Numerical Investigations of Two-phase Flows through Enhanced Microchannels

被引:18
作者
Chandra, A. K. [1 ]
Kishor, K. [1 ]
Mishra, P. K. [2 ]
Alama, M. S. [1 ]
机构
[1] Motilal Nehru Natl Inst Technol, Dept Chem Engn, Allahabad, Uttar Pradesh, India
[2] Motilal Nehru Natl Inst Technol, Dept Mech Engn, Allahabad, Uttar Pradesh, India
关键词
microchannel; liquid-liquid flows; pressure drop; slug flow; enhanced microchannel; SLUG FLOW; DROPLET FORMATION; MASS-TRANSFER; CAPILLARY MICROREACTOR; MICROFLUIDIC DEVICE; T-JUNCTION; LIQUID; PATTERNS; HYDRODYNAMICS; SIMULATION;
D O I
10.15255/CABEQ.2015.2289
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Microfluidic devices are quite important for process industries, as these devices can intensify heat and mass transfer in two-phase reaction systems. Two-phase reaction systems, such as gas-liquid and liquid-liquid reactions with certain limitations have already been carried out in microfluidic systems by a few authors. However, these concepts are still under development and a detailed understanding of the hydrodynamics involve is required. Hydrodynamics studies are inherently crucial to provide precise reaction conditions and identify asymptotic performance limits. In the present work, Computational Fluid Dynamics (CFD) simulation was carried out to investigate the hydrodynamics involved in the T-junction enhanced microchannel. The slug formation, slug size, slug shape, and pressure drop in the enhanced microchannel were predicted using the volume of fluid (VOF) for water-cyclohexane system. The effects of obstruction spacing on pressure drop, slug lengths, and mixing within the slug were also examined. This study revealed that mixing enhances tremendously within the slug and at the interface in the enhanced microchannel, but with slightly greater pressure drop. However, an increase in obstruction spacing affects the slug formation, unit slug length, and pressure drop.
引用
收藏
页码:149 / 159
页数:11
相关论文
共 26 条
[1]   Liquid-liquid two-phase flow patterns and mass transfer characteristics in rectangular glass microreactors [J].
Dessimoz, Anne-Laure ;
Cavin, Laurent ;
Renken, Albert ;
Kiwi-Minsker, Lioubov .
CHEMICAL ENGINEERING SCIENCE, 2008, 63 (16) :4035-4044
[2]  
Donata M. F., 2008, INT J MULTIPHASE FLO, V34, P1108
[3]  
Ehrfeld W., 2000, STATE ART MICROREACT, P1
[4]   Formation of droplets and bubbles in a microfluidic T-junction - scaling and mechanism of break-up [J].
Garstecki, P ;
Fuerstman, MJ ;
Stone, HA ;
Whitesides, GM .
LAB ON A CHIP, 2006, 6 (03) :437-446
[5]   Chemistry in microstructured reactors [J].
Jähnisch, K ;
Hessel, V ;
Löwe, H ;
Baerns, M .
ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2004, 43 (04) :406-446
[6]   CFD modelling of mass transfer with and without chemical reaction in the liquid-liquid slug flow microreactor [J].
Kashid, M. N. ;
Agar, D. W. ;
Turek, S. .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (18-20) :5102-5109
[7]   Computational modelling of slug flow in a capillary microreactor [J].
Kashid, M. N. ;
Platte, F. ;
Agar, D. W. ;
Turek, S. .
JOURNAL OF COMPUTATIONAL AND APPLIED MATHEMATICS, 2007, 203 (02) :487-497
[8]   CFD modelling of liquid-liquid multiphase microstructured reactor: Slug flow generation [J].
Kashid, M. N. ;
Renken, A. ;
Kiwi-Minsker, L. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2010, 88 (3A) :362-368
[9]  
Kashid M. N., 2007, BIOCH CHEM ENG, P1
[10]   Hydrodynamics of liquid-liquid slug flow capillary microreactor: Flow regimes, slug size and pressure drop [J].
Kashid, Madhvanand N. ;
Agar, David W. .
CHEMICAL ENGINEERING JOURNAL, 2007, 131 (1-3) :1-13