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
  • [21] Particle-fluid heat transfer in a circulating fluidized bed
    Hu, GX
    Cheng, H
    Fan, HJ
    ENERGY AND ENVIRONMENT, 1998, : 553 - 559
  • [22] DETERMINATION OF PARTICLE AND GAS CONVECTIVE HEAT-TRANSFER COMPONENTS IN A CIRCULATING FLUIDIZED-BED
    EBERT, TA
    GLICKSMAN, LR
    LINTS, M
    CHEMICAL ENGINEERING SCIENCE, 1993, 48 (12) : 2179 - 2188
  • [23] Effects of bed particle size on beat transfer in circulating fluidized bed boilers
    Andersson, BA
    POWDER TECHNOLOGY, 1996, 87 (03) : 239 - 248
  • [24] Pulsed gas regulation on heat and mass transfer behaviors in a wet particle fluidized bed
    Tang, Tianqi
    He, Yurong
    Wu, Yongji
    Ren, Anxing
    Wang, Tianyu
    SUSTAINABLE ENERGY TECHNOLOGIES AND ASSESSMENTS, 2021, 44 (44)
  • [25] Experimental and numerical studies on the gas flow surrounding a single cluster applied to a circulating fluidized bed
    Moran, JC
    Glicksman, LR
    CHEMICAL ENGINEERING SCIENCE, 2003, 58 (09) : 1879 - 1886
  • [26] Modelling of dense gas-particle flow in a circulating fluidized bed by Distinct Cluster Method (DCM)
    Liu, Xiangjun
    Xu, Xuchang
    POWDER TECHNOLOGY, 2009, 195 (03) : 235 - 244
  • [27] Experimental and theoretical investigation of mass transfer in a circulating fluidized bed
    Hou, Baolin
    Tang, Hailong
    Zhang, Haiying
    Shao, Guoqiang
    Li, Hongzhong
    Zhu, Qingshan
    CHEMICAL ENGINEERING SCIENCE, 2013, 102 : 354 - 364
  • [28] Mass transfer and reaction behaviour of a circulating fluidized bed reactor
    Vollert, Joachim
    Werther, Joachim
    Chemical Engineering and Technology, 1994, 17 (03): : 201 - 209
  • [29] ON THE CLUSTER STRUCTURE OF A CIRCULATING FLUIDIZED BED
    Teplitskii, Yu. S.
    JOURNAL OF ENGINEERING PHYSICS AND THERMOPHYSICS, 2005, 78 (02) : 316 - 322
  • [30] Circulating fluidized bed with high mass ratio of solid to gas
    Li, H
    Xu, DL
    Cheng, FA
    Feng, SH
    Horio, M
    Circulating Fluidized Bed Technology VIII, 2005, : 770 - 777