Vertical squeezing route taylor flow with angled microchannel junctions
Heretofore, the microchannel junction angle θ dependent behavior on Taylor flow with a vertical squeezing route lacks a comprehensive understanding. An experimental study was performed on the vertical squeezing route Taylor flow for θ = 20, 45, 90, 135, and 160° at different flow rates of helium (He...
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sg-ntu-dr.10356-1604922022-07-25T07:02:59Z Vertical squeezing route taylor flow with angled microchannel junctions Lim, An Eng Lam, Yee Cheong School of Mechanical and Aerospace Engineering Engineering::Mechanical engineering Gas Flowrate Junction Angles Heretofore, the microchannel junction angle θ dependent behavior on Taylor flow with a vertical squeezing route lacks a comprehensive understanding. An experimental study was performed on the vertical squeezing route Taylor flow for θ = 20, 45, 90, 135, and 160° at different flow rates of helium (He) and ethanol. By employing extreme θ of 20 and 160°, an in-depth knowledge of the associated mechanics is gained. Through the formulated theoretical model, the sizes of the bubble and slug were predicted quantitatively for various fluid flow rates and θ, with good qualitative and quantitative agreement with experimental results. With increasing liquid or decreasing gas flow rate, all the employed junction angle channels had insensitive unit cell volumeVUvariation with flow rate changes because of the near cancellation of the effect of increased liquid slug volumeVSwith the effect of decreased gas bubble volumeVB. Using the 90° channel as the reference, the 20, 45, 135, and 160° channels generated largerVBandVSresulting in a largerVU. This is attributed to the wider junction widthWJwhen θ deviated from 90°. With the widerWJ, it produces a longer gas neck length that leads to a larger bubble lengthLBduring the blocking process. The longer time due to the slower squeezing rate from the widerWJresults inLBgrowth during the squeezing process. AsWJvalues of 20 and 160° channels are similar (similarWJfor 45 and 135° channels), parabolic (U-shaped) trends forVB,VS, andVUagainst θ were observed for the various fluid flow rates. The understanding gained may be exploited for precise bubble and slug generation control for targeted applications. Nanyang Technological University The authors gratefully acknowledge Nanyang Technological University (NTU) for its financial support (grant no. 001274- 00001). 2022-07-25T07:02:59Z 2022-07-25T07:02:59Z 2021 Journal Article Lim, A. E. & Lam, Y. C. (2021). Vertical squeezing route taylor flow with angled microchannel junctions. Industrial and Engineering Chemistry Research, 60(39), 14307-14317. https://dx.doi.org/10.1021/acs.iecr.1c02324 0888-5885 https://hdl.handle.net/10356/160492 10.1021/acs.iecr.1c02324 2-s2.0-85116515775 39 60 14307 14317 en 001274-00001 Industrial and Engineering Chemistry Research © 2021 American Chemical Society. All rights reserved. |
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Engineering::Mechanical engineering Gas Flowrate Junction Angles Lim, An Eng Lam, Yee Cheong Vertical squeezing route taylor flow with angled microchannel junctions |
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Heretofore, the microchannel junction angle θ dependent behavior on Taylor flow with a vertical squeezing route lacks a comprehensive understanding. An experimental study was performed on the vertical squeezing route Taylor flow for θ = 20, 45, 90, 135, and 160° at different flow rates of helium (He) and ethanol. By employing extreme θ of 20 and 160°, an in-depth knowledge of the associated mechanics is gained. Through the formulated theoretical model, the sizes of the bubble and slug were predicted quantitatively for various fluid flow rates and θ, with good qualitative and quantitative agreement with experimental results. With increasing liquid or decreasing gas flow rate, all the employed junction angle channels had insensitive unit cell volumeVUvariation with flow rate changes because of the near cancellation of the effect of increased liquid slug volumeVSwith the effect of decreased gas bubble volumeVB. Using the 90° channel as the reference, the 20, 45, 135, and 160° channels generated largerVBandVSresulting in a largerVU. This is attributed to the wider junction widthWJwhen θ deviated from 90°. With the widerWJ, it produces a longer gas neck length that leads to a larger bubble lengthLBduring the blocking process. The longer time due to the slower squeezing rate from the widerWJresults inLBgrowth during the squeezing process. AsWJvalues of 20 and 160° channels are similar (similarWJfor 45 and 135° channels), parabolic (U-shaped) trends forVB,VS, andVUagainst θ were observed for the various fluid flow rates. The understanding gained may be exploited for precise bubble and slug generation control for targeted applications. |
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School of Mechanical and Aerospace Engineering |
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School of Mechanical and Aerospace Engineering Lim, An Eng Lam, Yee Cheong |
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Article |
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Lim, An Eng Lam, Yee Cheong |
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Lim, An Eng |
title |
Vertical squeezing route taylor flow with angled microchannel junctions |
title_short |
Vertical squeezing route taylor flow with angled microchannel junctions |
title_full |
Vertical squeezing route taylor flow with angled microchannel junctions |
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Vertical squeezing route taylor flow with angled microchannel junctions |
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Vertical squeezing route taylor flow with angled microchannel junctions |
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vertical squeezing route taylor flow with angled microchannel junctions |
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2022 |
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https://hdl.handle.net/10356/160492 |
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