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

被引:35
|
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
  • [31] Scale effects in gas-liquid-solid fluidization
    Nacef, S.
    Wild, G.
    Laurent, A.
    Kim, S.D.
    International chemical engineering, 1992, 32 (01): : 51 - 72
  • [32] PARTICLE-PARTICLE COLLISIONS IN LIQUID-SOLID AND GAS-LIQUID-SOLID FLUIDIZED-BEDS
    DELPOZO, M
    BRIENS, CL
    WILD, G
    CHEMICAL ENGINEERING SCIENCE, 1993, 48 (18) : 3313 - 3319
  • [33] Multiscale Model of Gas-Liquid Interface Mass Transfer in Gas-Liquid-Solid Fluidized Beds
    Lan, Dizhou
    Ma, Yongli
    Areej, Javed
    Liu, Mingyan
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2024, 63 (28) : 12704 - 12714
  • [34] Transition velocities and phase holdups at minimum fluidization in gas-liquid-solid systems
    Lee, D
    Macchi, A
    Epstein, N
    Grace, JR
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2001, 79 (04): : 579 - 583
  • [35] Minimum liquid velocity for particle transport from gas-liquid fluidized beds
    Zhang, JP
    Epstein, N
    Grace, JR
    FLUIDIZATION IX, 1998, : 645 - 652
  • [36] Minimum fluidization velocities for gas-liquid-solid three-phase systems
    Zhang, JP
    Epstein, N
    Grace, JR
    POWDER TECHNOLOGY, 1998, 100 (2-3) : 113 - 118
  • [37] Measurement and modeling of particle-liquid heat transfer in liquid-solid and gas-liquid-solid fluidized beds
    Briens, CL
    Del Pozo, M
    Trudell, C
    Wild, G
    CHEMICAL ENGINEERING SCIENCE, 1999, 54 (06) : 731 - 739
  • [38] Description of the temperature, humidity, and concentration distribution in gas-liquid-solid fluidized beds
    Heinrich, Stefan
    Mörl, Lothar
    Chemical Engineering and Technology, 1999, 22 (02): : 118 - 122
  • [39] Single bubble behavior in gas-liquid-solid mini-fluidized beds
    Li, Yanjun
    Liu, Mingyan
    Li, Xiangnan
    CHEMICAL ENGINEERING JOURNAL, 2016, 286 : 497 - 507
  • [40] Description of the temperature, humidity, and concentration distribution in gas-liquid-solid fluidized beds
    Heinrich, S
    Mörl, L
    CHEMICAL ENGINEERING & TECHNOLOGY, 1999, 22 (02) : 118 - 122