Two-phase flow behavior inside a header connected to multiple parallel channels
The main objective of this work is to examine the flow distribution of two-phase mixture to parallel channels and to investigate the flow behavior at header-channel junctions simulating the corresponding parts of compact heat exchangers. The cross-section of the header and the channels were fixed to...
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Published in | Experimental thermal and fluid science Vol. 33; no. 2; pp. 195 - 202 |
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Main Author | |
Format | Journal Article |
Language | English |
Published |
Amsterdam
Elsevier Inc
01.01.2009
Elsevier |
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Abstract | The main objective of this work is to examine the flow distribution of two-phase mixture to parallel channels and to investigate the flow behavior at header-channel junctions simulating the corresponding parts of compact heat exchangers. The cross-section of the header and the channels were fixed to 14
mm
×
14
mm and 12
mm
×
1.6
mm, respectively. The mass flux and the mass quality ranges were 70–165
kg/m
2
s and 0.3–0.7, respectively. Air and water were used as the test fluids. The flow distribution at the fore part of the header (region A) is affected only by the upstream flow configuration and the rate of liquid flow separation decreased a flowing downwards. On the other hand, in the rear part, the downstream effect predominates over the upstream effect due to strong flow recirculation near the end plate. In this part, the liquid separation increased (region B) and then decreased (region C) as the mixture proceeds downwards. The validity of the existing models for branching flows at parallel T-junction was tested, and turned out to be appropriate for region A. However, the models were not applicable to the rear part due to a strong flow recirculation. Moreover, the effect of the membranes in channels was investigated, but that was minor. |
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AbstractList | The main objective of this work is to examine the flow distribution of two-phase mixture to parallel channels and to investigate the flow behavior at header-channel junctions simulating the corresponding parts of compact heat exchangers. The cross-section of the header and the channels were fixed to 14 mm X 14 mm and 12 mm X 1.6 mm, respectively. The mass flux and the mass quality ranges were 70-165 kg/m2 s and 0.3-0.7, respectively. Air and water were used as the test fluids. The flow distribution at the fore part of the header (region A) is affected only by the upstream flow configuration and the rate of liquid flow separation decreased a flowing downwards. On the other hand, in the rear part, the downstream effect predominates over the upstream effect due to strong flow recirculation near the end plate. In this part, the liquid separation increased (region B) and then decreased (region C) as the mixture proceeds downwards. The validity of the existing models for branching flows at parallel T-junction was tested, and turned out to be appropriate for region A. However, the models were not applicable to the rear part due to a strong flow recirculation. Moreover, the effect of the membranes in channels was investigated, but that was minor. The main objective of this work is to examine the flow distribution of two-phase mixture to parallel channels and to investigate the flow behavior at header-channel junctions simulating the corresponding parts of compact heat exchangers. The cross-section of the header and the channels were fixed to 14 mm x 14 mm and 12 mm x 1.6 mm, respectively. The mass flux and the mass quality ranges were 70-165 kg/m{sup 2} s and 0.3-0.7, respectively. Air and water were used as the test fluids. The flow distribution at the fore part of the header (region A) is affected only by the upstream flow configuration and the rate of liquid flow separation decreased a flowing downwards. On the other hand, in the rear part, the downstream effect predominates over the upstream effect due to strong flow recirculation near the end plate. In this part, the liquid separation increased (region B) and then decreased (region C) as the mixture proceeds downwards. The validity of the existing models for branching flows at parallel T-junction was tested, and turned out to be appropriate for region A. However, the models were not applicable to the rear part due to a strong flow recirculation. Moreover, the effect of the membranes in channels was investigated, but that was minor. (author) The main objective of this work is to examine the flow distribution of two-phase mixture to parallel channels and to investigate the flow behavior at header-channel junctions simulating the corresponding parts of compact heat exchangers. The cross-section of the header and the channels were fixed to 14 mm × 14 mm and 12 mm × 1.6 mm, respectively. The mass flux and the mass quality ranges were 70–165 kg/m 2 s and 0.3–0.7, respectively. Air and water were used as the test fluids. The flow distribution at the fore part of the header (region A) is affected only by the upstream flow configuration and the rate of liquid flow separation decreased a flowing downwards. On the other hand, in the rear part, the downstream effect predominates over the upstream effect due to strong flow recirculation near the end plate. In this part, the liquid separation increased (region B) and then decreased (region C) as the mixture proceeds downwards. The validity of the existing models for branching flows at parallel T-junction was tested, and turned out to be appropriate for region A. However, the models were not applicable to the rear part due to a strong flow recirculation. Moreover, the effect of the membranes in channels was investigated, but that was minor. |
Author | Lee, Jun Kyoung |
Author_xml | – sequence: 1 givenname: Jun Kyoung surname: Lee fullname: Lee, Jun Kyoung email: jklee99@kyungnam.ac.kr organization: School of Mechanical Engineering and Automation, Kyungnam University, Masan 631-701, Republic of Korea |
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Keywords | Header-channels Annular flow Two-phase flow distribution Prediction model Gas liquid interface Two phase flow Pipe flow Test facility Heat exchanger Distribution Compact heat exchanger Experimental study |
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References_xml | – volume: 11 start-page: 223 year: 1999 end-page: 329 ident: bib16 article-title: Phase separation at T junctions publication-title: Multiphase Sci. Technol. contributor: fullname: Azzopardi – volume: 39 start-page: 751 year: 1984 end-page: 765 ident: bib12 article-title: Two phase gas liquid flow in rectangular channels publication-title: Chem. Eng. Sci. contributor: fullname: Ulbrich – volume: 19 start-page: 847 year: 1999 end-page: 863 ident: bib1 article-title: Flow maldistribution in heat exchangers publication-title: App. Ther. Eng. contributor: fullname: Bergles – volume: 25 start-page: 827 year: 1999 end-page: 840 ident: bib6 article-title: Water flow distribution in horizontal header contaminated with bubbles publication-title: Int. J. Multiphase Flow contributor: fullname: Horiki – volume: 14 start-page: 439 year: 1988 end-page: 458 ident: bib8 article-title: Phase separation in dividing two-phase flows publication-title: Int. J. Multiphase Flow contributor: fullname: Lahey – volume: 42 start-page: 2667 year: 1987 end-page: 2676 ident: bib14 article-title: Two-phase flow splitting in a tee junction – experimental and modelling publication-title: Chem. Eng. Sci. contributor: fullname: Taitel – volume: 37 start-page: 297 year: 2003 end-page: 429 ident: bib3 article-title: Microchannel heat exchanger design for evaporator and condenser applications publication-title: Adv. Heat Transfer contributor: fullname: Webb – volume: 6 start-page: 217 year: 2005 end-page: 234 ident: bib10 article-title: Assessment of prediction models for dividing two-phase flow at small T-junctions publication-title: Int. J. Heat Exchang. contributor: fullname: Lee – volume: 26 start-page: 845 year: 2000 end-page: 856 ident: bib15 article-title: The split of annular two phase flow at a small diameter T-junction publication-title: Int. J. 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Multiphase Flow doi: 10.1016/0301-9322(82)90020-9 contributor: fullname: Azzopardi – volume: 6 start-page: 217 year: 2005 ident: 10.1016/j.expthermflusci.2008.03.009_bib10 article-title: Assessment of prediction models for dividing two-phase flow at small T-junctions publication-title: Int. J. Heat Exchang. contributor: fullname: Lee – ident: 10.1016/j.expthermflusci.2008.03.009_bib11 – volume: 11 start-page: 223 year: 1999 ident: 10.1016/j.expthermflusci.2008.03.009_bib16 article-title: Phase separation at T junctions publication-title: Multiphase Sci. Technol. doi: 10.1615/MultScienTechn.v11.i4.10 contributor: fullname: Azzopardi – volume: 22 start-page: 1369 year: 2002 ident: 10.1016/j.expthermflusci.2008.03.009_bib2 article-title: Thermal and hydraulic analysis of a brazed aluminum evaporator publication-title: App. Ther. Eng. doi: 10.1016/S1359-4311(02)00058-3 contributor: fullname: Wu – volume: 39 start-page: 751 year: 1984 ident: 10.1016/j.expthermflusci.2008.03.009_bib12 article-title: Two phase gas liquid flow in rectangular channels publication-title: Chem. Eng. Sci. doi: 10.1016/0009-2509(84)80182-7 contributor: fullname: Troniewski – volume: 42 start-page: 2667 year: 1987 ident: 10.1016/j.expthermflusci.2008.03.009_bib14 article-title: Two-phase flow splitting in a tee junction – experimental and modelling publication-title: Chem. Eng. Sci. doi: 10.1016/0009-2509(87)87017-3 contributor: fullname: Shoham – ident: 10.1016/j.expthermflusci.2008.03.009_bib7 – volume: 14 start-page: 439 year: 1988 ident: 10.1016/j.expthermflusci.2008.03.009_bib8 article-title: Phase separation in dividing two-phase flows publication-title: Int. J. Multiphase Flow doi: 10.1016/0301-9322(88)90021-3 contributor: fullname: Hwang – ident: 10.1016/j.expthermflusci.2008.03.009_bib9 |
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SubjectTerms | AIR Annular flow Applied sciences BRANCHING RATIO Devices using thermal energy DISTRIBUTION DUCTS Energy Energy. Thermal use of fuels ENGINEERING Exact sciences and technology Header-channels HEAT EXCHANGERS Heat exchangers (included heat transformers, condensers, cooling towers) LIQUID FLOW LIQUIDS MASS MEMBRANES Prediction model SIMULATION TWO-PHASE FLOW Two-phase flow distribution WATER |
Title | Two-phase flow behavior inside a header connected to multiple parallel channels |
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