Flow structure of the solids in gas-solid fluidized beds

被引:76
|
作者
Mostoufi, N
Chaouki, J
机构
[1] Ecole Polytech Montreal, Dept Chem Engn, Montreal, PQ H3C 3A7, Canada
[2] Univ Tehran, Proc Design & Simulat Res Ctr, Dept Chem Engn, Fac Engn, Tehran, Iran
关键词
fluidization; hydrodynamics; multiphase flow; powder technology; cluster; particle tracking;
D O I
10.1016/j.ces.2004.06.006
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Existence of clusters in dense fluidized beds was investigated by analyzing the time-position data of a tracer obtained in several radioactive particle tracking experiments. It was found that in the case of sand particles, more gas passes through the bed as bubbles with increasing the superficial gas velocity and in the case of FCC powder, flow of the gas through the bed as bubbles does not increase in the turbulent fluidization regime. Cluster diameters were estimated from their velocities and found that descending clusters are generally larger than ascending ones and the size of both increases with increasing the superficial gas velocity. Bubble velocities evaluated in this work are in good agreement with the correlations in the bubbling regime of the fluidization available in the literature. (C) 2004 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4217 / 4227
页数:11
相关论文
共 50 条
  • [21] Bubbling gas-solid fluidized beds with BDIM
    Pozarnik, M
    Skerget, L
    BOUNDARY ELEMENTS XXI, 1999, 6 : 423 - 432
  • [22] Gas-solid fluidized beds in vortex chambers
    De Wilde, Juray
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2014, 85 : 256 - 290
  • [23] GAS-SOLID HEAT TRANSER IN FLUIDIZED BEDS
    MANN, RS
    FENG, LCL
    INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1968, 7 (03): : 327 - &
  • [24] Critical comparison of hydrodynamic models for gas-solid fluidized beds - Part II: freely bubbling gas-solid fluidized beds
    Patil, DJ
    Annaland, AV
    Kuipers, JAM
    CHEMICAL ENGINEERING SCIENCE, 2005, 60 (01) : 73 - 84
  • [25] On the internal solids circulation rates in freely-bubbling gas-solid fluidized beds
    Medrano, J. A.
    Tasdemir, M.
    Gallucci, F.
    Annaland, M. van Sint
    CHEMICAL ENGINEERING SCIENCE, 2017, 172 : 395 - 406
  • [26] SOLID FLOW BEHAVIOR IN GAS-SOLID FLUIDIZED-BEDS - NEW EXPERIMENTAL TECHNIQUE
    ABRAHAMI, S
    RESNICK, W
    POWDER TECHNOLOGY, 1972, 6 (02) : 113 - &
  • [27] Critical comparison of hydrodynamic models for gas-solid fluidized beds - Part I: bubbling gas-solid fluidized beds operated with a jet
    Patil, DJ
    Annaland, MV
    Kuipers, JAM
    CHEMICAL ENGINEERING SCIENCE, 2005, 60 (01) : 57 - 72
  • [28] Hydrodynamics of gas-solid flow around immersed tubes in bubbling fluidized beds
    He, YR
    Lu, HL
    Sun, QQ
    Yang, LD
    Zhao, YH
    Gidaspow, D
    Bouillard, J
    POWDER TECHNOLOGY, 2004, 145 (02) : 88 - 105
  • [29] Effects of heterogeneous flow on carbon conversion in gas-solid circulating fluidized beds
    Nikku, Markku
    Bordbar, Hadi
    Myohanen, Kari
    Hyppanen, Timo
    FUEL, 2020, 280
  • [30] Effects of riser geometry on gas-solid flow characteristics in circulating fluidized beds
    Tu, Qiuya
    Wang, Haigang
    PARTICUOLOGY, 2020, 49 : 205 - 217