particles in Fluidized Bed
    Vatani, Zoha
    Taghizadeh, Majid
    Orouj, Reza
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2011, 9
  • [35] CFD simulation of mass transfer around spherical particles in fluidized bed
    Vatani Z.
    Taghizadeh M.
    Orouj R.
    International Journal of Chemical Reactor Engineering, 2011, 9
  • [36] A Local Model for Gas-Liquid Mass Transfer in a Gas-Liquid-Solid Circulating Fluidized Bed
    Liu, Zhengliang
    Zheng, Ying
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2004, 2
  • [37] A local model for gas-liquid mass transfer in a gas-liquid-solid circulating fluidized bed
    Liu, Zhengliang
    Zheng, Ying
    International Journal of Chemical Reactor Engineering, 2004, 2
  • [38] Axial and radial heat transfer studies in a circulating fluidized bed
    Reddy, BV
    Nag, PK
    INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 1997, 21 (12) : 1109 - 1122
  • [39] CFD simulation of gas and particle flow and a carbon capture process using a circulating fluidized bed (CFB) reacting loop
    Ghadirian, Emad
    Abbasian, Javad
    Arastoopour, Hamid
    POWDER TECHNOLOGY, 2019, 344 : 27 - 35
  • [40] An enhanced correlation for gas-particle heat and mass transfer in packed and fluidized bed reactors
    Zhu, Li-Tao
    Liu, Yuan-Xing
    Luo, Zheng-Hong
    CHEMICAL ENGINEERING JOURNAL, 2019, 374 : 531 - 544