CORRELATION BETWEEN HYSTERESIS OF GAS-LIQUID MASS TRANSFER AND LIQUID DISTRIBUTION IN A TRICKLE BED

被引:0
|
作者
王蓉
栾美琅
毛在砂
陈家镛
机构
[1] China
[2] Academia Sinica
[3] Institute of Chemical Metallurgy
[4] Academia Sinica Beijing 100080
基金
中国国家自然科学基金;
关键词
trickle-bed reactor; radial liquid distribution; gas-liquid mass transfer; hysteresis;
D O I
暂无
中图分类号
TQ021 [基础理论];
学科分类号
081701 ; 081704 ;
摘要
The hysteresis of gas-liquid mass transfer rate and the corresponding radial liquiddistribution in a trickle bed reactor are measured to provide evidence for the correlation between thesetwo behaviors.Experimental results indicate that the hysteresis of gas-liquid mass transfer originatesfrom the nonuniformity of the hydrodynamic state of gas-liquid flow and the radial maldistributionof local kcorresponds very well to the radial maldistribution of liquid flow in the bed.The localliquid flow rate is also found to be nonuniform in the azimuthal direction.In view of maldistributedliquid flow even in the pulsing flow regime,the conventional plug flow model seems oversimplifiedfor describing the behavior of a trickle bed.
引用
收藏
页码:43 / 47
页数:5
相关论文
共 50 条
  • [1] Correlation between hysteresis of gas-liquid mass transfer and liquid distribution in a trickle bed
    Wang, R
    Luan, ML
    Mao, ZS
    Chen, JY
    [J]. CHINESE JOURNAL OF CHEMICAL ENGINEERING, 1997, 5 (02) : 135 - 139
  • [2] HYSTERESIS OF GAS-LIQUID MASS TRANSFER IN A TRICKLE BED REACTOR
    王蓉
    毛在砂
    陈家镛
    [J]. Chinese Journal of Chemical Engineering, 1994, (04) : 53 - 57
  • [3] HYSTERESIS OF GAS-LIQUID MASS-TRANSFER IN A TRICKLE-BED REACTOR
    WANG, R
    MAO, ZS
    CHEN, JY
    [J]. CHINESE JOURNAL OF CHEMICAL ENGINEERING, 1994, 2 (04) : 236 - 240
  • [4] Connection Between Liquid Distribution and Gas-Liquid Mass Transfer in Monolithic Bed
    Xu Min
    Liu Hui
    Li Chengyue
    Zhou Yuan
    Ji Shengfu
    [J]. CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2011, 19 (05) : 738 - 746
  • [5] Gas-liquid mass transfer in trickle-bed reactors: Gas-side mass transfer
    Iliuta, I
    Iliuta, MC
    Thyrion, FC
    [J]. CHEMICAL ENGINEERING & TECHNOLOGY, 1997, 20 (09) : 589 - 595
  • [6] Gas-liquid interfacial mass transfer in trickle-bed reactors at elevated pressures
    Larachi, F
    Cassanello, M
    Laurent, A
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (03) : 718 - 733
  • [7] Residence time distribution in the liquid phase in a cocurrent gas-liquid trickle bed reactor
    Stegeman, D
    vanRooijen, FE
    Kamperman, AA
    Weijer, S
    Westerterp, KR
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (02) : 378 - 385
  • [8] GAS-LIQUID MASS-TRANSFER IN PACKED TRICKLE BEDS
    PATWARDHAN, VS
    [J]. CHEMICAL ENGINEERING SCIENCE, 1979, 34 (03) : 436 - 437
  • [9] Heat transfer characterization of gas-liquid flows in a trickle-bed
    Huang, X
    Varma, A
    McCready, MJ
    [J]. CHEMICAL ENGINEERING SCIENCE, 2004, 59 (18) : 3767 - 3776
  • [10] Gas-liquid mass transfer in high pressure trickle-bed reactors: Experiments and modelling
    Cassanello, M
    Larachi, F
    Laurent, A
    Wild, G
    Midoux, N
    [J]. HIGH PRESSURE CHEMICAL ENGINEERING, 1996, 12 : 493 - 498