The influence of the riser exit on the particle residence time distribution in a circulating fluidised bed riser

被引:62
|
作者
Harris, AT
Davidson, JF
Thorpe, RB
机构
[1] Univ Cambridge, Dept Chem Engn, Cambridge, England
[2] Univ Surrey, Dept Chem & Proc Engn, Guildford GU2 7XH, Surrey, England
关键词
circulating fluidised bed; residence time distribution; exit effect;
D O I
10.1016/S0009-2509(03)00215-X
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper reports measurements of the influence of riser exit geometry upon the particle residence time distribution in the riser of a square cross section, cold model, circulating fluidised bed. The bed is operated within the fast fluidisation regime. The fast response particle RTD technique developed by Harris et al. (Chem. Eng. J. 89 (2002) 127-142) was used to measure the residence time distribution. The geometry of the riser exit is shown to have a modest but consistent influence upon the particle RTD; the influence of operating conditions, i.e. superficial gas velocity and solids flux is more significant. Increasing the refluxing effect of the riser exit increases the mean, variance and breakthrough time and decreases the coefficient of variation of the residence time distribution. Changes in reflux do not have a systematic effect upon the skewness of the RTD. (C) 2003 Published by Elsevier Ltd.
引用
收藏
页码:3669 / 3680
页数:12
相关论文
共 50 条
  • [1] Flow patterns in the square cross-section riser of a circulating fluidised bed and the effect of riser exit design
    van der Meer, EH
    Thorpe, RB
    Davidson, JF
    [J]. CHEMICAL ENGINEERING SCIENCE, 2000, 55 (19) : 4079 - 4099
  • [2] The residence time distribution and mixing of the gas phase in the riser of a circulating fluidized bed
    Mahmoudi, S.
    Seville, J. P. K.
    Baeyens, J.
    [J]. POWDER TECHNOLOGY, 2010, 203 (02) : 322 - 330
  • [3] Slip velocity characteristics in the riser of circulating fluidised bed
    Subramanian, N.B.
    Kannan, C.S.
    [J]. Chemical Engineering and Technology, 1997, 20 (07): : 491 - 494
  • [4] Slip velocity characteristics in the riser of circulating fluidised bed
    Subramanian, NB
    Kannan, CS
    [J]. CHEMICAL ENGINEERING & TECHNOLOGY, 1997, 20 (07) : 491 - 494
  • [5] Particle velocities and their residence time distribution in the riser of a CFB
    Chan, Chian W.
    Seville, Jonathan P. K.
    Parker, David J.
    Baeyens, Jan
    [J]. POWDER TECHNOLOGY, 2010, 203 (02) : 187 - 197
  • [6] Stochastic modelling of the particle residence time distribution in circulating fluidised bed risers
    Harris, AT
    Thorpe, RB
    Davidson, JF
    [J]. CHEMICAL ENGINEERING SCIENCE, 2002, 57 (22-23) : 4779 - 4796
  • [7] THE PARTICLE VELOCITY DISTRIBUTION IN A RISER OF DILUTE CIRCULATING FLUIDIZED BED
    杨勇林
    金涌
    俞芷青
    汪展文
    白丁荣
    [J]. Chinese Journal of Chemical Engineering, 1991, (02) : 182 - 191
  • [8] Effect of riser exit geometry on bed hydrodynamics and heat transfer in a circulating fluidized bed riser column
    Reddy, BV
    Nag, PK
    [J]. INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2001, 25 (01) : 1 - 8
  • [9] Analysis of flexible ribbon particle residence time distribution in a fluidised bed riser using three-dimensional CFD-DEM simulation
    Wu, Kai
    Zhang, Erqiang
    Yuan, Zhulin
    Li, Bin
    Zhu, Wenkui
    Xu, Ji
    Wang, Le
    Luo, Dengshan
    [J]. POWDER TECHNOLOGY, 2020, 369 : 184 - 201
  • [10] Experimental Analysis of the Solids Acceleration Region in a Circulating Fluidised Bed Riser
    Chen, Yong
    Zhou, Faqi
    Wei, Yaodong
    [J]. INDIAN CHEMICAL ENGINEER, 2015, 57 (02) : 136 - 146