Impact of gas-solid direct contact on gas-liquid-solid reaction performance in a flow reactor

被引:4
|
作者
Asano, Shusaku [1 ,2 ]
Miyamura, Hiroyuki [3 ]
Matsushita, Mizuki [2 ]
Kudo, Shinji [1 ]
Kobayashi, Shu [4 ]
Hayashi, Jun-ichiro [1 ,2 ]
机构
[1] Kyushu Univ, Inst Mat Chem & Engn, Kasuga, Fukuoka 8168580, Japan
[2] Kyushu Univ, Interdisciplinary Grad Sch Engn Sci, Kasuga, Fukuoka 8168580, Japan
[3] Natl Inst Adv Ind Sci & Technol, Interdisciplinary Res Ctr Catalyt Chem, Tsukuba, Ibaraki 3058565, Japan
[4] Univ Tokyo, Sch Sci, Dept Chem, Hongo,Bunkyo Ku, Tokyo 1130033, Japan
基金
日本学术振兴会;
关键词
Flow reactor; Hydrogenation; Powder catalyst; Mass transfer; Liquid holdup; PACKED-BED; HYDROGENATION; REGIMES; UPFLOW;
D O I
10.1007/s41981-023-00295-9
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Although gas-liquid-solid reactions, such as catalytic hydrogenation, have a long history, a fundamental understanding of the flow behavior and its effect on the reaction is lacking for flow chemistry applications using powder catalysts. This study revealed the distinctive effect of gas-solid direct contact on the surface of a powder catalyst. Direct gas-solid contact accelerates the reaction beyond the theoretical maximum of the batch reaction system, where gaseous species are supplied to the catalyst surface after dissolution into the liquid. The benefit of direct contact is further pronounced in systems with low-solubility gaseous species. Liquid holdup analysis revealed that the micro-concavities of the catalyst support is crucial for sustaining the liquid using capillary forces and supplying the liquid substrate to the catalyst surface even under high gas flow rate conditions. The gas-to-liquid flow rate ratio (G/L) is a decisive factor for direct gas-solid contact, whereas the flow direction, whether upflow or downflow, has no impact on powder catalysts with a size of a few hundred microns. [GRAPHICS] .
引用
收藏
页码:329 / 335
页数:7
相关论文
共 50 条
  • [1] Impact of gas-solid direct contact on gas-liquid-solid reaction performance in a flow reactor
    Shusaku Asano
    Hiroyuki Miyamura
    Mizuki Matsushita
    Shinji Kudo
    Shū Kobayashi
    Jun-ichiro Hayashi
    Journal of Flow Chemistry, 2024, 14 : 329 - 335
  • [2] Discrete Element Simulation of Gas-Solid and Gas-Liquid-Solid Flows
    Yu, Jiahui
    Wang, Shuai
    Luo, Kun
    Fan, Jianren
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2023, 62 (42) : 17019 - 17028
  • [3] Electrical capacitance tomography imaging of gas-solid and gas-liquid-solid fluidized bed systems
    Fan, LS
    Warsito, W
    Du, B
    JOURNAL OF VISUALIZATION, 2004, 7 (01) : 5 - 5
  • [4] GAS HOLDUP IN GAS-LIQUID AND GAS-LIQUID-SOLID FLOW REACTORS
    YING, DH
    GIVENS, EN
    WEIMER, RF
    INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1980, 19 (04): : 635 - 638
  • [5] Electrical capacitance tomography imaging of gas-solid and gas-liquid-solid fluidized bed systems
    L. -S. Fan
    W. Warsito
    B. Du.
    Journal of Visualization, 2004, 7 : 5 - 5
  • [6] REACTIONS IN INTERPHASE TRANSFER CATALYSIS .2. GAS-SOLID AND GAS-LIQUID-SOLID SYSTEMS
    SIMANDAN, T
    VLADEA, R
    REVISTA DE CHIMIE, 1990, 41 (11-12): : 877 - 880
  • [7] Special issue on gas-liquid and gas-liquid-solid reactor engineering
    Crine, M
    Vasel, JL
    Wild, G
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2004, 43 (11) : 1337 - 1337
  • [8] Special issue on gas-liquid and gas-liquid-solid reactor engineering
    Wild, G
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2001, 40 (02) : 85 - 85
  • [9] Global modelling of a gas-liquid-solid airlift reactor
    Talvy, S
    Cockx, A
    Line, A
    CHEMICAL ENGINEERING SCIENCE, 2005, 60 (22) : 5991 - 6003
  • [10] Thermal-hydraulics performance evaluation of bubble swarms sweeping tube bundles in a direct contact gas-liquid-solid reactor
    Han, Changliang
    Huang, Yiyan
    Guo, Weiping
    Wu, Yizhong
    Chen, Zhipeng
    Li, Xibing
    APPLIED THERMAL ENGINEERING, 2024, 250