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 inExperimental thermal and fluid science Vol. 33; no. 2; pp. 195 - 202
Main Author Lee, Jun Kyoung
Format Journal Article
LanguageEnglish
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.
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
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Issue 2
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
Language English
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Snippet 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...
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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
URI https://dx.doi.org/10.1016/j.expthermflusci.2008.03.009
https://search.proquest.com/docview/33021901
https://www.osti.gov/biblio/21137936
Volume 33
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