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Influence of the aspect ratio on boiling flows in rectangular mini-channels
This article presents experiments conducted with two single rectangular mini-channels of same hydraulic diameter (1.4 mm) and different aspect ratios for conditions of horizontal boiling flow. The Forane® 365 HX used was subcooled (Δ T sub = 15 °C) for all the boiling curves presented in the paper....
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Published in: | Experimental thermal and fluid science 2011-07, Vol.35 (5), p.797-809 |
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creator | Soupremanien, Ulrich Person, Stephane Le Favre-Marinet, Michel Bultel, Yann |
description | This article presents experiments conducted with two single rectangular mini-channels of same hydraulic diameter (1.4
mm) and different aspect ratios for conditions of horizontal boiling flow. The Forane® 365 HX used was subcooled (Δ
T
sub
=
15
°C) for all the boiling curves presented in the paper. Local heat transfer coefficients were measured for heat flux ranging from 25 to 62
kW
m
−2 and mass flux from 200
kg
m
−2
s
−1 to 400
kg
m
−2
s
−1. The boiling flows were observed with two different cameras (depending on the flow velocity) through a visualization window. The flow patterns in the two channels were compared for similar conditions. The results show that the boiling heat transfer coefficient and the pressure drop values are different for the two single mini-channels. For low heat flux condition, the channel with lowest aspect ratio (
H/
W
=
0.143) has a higher heat transfer coefficient. On the other hand, for high heat flux condition, the opposite situation occurs, namely the heat transfer coefficient becomes higher for the channel with highest aspect ratio (
H/
W
=
0.43). This is probably due to the earlier onset of dryout in the channel with lowest aspect ratio. For the two cases of heating, the pressure drop for the two-phase flow remains lower for the channel with lowest aspect ratio. These results show that the aspect ratio plays a substantial role for boiling flows in rectangular channels. As for single-phase flows, the heat transfer characteristics are significantly influenced (even though the hydraulic diameter remains the same) by this parameter. |
doi_str_mv | 10.1016/j.expthermflusci.2010.06.014 |
format | article |
fullrecord | <record><control><sourceid>proquest_hal_p</sourceid><recordid>TN_cdi_hal_primary_oai_HAL_hal_04714342v1</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S0894177710001263</els_id><sourcerecordid>889443084</sourcerecordid><originalsourceid>FETCH-LOGICAL-c525t-b9b48b0bf5a71874c220f95657489055c8e5fe9510e89f21c63ccd215a545cbd3</originalsourceid><addsrcrecordid>eNqNkU1vGyEQhlHUSnWT_gcOqdoe1hlYWEDqJYqaD9VSL8kZsRhiLAwurNP235eVo0i5VD0hMc-8M5oHoXMCSwJkuNgu3e_9tHFl5-Oh2rCk0EowLIGwE7QgUqiOUjm8QQuQinVECPEOva91CwCSElig73ep9bpkHc4etyxs6t7ZCRczhYxzwmMOMaRH7GP-VXFIuLSySY-HaArehRQ6uzEpuVjP0FtvYnUfnt9T9HD97f7qtlv9uLm7ulx1llM-daMamRxh9NyItiKzlIJXfOCCSQWcW-m4d4oTcFJ5SuzQW7umhBvOuB3X_Sn6cszdmKj3JexM-aOzCfr2cqXnP2CCsJ7RJ9LYT0d2X_LPg6uT3oVqXYwmuXyoWra7sB4ka-Tnf5JkEEKRXknV0K9H1JZca3H-ZQsCejajt_q1GT2b0TDoZqa1f3yeZKo10ReTbKgvGZRRpijrG3d95Npt3VNwRbekWdU6zA70Oof_G_gXSpGryw</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>1677913989</pqid></control><display><type>article</type><title>Influence of the aspect ratio on boiling flows in rectangular mini-channels</title><source>ScienceDirect Freedom Collection</source><creator>Soupremanien, Ulrich ; Person, Stephane Le ; Favre-Marinet, Michel ; Bultel, Yann</creator><creatorcontrib>Soupremanien, Ulrich ; Person, Stephane Le ; Favre-Marinet, Michel ; Bultel, Yann</creatorcontrib><description>This article presents experiments conducted with two single rectangular mini-channels of same hydraulic diameter (1.4
mm) and different aspect ratios for conditions of horizontal boiling flow. The Forane® 365 HX used was subcooled (Δ
T
sub
=
15
°C) for all the boiling curves presented in the paper. Local heat transfer coefficients were measured for heat flux ranging from 25 to 62
kW
m
−2 and mass flux from 200
kg
m
−2
s
−1 to 400
kg
m
−2
s
−1. The boiling flows were observed with two different cameras (depending on the flow velocity) through a visualization window. The flow patterns in the two channels were compared for similar conditions. The results show that the boiling heat transfer coefficient and the pressure drop values are different for the two single mini-channels. For low heat flux condition, the channel with lowest aspect ratio (
H/
W
=
0.143) has a higher heat transfer coefficient. On the other hand, for high heat flux condition, the opposite situation occurs, namely the heat transfer coefficient becomes higher for the channel with highest aspect ratio (
H/
W
=
0.43). This is probably due to the earlier onset of dryout in the channel with lowest aspect ratio. For the two cases of heating, the pressure drop for the two-phase flow remains lower for the channel with lowest aspect ratio. These results show that the aspect ratio plays a substantial role for boiling flows in rectangular channels. As for single-phase flows, the heat transfer characteristics are significantly influenced (even though the hydraulic diameter remains the same) by this parameter.</description><identifier>ISSN: 0894-1777</identifier><identifier>EISSN: 1879-2286</identifier><identifier>DOI: 10.1016/j.expthermflusci.2010.06.014</identifier><language>eng</language><publisher>Amsterdam: Elsevier Inc</publisher><subject>Applied sciences ; Aspect ratio ; Boiling ; Channels ; Energy ; Energy. Thermal use of fuels ; Engineering Sciences ; Exact sciences and technology ; Fluid dynamics ; Fluid flow ; Forane ; Heat flux ; Heat transfer ; Heat transfer coefficients ; Rectangular mini-channels ; Subcooled boiling flow ; Theoretical studies. Data and constants. Metering</subject><ispartof>Experimental thermal and fluid science, 2011-07, Vol.35 (5), p.797-809</ispartof><rights>2010 Elsevier Inc.</rights><rights>2015 INIST-CNRS</rights><rights>Distributed under a Creative Commons Attribution 4.0 International License</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c525t-b9b48b0bf5a71874c220f95657489055c8e5fe9510e89f21c63ccd215a545cbd3</citedby><cites>FETCH-LOGICAL-c525t-b9b48b0bf5a71874c220f95657489055c8e5fe9510e89f21c63ccd215a545cbd3</cites><orcidid>0000-0001-7092-6296</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>230,309,310,314,780,784,789,790,885,23930,23931,25140,27924,27925</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=24249243$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://hal.science/hal-04714342$$DView record in HAL$$Hfree_for_read</backlink></links><search><creatorcontrib>Soupremanien, Ulrich</creatorcontrib><creatorcontrib>Person, Stephane Le</creatorcontrib><creatorcontrib>Favre-Marinet, Michel</creatorcontrib><creatorcontrib>Bultel, Yann</creatorcontrib><title>Influence of the aspect ratio on boiling flows in rectangular mini-channels</title><title>Experimental thermal and fluid science</title><description>This article presents experiments conducted with two single rectangular mini-channels of same hydraulic diameter (1.4
mm) and different aspect ratios for conditions of horizontal boiling flow. The Forane® 365 HX used was subcooled (Δ
T
sub
=
15
°C) for all the boiling curves presented in the paper. Local heat transfer coefficients were measured for heat flux ranging from 25 to 62
kW
m
−2 and mass flux from 200
kg
m
−2
s
−1 to 400
kg
m
−2
s
−1. The boiling flows were observed with two different cameras (depending on the flow velocity) through a visualization window. The flow patterns in the two channels were compared for similar conditions. The results show that the boiling heat transfer coefficient and the pressure drop values are different for the two single mini-channels. For low heat flux condition, the channel with lowest aspect ratio (
H/
W
=
0.143) has a higher heat transfer coefficient. On the other hand, for high heat flux condition, the opposite situation occurs, namely the heat transfer coefficient becomes higher for the channel with highest aspect ratio (
H/
W
=
0.43). This is probably due to the earlier onset of dryout in the channel with lowest aspect ratio. For the two cases of heating, the pressure drop for the two-phase flow remains lower for the channel with lowest aspect ratio. These results show that the aspect ratio plays a substantial role for boiling flows in rectangular channels. As for single-phase flows, the heat transfer characteristics are significantly influenced (even though the hydraulic diameter remains the same) by this parameter.</description><subject>Applied sciences</subject><subject>Aspect ratio</subject><subject>Boiling</subject><subject>Channels</subject><subject>Energy</subject><subject>Energy. Thermal use of fuels</subject><subject>Engineering Sciences</subject><subject>Exact sciences and technology</subject><subject>Fluid dynamics</subject><subject>Fluid flow</subject><subject>Forane</subject><subject>Heat flux</subject><subject>Heat transfer</subject><subject>Heat transfer coefficients</subject><subject>Rectangular mini-channels</subject><subject>Subcooled boiling flow</subject><subject>Theoretical studies. Data and constants. Metering</subject><issn>0894-1777</issn><issn>1879-2286</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2011</creationdate><recordtype>article</recordtype><recordid>eNqNkU1vGyEQhlHUSnWT_gcOqdoe1hlYWEDqJYqaD9VSL8kZsRhiLAwurNP235eVo0i5VD0hMc-8M5oHoXMCSwJkuNgu3e_9tHFl5-Oh2rCk0EowLIGwE7QgUqiOUjm8QQuQinVECPEOva91CwCSElig73ep9bpkHc4etyxs6t7ZCRczhYxzwmMOMaRH7GP-VXFIuLSySY-HaArehRQ6uzEpuVjP0FtvYnUfnt9T9HD97f7qtlv9uLm7ulx1llM-daMamRxh9NyItiKzlIJXfOCCSQWcW-m4d4oTcFJ5SuzQW7umhBvOuB3X_Sn6cszdmKj3JexM-aOzCfr2cqXnP2CCsJ7RJ9LYT0d2X_LPg6uT3oVqXYwmuXyoWra7sB4ka-Tnf5JkEEKRXknV0K9H1JZca3H-ZQsCejajt_q1GT2b0TDoZqa1f3yeZKo10ReTbKgvGZRRpijrG3d95Npt3VNwRbekWdU6zA70Oof_G_gXSpGryw</recordid><startdate>20110701</startdate><enddate>20110701</enddate><creator>Soupremanien, Ulrich</creator><creator>Person, Stephane Le</creator><creator>Favre-Marinet, Michel</creator><creator>Bultel, Yann</creator><general>Elsevier Inc</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7TB</scope><scope>7U5</scope><scope>8FD</scope><scope>FR3</scope><scope>H8D</scope><scope>KR7</scope><scope>L7M</scope><scope>7QH</scope><scope>7UA</scope><scope>C1K</scope><scope>F1W</scope><scope>H96</scope><scope>L.G</scope><scope>1XC</scope><orcidid>https://orcid.org/0000-0001-7092-6296</orcidid></search><sort><creationdate>20110701</creationdate><title>Influence of the aspect ratio on boiling flows in rectangular mini-channels</title><author>Soupremanien, Ulrich ; Person, Stephane Le ; Favre-Marinet, Michel ; Bultel, Yann</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c525t-b9b48b0bf5a71874c220f95657489055c8e5fe9510e89f21c63ccd215a545cbd3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2011</creationdate><topic>Applied sciences</topic><topic>Aspect ratio</topic><topic>Boiling</topic><topic>Channels</topic><topic>Energy</topic><topic>Energy. Thermal use of fuels</topic><topic>Engineering Sciences</topic><topic>Exact sciences and technology</topic><topic>Fluid dynamics</topic><topic>Fluid flow</topic><topic>Forane</topic><topic>Heat flux</topic><topic>Heat transfer</topic><topic>Heat transfer coefficients</topic><topic>Rectangular mini-channels</topic><topic>Subcooled boiling flow</topic><topic>Theoretical studies. Data and constants. Metering</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Soupremanien, Ulrich</creatorcontrib><creatorcontrib>Person, Stephane Le</creatorcontrib><creatorcontrib>Favre-Marinet, Michel</creatorcontrib><creatorcontrib>Bultel, Yann</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Aqualine</collection><collection>Water Resources Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ASFA: Aquatic Sciences and Fisheries Abstracts</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) 2: Ocean Technology, Policy & Non-Living Resources</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) Professional</collection><collection>Hyper Article en Ligne (HAL)</collection><jtitle>Experimental thermal and fluid science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Soupremanien, Ulrich</au><au>Person, Stephane Le</au><au>Favre-Marinet, Michel</au><au>Bultel, Yann</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Influence of the aspect ratio on boiling flows in rectangular mini-channels</atitle><jtitle>Experimental thermal and fluid science</jtitle><date>2011-07-01</date><risdate>2011</risdate><volume>35</volume><issue>5</issue><spage>797</spage><epage>809</epage><pages>797-809</pages><issn>0894-1777</issn><eissn>1879-2286</eissn><abstract>This article presents experiments conducted with two single rectangular mini-channels of same hydraulic diameter (1.4
mm) and different aspect ratios for conditions of horizontal boiling flow. The Forane® 365 HX used was subcooled (Δ
T
sub
=
15
°C) for all the boiling curves presented in the paper. Local heat transfer coefficients were measured for heat flux ranging from 25 to 62
kW
m
−2 and mass flux from 200
kg
m
−2
s
−1 to 400
kg
m
−2
s
−1. The boiling flows were observed with two different cameras (depending on the flow velocity) through a visualization window. The flow patterns in the two channels were compared for similar conditions. The results show that the boiling heat transfer coefficient and the pressure drop values are different for the two single mini-channels. For low heat flux condition, the channel with lowest aspect ratio (
H/
W
=
0.143) has a higher heat transfer coefficient. On the other hand, for high heat flux condition, the opposite situation occurs, namely the heat transfer coefficient becomes higher for the channel with highest aspect ratio (
H/
W
=
0.43). This is probably due to the earlier onset of dryout in the channel with lowest aspect ratio. For the two cases of heating, the pressure drop for the two-phase flow remains lower for the channel with lowest aspect ratio. These results show that the aspect ratio plays a substantial role for boiling flows in rectangular channels. As for single-phase flows, the heat transfer characteristics are significantly influenced (even though the hydraulic diameter remains the same) by this parameter.</abstract><cop>Amsterdam</cop><pub>Elsevier Inc</pub><doi>10.1016/j.expthermflusci.2010.06.014</doi><tpages>13</tpages><orcidid>https://orcid.org/0000-0001-7092-6296</orcidid></addata></record> |
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language | eng |
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source | ScienceDirect Freedom Collection |
subjects | Applied sciences Aspect ratio Boiling Channels Energy Energy. Thermal use of fuels Engineering Sciences Exact sciences and technology Fluid dynamics Fluid flow Forane Heat flux Heat transfer Heat transfer coefficients Rectangular mini-channels Subcooled boiling flow Theoretical studies. Data and constants. Metering |
title | Influence of the aspect ratio on boiling flows in rectangular mini-channels |
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