Design criteria for a barrier-based gas-liquid flow distributor for parallel microchannels

被引:61
|
作者
Al-Rawashdeh, M. [1 ]
Fluitsma, L. J. M. [1 ]
Nijhuis, T. A. [1 ]
Rebrov, E. V. [2 ]
Hessel, V. [1 ]
Schouten, J. C. [1 ]
机构
[1] Eindhoven Univ Technol, Lab Chem Reactor Engn, Dept Chem Engn & Chem, NL-5600 MB Eindhoven, Netherlands
[2] Queens Univ Belfast, Sch Chem & Chem Engn, Belfast BT9 5AG, Antrim, North Ireland
关键词
Microreactor; Multiphase flow; Taylor flow; Numbering-up; Scale-up; Fabrication tolerance; MICROSTRUCTURED REACTORS; MASS-TRANSFER; TAYLOR FLOW; MULTICHANNEL MICROREACTORS; PROCESS WINDOWS; SEGMENTED FLOW; HEAT-TRANSFER; NUMBERING-UP; 2-PHASE FLOW; SCALE-OUT;
D O I
10.1016/j.cej.2011.11.086
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This paper presents criteria for the design of a flow distributor for even distribution of gas and liquid flows over parallel microchannels. The design criteria are illustrated for the case of a nitrogen-water Taylor flow (1 <Re-GL <30 and 3 x 10(-5) < Ca-GL < 4 x 10(-4)) in four parallel microchannels of 0.9 mm inner diameter. The distributor consists of a gas manifold, a liquid manifold, four barrier channels for the gas and four for the liquid, and four T-mixers for mixing of the gas and liquid flows. The four barrier channels have equal inner diameters and length: four different diameters have been studied: 0.05, 0.1, 0.15 and 0.2 mm. Uniform distribution of the gas and liquid flows over the microchannels is achieved when the pressure drop over the barrier channels is in the range of around 4-25 times the pressure drop over the corresponding T-mixers and microchannels. Gas-liquid channeling is prevented at equal pressures in the gas and liquid manifolds. An optimal operational window is realized when the gas to liquid flow ratio kept constant and the ratio of the maximum over the minimum flow rates remain less than 20. The effect of variations in the inner diameters (result of the fabrication process) of the barrier channels and the microchannels on the flow distribution is demonstrated. It is suggested that these design criteria can also be applied at larger numbers of parallel microchannels. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:549 / 556
页数:8
相关论文
共 50 条
  • [1] Design methodology for barrier-based two phase flow distributor
    Al-Rawashdeh, Ma'moun
    Nijhuis, Xander
    Rebrov, Evgeny V.
    Hessel, Volker
    Schouten, Jaap C.
    AICHE JOURNAL, 2012, 58 (11) : 3482 - 3493
  • [2] Gas-liquid flow distribution of parallel microchannels
    Bai, Lu
    Zhu, Chunying
    Fu, Taotao
    Ma, Youguang
    Huagong Xuebao/CIESC Journal, 2014, 65 (01): : 108 - 115
  • [3] Adiabatic gas-liquid flow in microchannels
    Kawaji, M
    Chung, PMY
    MICROSCALE THERMOPHYSICAL ENGINEERING, 2004, 8 (03): : 239 - 257
  • [4] Flow regimes for adiabatic gas-liquid flow in microchannels
    Shao, N.
    Gavriilidis, A.
    Angeli, P.
    CHEMICAL ENGINEERING SCIENCE, 2009, 64 (11) : 2749 - 2761
  • [5] Gas-liquid flow characteristics in serpentine microchannels
    College of Energy and Power Engineering, Northeast Dianli University, Jilin
    Jilin
    132012, China
    Huagong Xuebao, 11 (4350-4358):
  • [6] Mass transfer in gas-liquid flow in microchannels
    Yue, Jun
    Chen, Guangwen
    Yuan, Quan
    Luo, Ling'ai
    le Gall, Hervé
    Huagong Xuebao/Journal of Chemical Industry and Engineering (China), 2006, 57 (06): : 1296 - 1303
  • [7] Distribution of gas-liquid two-phase flow in parallel microchannels with the splitting of the liquid feed
    Duan, Cong
    Liu, Ziwei
    Zhu, Chunying
    Ma, Youguang
    Fu, Taotao
    CHEMICAL ENGINEERING JOURNAL, 2020, 398
  • [8] Effect of distributor on gas-liquid downward flow in capillaries
    Mogalicherla, Aswani K.
    De, Mahuya
    Kunzru, Deepak
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (25) : 8406 - 8412
  • [9] Characteristics of liquid slugs in gas-liquid Taylor flow in microchannels
    Zaloha, Petr
    Kristal, Jiri
    Jiricny, Vladimir
    Voelkel, Norbert
    Xuereb, Catherine
    Aubin, Joelle
    CHEMICAL ENGINEERING SCIENCE, 2012, 68 (01) : 640 - 649
  • [10] Bubble lengths in the gas-liquid Taylor flow in microchannels
    Sobieszuk, Pawel
    Cyganski, Pawel
    Pohorecki, Ryszard
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2010, 88 (3A): : 263 - 269