Flow regimes in a gas-liquid-solid three-phase moving bed

被引:4
|
作者
Wang, Chao [1 ]
Yang, Yao [1 ]
Huang, Zhengliang [1 ]
Sun, Jingyuan [1 ]
Liao, Zuwei [1 ]
Wang, Jingdai [1 ]
Yang, Yongrong [1 ]
Du, Bing [2 ]
机构
[1] Zhejiang Univ, Coll Chem & Biol Engn, Hangzhou 310027, Peoples R China
[2] ExxonMobil Res & Engn Co, Annandale, NJ USA
基金
中国国家自然科学基金;
关键词
flow behavior; flow regime transition; moving particles; particle velocity; three-phase moving bed; PULSING FLOW; COCURRENT DOWNFLOW; PRESSURE-DROP; VOID FRACTION; MASS-TRANSFER; PACKED-BED; TRICKLE; TRANSITION; REACTORS; HYDRODYNAMICS;
D O I
10.1002/aic.17374
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The gas-liquid-solid three-phase moving beds could supply a potential solution for multiphase reactions with catalyst easily deactivated, and the flow regimes in it were studied by optical method and pressure drop measurement. Results showed that taking the trickle flow as the initial flow regime, the flow channels were more obvious as the particle velocity increased. When the initial flow regimes were pulse flow and bubble flow respectively, the pulse-to-trickle and bubble-to-pulse flow transitions mainly occurred at moderate-to-high particle velocities (0.01-0.04 m s(-1) under conditions used in this work). Moreover, the flow regime map in the three-phase moving bed was constructed and shown that the region of trickle flow increased and the region of bubble flow decreased. Finally, the application of three-phase moving beds was discussed, and it could be suitable for those reactions, which had to operate in the pulse flow, bubble flow, and transition zone.
引用
收藏
页数:15
相关论文
共 50 条
  • [31] Characteristics of Three-Phase (Gas-Liquid-Solid) Circulating Fluidized Beds
    Kang, Yong
    Kim, Min Kon
    Yang, Si Woo
    Kim, Sang Dong
    JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2018, 51 (09) : 740 - 761
  • [32] Minimum fluidization velocities for gas-liquid-solid three-phase systems
    Zhang, JP
    Epstein, N
    Grace, JR
    POWDER TECHNOLOGY, 1998, 100 (2-3) : 113 - 118
  • [33] Modelling of steady gas-liquid-solid three-phase flow with application to oil well drilling
    Kamp, AM
    Rivero, M
    Sharma, Y
    Yonezawa, T
    9TH INTERNATIONAL CONFERENCE ON MULTIPHASE '99: FRONTIER TECHNOLOGY COMES OF AGE, 1999, (35): : 201 - 216
  • [34] Treatment of the refinery wastewater in a gas-liquid-solid three-phase flow airlift loop bioreactor
    Wen, JP
    Qing, Y
    Lei, P
    Mao, GZ
    JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2005, 80 (07) : 767 - 771
  • [35] Solid-liquid mass transfer in a gas-liquid-solid three-phase reversed flow jet loop reactor
    Wen, JP
    Huang, L
    Zhu, Y
    Li, C
    Chen, YL
    CHEMICAL ENGINEERING JOURNAL, 2000, 78 (2-3) : 231 - 235
  • [37] Axial mixing and segregation in a gas-liquid-solid three-phase fluidized bed of solid particles of different sizes and densities
    Matsumoto, T
    Hidaka, N
    Takebayasi, Y
    Morooka, S
    CHEMICAL ENGINEERING SCIENCE, 1997, 52 (21-22) : 3961 - 3970
  • [38] Radial Distributions of Phase Holdups and Phase Propagation Velocities in a Three-Phase Gas-Liquid-Solid Fluidized Bed (GLSCFB) Riser
    Razzak, S. A.
    Zhu, J-X.
    Barghi, S.
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (01) : 281 - 289
  • [39] FLOW REGIMES AND LIQUID-MIXING IN A DRAFT TUBE GAS-LIQUID-SOLID FLUIDIZED-BED
    VUNJAKNOVAKOVIC, G
    JOVANOVIC, G
    KUNDAKOVIC, L
    OBRADOVIC, B
    CHEMICAL ENGINEERING SCIENCE, 1992, 47 (13-14) : 3451 - 3458
  • [40] New CO2 Capture Process with Gas-Liquid-Solid Three-Phase Circulating Fluidized Bed
    Hu, Kangtao
    Liu, Jinghao
    Yang, Hairui
    Zhang, Hai
    Liu, Qing
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (45) : 15905 - 15911