An experimental study of refrigerant distribution in an automotive condenser
•R-134a distribution into parallel flow condenser was investigated in detail.•The flow distribution was relatively uniform except at top and bottommost channels.•The thermal degradation by flow mal-distribution was not significant (0.1–2.8%).•Correlations were developed as a function of gas Reynolds...
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Veröffentlicht in: | Applied thermal engineering 2021-02, Vol.184, p.116259, Article 116259 |
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creator | Kim, C.-H. Kim, N.-H. |
description | •R-134a distribution into parallel flow condenser was investigated in detail.•The flow distribution was relatively uniform except at top and bottommost channels.•The thermal degradation by flow mal-distribution was not significant (0.1–2.8%).•Correlations were developed as a function of gas Reynolds number and quality.
The literature shows almost no prior investigations on two-phase flow distribution in a parallel flow condenser. In the present study, R-134a flow distribution tests were conducted in the test section, which simulated an actual parallel flow condenser having 58 mini-channel tubes and 4 passes. R-134a gas was supplied at 25 °C superheat, which exited the test section at 5 °C subcooled condition. At inlet of the header, the flow distribution was relatively uniform, except at topmost channels. At the second and third pass, the flow distribution was also relatively uniform except at topmost and bottommost channels. At the exit of each pass, two-phase jets were issued from the tubes of the previous pass, which hit opposite wall of the header, and flowed downward forming a liquid film. At the bottom of the header, the remnant liquid, which was not supplied into the next pass, formed a liquid pool. The thermal degradation due to flow mal-distribution was not significant (0.1–2.82%), which increased as mass flux decreased. Flow distribution correlations were developed to predict the fraction of liquid or gas taken off by downstream channel as a function of gas Reynolds number and channel inlet vapor quality. |
doi_str_mv | 10.1016/j.applthermaleng.2020.116259 |
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The literature shows almost no prior investigations on two-phase flow distribution in a parallel flow condenser. In the present study, R-134a flow distribution tests were conducted in the test section, which simulated an actual parallel flow condenser having 58 mini-channel tubes and 4 passes. R-134a gas was supplied at 25 °C superheat, which exited the test section at 5 °C subcooled condition. At inlet of the header, the flow distribution was relatively uniform, except at topmost channels. At the second and third pass, the flow distribution was also relatively uniform except at topmost and bottommost channels. At the exit of each pass, two-phase jets were issued from the tubes of the previous pass, which hit opposite wall of the header, and flowed downward forming a liquid film. At the bottom of the header, the remnant liquid, which was not supplied into the next pass, formed a liquid pool. The thermal degradation due to flow mal-distribution was not significant (0.1–2.82%), which increased as mass flux decreased. Flow distribution correlations were developed to predict the fraction of liquid or gas taken off by downstream channel as a function of gas Reynolds number and channel inlet vapor quality.</description><identifier>ISSN: 1359-4311</identifier><identifier>EISSN: 1873-5606</identifier><identifier>DOI: 10.1016/j.applthermaleng.2020.116259</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Channels ; Condenser ; Condenser tubes ; Condensers ; Flow distribution ; Fluid dynamics ; Fluid flow ; Header ; Heat exchanger ; Parallel flow ; Reynolds number ; Simulation ; Studies ; Thermal degradation ; Two phase flow</subject><ispartof>Applied thermal engineering, 2021-02, Vol.184, p.116259, Article 116259</ispartof><rights>2020 Elsevier Ltd</rights><rights>Copyright Elsevier BV Feb 5, 2021</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c358t-aa13814d866d14c78cd5bb17b4df1b785e38dc1d8103329b5cb78e07d8d72b03</citedby><cites>FETCH-LOGICAL-c358t-aa13814d866d14c78cd5bb17b4df1b785e38dc1d8103329b5cb78e07d8d72b03</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S1359431120337388$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65306</link.rule.ids></links><search><creatorcontrib>Kim, C.-H.</creatorcontrib><creatorcontrib>Kim, N.-H.</creatorcontrib><title>An experimental study of refrigerant distribution in an automotive condenser</title><title>Applied thermal engineering</title><description>•R-134a distribution into parallel flow condenser was investigated in detail.•The flow distribution was relatively uniform except at top and bottommost channels.•The thermal degradation by flow mal-distribution was not significant (0.1–2.8%).•Correlations were developed as a function of gas Reynolds number and quality.
The literature shows almost no prior investigations on two-phase flow distribution in a parallel flow condenser. In the present study, R-134a flow distribution tests were conducted in the test section, which simulated an actual parallel flow condenser having 58 mini-channel tubes and 4 passes. R-134a gas was supplied at 25 °C superheat, which exited the test section at 5 °C subcooled condition. At inlet of the header, the flow distribution was relatively uniform, except at topmost channels. At the second and third pass, the flow distribution was also relatively uniform except at topmost and bottommost channels. At the exit of each pass, two-phase jets were issued from the tubes of the previous pass, which hit opposite wall of the header, and flowed downward forming a liquid film. At the bottom of the header, the remnant liquid, which was not supplied into the next pass, formed a liquid pool. The thermal degradation due to flow mal-distribution was not significant (0.1–2.82%), which increased as mass flux decreased. Flow distribution correlations were developed to predict the fraction of liquid or gas taken off by downstream channel as a function of gas Reynolds number and channel inlet vapor quality.</description><subject>Channels</subject><subject>Condenser</subject><subject>Condenser tubes</subject><subject>Condensers</subject><subject>Flow distribution</subject><subject>Fluid dynamics</subject><subject>Fluid flow</subject><subject>Header</subject><subject>Heat exchanger</subject><subject>Parallel flow</subject><subject>Reynolds number</subject><subject>Simulation</subject><subject>Studies</subject><subject>Thermal degradation</subject><subject>Two phase flow</subject><issn>1359-4311</issn><issn>1873-5606</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><recordid>eNqNUMtqwzAQNKWFpmn_wdBenWoty1aglxD6gkAvuQtZWqcyjuRKcmj-vgrppbfCwi67M7PMZNkDkAUQqB_7hRzHIX6i38sB7W5RkjKdoC7Z8iKbAW9owWpSX6aZsmVRUYDr7CaEnhAoeVPNss3K5vg9ojd7tFEOeYiTPuauyz123uzQSxtzbUL0pp2icTY3Npeppuj2LpoD5spZjTagv82uOjkEvPvt82z78rxdvxWbj9f39WpTKMp4LKQEyqHSvK41VKrhSrO2haatdAdtwxlSrhVoDoTSctkylZZIGs11U7aEzrP7s-zo3deEIYreTd6mj6JkhFY1ozUk1NMZpbwLIbkRYzIp_VEAEaf4RC_-xidO8YlzfIn-cqZjMnIw6EVQBq1CbTyqKLQz_xP6AR5tgpg</recordid><startdate>20210205</startdate><enddate>20210205</enddate><creator>Kim, C.-H.</creator><creator>Kim, N.-H.</creator><general>Elsevier Ltd</general><general>Elsevier BV</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7TB</scope><scope>8FD</scope><scope>FR3</scope><scope>KR7</scope></search><sort><creationdate>20210205</creationdate><title>An experimental study of refrigerant distribution in an automotive condenser</title><author>Kim, C.-H. ; Kim, N.-H.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c358t-aa13814d866d14c78cd5bb17b4df1b785e38dc1d8103329b5cb78e07d8d72b03</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2021</creationdate><topic>Channels</topic><topic>Condenser</topic><topic>Condenser tubes</topic><topic>Condensers</topic><topic>Flow distribution</topic><topic>Fluid dynamics</topic><topic>Fluid flow</topic><topic>Header</topic><topic>Heat exchanger</topic><topic>Parallel flow</topic><topic>Reynolds number</topic><topic>Simulation</topic><topic>Studies</topic><topic>Thermal degradation</topic><topic>Two phase flow</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Kim, C.-H.</creatorcontrib><creatorcontrib>Kim, N.-H.</creatorcontrib><collection>CrossRef</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><jtitle>Applied thermal engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Kim, C.-H.</au><au>Kim, N.-H.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>An experimental study of refrigerant distribution in an automotive condenser</atitle><jtitle>Applied thermal engineering</jtitle><date>2021-02-05</date><risdate>2021</risdate><volume>184</volume><spage>116259</spage><pages>116259-</pages><artnum>116259</artnum><issn>1359-4311</issn><eissn>1873-5606</eissn><abstract>•R-134a distribution into parallel flow condenser was investigated in detail.•The flow distribution was relatively uniform except at top and bottommost channels.•The thermal degradation by flow mal-distribution was not significant (0.1–2.8%).•Correlations were developed as a function of gas Reynolds number and quality.
The literature shows almost no prior investigations on two-phase flow distribution in a parallel flow condenser. In the present study, R-134a flow distribution tests were conducted in the test section, which simulated an actual parallel flow condenser having 58 mini-channel tubes and 4 passes. R-134a gas was supplied at 25 °C superheat, which exited the test section at 5 °C subcooled condition. At inlet of the header, the flow distribution was relatively uniform, except at topmost channels. At the second and third pass, the flow distribution was also relatively uniform except at topmost and bottommost channels. At the exit of each pass, two-phase jets were issued from the tubes of the previous pass, which hit opposite wall of the header, and flowed downward forming a liquid film. At the bottom of the header, the remnant liquid, which was not supplied into the next pass, formed a liquid pool. The thermal degradation due to flow mal-distribution was not significant (0.1–2.82%), which increased as mass flux decreased. Flow distribution correlations were developed to predict the fraction of liquid or gas taken off by downstream channel as a function of gas Reynolds number and channel inlet vapor quality.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.applthermaleng.2020.116259</doi></addata></record> |
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subjects | Channels Condenser Condenser tubes Condensers Flow distribution Fluid dynamics Fluid flow Header Heat exchanger Parallel flow Reynolds number Simulation Studies Thermal degradation Two phase flow |
title | An experimental study of refrigerant distribution in an automotive condenser |
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