An adiabatic experiment was conducted to investigate the effect of channel geometry on gas-liquid two-phase flow characteristics in microchannels. A mixture of water and nitrogen gas was pumped through a 96 μm × 96 μm square microchannel and the flow pattern, void fraction and pressure drop data were obtained and compared with those previously obtained in a 100 μm circular microchannel. The frictional pressure drop was determined from the measured total pressure drop, and the two-phase flow pattern and void fraction were determined from image analysis of the video recordings. In the square channel, 136 runs were performed over a range of 0.09 ≤ jG,AVG ≤ 62 m/s for the average superficial gas velocity and 0.01 ≤ jL ≤ 4 m/s for the superficial liquid velocity. The frictional pressure drop data showed that the calculations based on a separated–flow model were best at estimating the frictional pressure drop for both microchannels. No particular effect of the channel shape was found for the two-phase frictional pressure drop. The void fraction-to-volumetric quality relationship was also found to be similar for both shapes of microchannels, exhibiting an exponential increase in void fraction with increasing volumetric quality. The empirical correlation that describes the void fraction-to-volumetric quality relationship for the square microchannel was developed earlier from the measured data for the circular microchannel. Observations of the recorded images indicated the two-phase flow patterns to be primarily intermittent with liquid and gas slugs. The liquid film surrounding the gas core displayed a smooth or ring-like structure. The probability of each interfacial structure occurring was examined in detail to develop a novel flow pattern map consisting of four regions named slug-ring flow, ring-slug flow, multiple flow and semiannular flow. Between the square and circular microchannels, the two-phase flow maps exhibited transition boundaries that were shifted depending on the channel shape. The region of ring-slug flow that appears in the circular microchannel collapsed in the square microchannel, possibly due to the suppression of the liquid-ring film in the corners of the square channel.
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ASME/JSME 2003 4th Joint Fluids Summer Engineering Conference
July 6–10, 2003
Honolulu, Hawaii, USA
Conference Sponsors:
- Fluids Engineering Division
ISBN:
0-7918-3696-7
PROCEEDINGS PAPER
Two-Phase Flow Through Square and Circular Microchannels: Effect of Channel Geometry
Peter M.-Y. Chung,
Peter M.-Y. Chung
University of Toronto, Toronto, Ontario, Canada
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Masahiro Kawaji,
Masahiro Kawaji
University of Toronto, Toronto, Ontario, Canada
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Akimaro Kawahara,
Akimaro Kawahara
Kumamoto University, Kumamoto, Japan
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Yuichi Shibata
Yuichi Shibata
Ibaraki National College of Technology, Hitachinaka-shi, Ibaraki-ken, Japan
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Peter M.-Y. Chung
University of Toronto, Toronto, Ontario, Canada
Masahiro Kawaji
University of Toronto, Toronto, Ontario, Canada
Akimaro Kawahara
Kumamoto University, Kumamoto, Japan
Yuichi Shibata
Ibaraki National College of Technology, Hitachinaka-shi, Ibaraki-ken, Japan
Paper No:
FEDSM2003-45377, pp. 1459-1467; 9 pages
Published Online:
February 4, 2009
Citation
Chung, PM, Kawaji, M, Kawahara, A, & Shibata, Y. "Two-Phase Flow Through Square and Circular Microchannels: Effect of Channel Geometry." Proceedings of the ASME/JSME 2003 4th Joint Fluids Summer Engineering Conference. Volume 1: Fora, Parts A, B, C, and D. Honolulu, Hawaii, USA. July 6–10, 2003. pp. 1459-1467. ASME. https://doi.org/10.1115/FEDSM2003-45377
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