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 48 条
[31]   Two-phase convective heat transfer in miniature pipes under normal and microgravity conditions [J].
Narayanan, Chidambaram ;
Lakehal, Djamel .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 2008, 130 (07)
[32]   Modeling of Velocity Distribution Among Microchannels with Triangle Manifolds [J].
Pan, Minqiang ;
Tang, Yong ;
Yu, Hao ;
Chen, Hongqing .
AICHE JOURNAL, 2009, 55 (08) :1969-1982
[33]   AXIAL-DISPERSION IN A SEGMENTED GAS-LIQUID FLOW [J].
PEDERSEN, H ;
HORVATH, C .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1981, 20 (03) :181-186
[34]   Accessing Novel Process Windows in a High-Temperature/Pressure Capillary Flow Reactor [J].
Razzaq, Tahseen ;
Glasnov, Toma N. ;
Kappe, C. Oliver .
CHEMICAL ENGINEERING & TECHNOLOGY, 2009, 32 (11) :1702-1716
[35]   Design of a thick-walled screen for flow equalization in microstructured reactors [J].
Rebrov, Evgeny V. ;
Ekatpure, Rahul P. ;
de Croon, Mart H. J. M. ;
Schouten, Jaap C. .
JOURNAL OF MICROMECHANICS AND MICROENGINEERING, 2007, 17 (03) :633-641
[36]   Header design for flow equalization in microstructured reactors [J].
Rebrov, Evgeny V. ;
Ismagilov, Ryas Z. ;
Ekatpure, Rahul P. ;
de Croon, Mart H. J. M. ;
Schouten, Jaap C. .
AICHE JOURNAL, 2007, 53 (01) :28-38
[37]   Single-phase fluid flow distribution and heat transfer in microstructured reactors [J].
Rebrov, Evgeny V. ;
Schouten, Jaap C. ;
de Croon, Mart H. J. M. .
CHEMICAL ENGINEERING SCIENCE, 2011, 66 (07) :1374-1393
[38]   Sample pulse broadening in Taylor flow microchannels for screening applications [J].
Salman, W ;
Angeli, P ;
Gavriilidis, A .
CHEMICAL ENGINEERING & TECHNOLOGY, 2005, 28 (04) :509-514
[39]   Novel liquid-flow splitting unit numbering-up of liquid/liquid specifically made for chemical microprocessing [J].
Schenk, R ;
Hessel, V ;
Hofmann, C ;
Löwe, H ;
Schönfeld, F .
CHEMICAL ENGINEERING & TECHNOLOGY, 2003, 26 (12) :1271-1280
[40]   Flow regimes for adiabatic gas-liquid flow in microchannels [J].
Shao, N. ;
Gavriilidis, A. ;
Angeli, P. .
CHEMICAL ENGINEERING SCIENCE, 2009, 64 (11) :2749-2761