Minimum liquid fluidization velocity in gas-liquid-solid fluidized beds

被引:33
|
作者
Briens, LA
Briens, CL
Margaritis, A
Hay, J
机构
[1] Dept. of Chem. and Biochem. Eng., University of Western Ontario, London
关键词
D O I
10.1002/aic.690430507
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Accurate defection of minimum liquid fluidization is essential to the successful operation of gas-liquid-solid fluidized beds, especially when particle or liquid properties evolve. A gas-liquid-solid system of 3-mm glass beads exhibits three distinct flow regimes as the liquid velocity is increased: compacted agitated and fluidized-bed regimes. Measurements showed that the bed is not fluidized in the agitated bed regime. Pressure gradient and bed height measurements do not provide the minimum liquid fluidization velocity; instead they offer the velocity between the compacted and agitated bed regimes. Time-averaged signals are not reliable for determining the minimum liquid fluidization velocity. it can be obtained from the standard deviation, the average frequency, the Hurst exponent and the V statistic of the cross-sectional average conductivity, which can be measured under many industrial conditions.
引用
收藏
页码:1180 / 1189
页数:10
相关论文
共 50 条
  • [1] Minimum liquid fluidization velocity in gas-liquid-solid fluidized beds
    Dept of Chem + Biochemical Eng, The University of Western Ontario, London Ont N6A 5B9, Canada
    AIChE J, 5 (1180-1189):
  • [2] Minimum liquid fluidization velocity in gas-liquid-solid fluidized beds of low density particles
    Briens, LA
    Briens, CL
    Margaritis, A
    Hay, J
    CHEMICAL ENGINEERING SCIENCE, 1997, 52 (21-22) : 4231 - 4238
  • [3] Minimum Fluidization Velocity in Gas-Liquid-Solid Minifluidized Beds
    Li, Yanjun
    Liu, Mingyan
    Li, Xiangnan
    AICHE JOURNAL, 2016, 62 (06) : 1940 - 1957
  • [4] Minimum liquid fluidization velocity of gas-liquid fluidized beds
    Zhang, J.-P.
    Epstein, N.
    Grace, J.R.
    Zhu, J.
    Chemical Engineering Research and Design, 1995, 73 (A3) : 347 - 353
  • [5] Minimum fluidization velocity and gas holdup in gas-liquid-solid fluidized bed reactors
    Ramesh, K
    Murugesan, T
    JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2002, 77 (02) : 129 - 136
  • [6] MINIMUM LIQUID FLUIDIZATION VELOCITY OF GAS-LIQUID FLUIDIZED-BEDS
    ZHANG, JP
    EPSTEIN, N
    GRACE, JR
    ZHU, J
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 1995, 73 (A3): : 347 - 353
  • [7] Models for minimum liquid fluidization velocity of gas-liquid fluidized beds
    Lee, D
    Epstein, N
    Grace, JR
    JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2001, 34 (02) : 95 - 101
  • [8] Liquid axial dispersion in gas-liquid-solid fluidized beds
    Saberian-Broudjenni, Mohamad, 1600, (40):
  • [9] Liquid dispersion in gas-liquid-solid circulating fluidized beds
    Han, SJ
    Zhou, J
    Jin, Y
    Loh, KC
    Wang, ZW
    CHEMICAL ENGINEERING JOURNAL, 1998, 70 (01) : 9 - 14
  • [10] The variable-voidage effect on modeling the minimum liquid fluidization velocity of gas-liquid fluidized beds
    Lee, D
    Epstein, N
    Grace, JR
    JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2003, 36 (09) : 1111 - 1115