Flow boiling heat transfer of zeotropic mixture R1234yf/R32 inside a horizontal multiport tube

•Experimental studies of R1234yf/R32 mixtures were conducted.•Flow boiling heat transfer and pressure drop inside multiport tubes were examined.•Heat transfer and pressure drops of mixtures and pure components were compared.•Effects of mass flux, heat flux, and quality on flow boiling were clarified...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Veröffentlicht in:International journal of refrigeration 2020-11, Vol.119, p.390-400
Hauptverfasser: Jige, Daisuke, Kikuchi, Shogo, Mikajiri, Naoki, Inoue, Norihiro
Format: Artikel
Sprache:eng
Schlagworte:
Online-Zugang:Volltext
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
container_end_page 400
container_issue
container_start_page 390
container_title International journal of refrigeration
container_volume 119
creator Jige, Daisuke
Kikuchi, Shogo
Mikajiri, Naoki
Inoue, Norihiro
description •Experimental studies of R1234yf/R32 mixtures were conducted.•Flow boiling heat transfer and pressure drop inside multiport tubes were examined.•Heat transfer and pressure drops of mixtures and pure components were compared.•Effects of mass flux, heat flux, and quality on flow boiling were clarified.•A predictive heat transfer correlation for refrigerant mixtures was proposed. The flow boiling heat transfer and pressure drop of zeotropic binary mixture R1234yf/R32 were experimentally investigated inside a horizontal multiport tube with rectangular minichannels. Local heat transfer coefficients were quantified under mass fluxes in the range 50–400 kgm−2s−1, heat fluxes in the range 5–20 kWm−2, and circulation compositions of 80/20 and 50/50mass%. The obtained heat transfer coefficient of the mixtures were compared with those of pure components under the same experimental conditions. The heat transfer of the mixtures was strongly influenced by mass flux, vapor quality, and mass fraction, whereas the influence of heat flux on heat transfer was small. The heat transfer coefficients of the mixtures were lower than those of the pure components under most conditions owing to mass diffusion resistance and temperature glide; however, the heat transfer coefficients of the mixtures were same or higher than those of R1234yf at high mass flux and high vapor quality regions. The frictional pressure drops of the mixtures increased with increasing mass flux, vapor quality, and mass fraction of R1234yf. The database encompassing more than 900 and 190 for boiling heat transfer coefficient and frictional pressure drop were compared with available previous correlations. Previous correlations underestimated the heat transfer coefficients of the mixtures, especially for data with higher temperature glide and dominant forced convective heat transfer. The proposed correlation shows good agreement with the heat transfer coefficients of the R1234yf/R32 mixtures with mean and mean absolute deviations of −5.0% and 10.3%, respectively.
doi_str_mv 10.1016/j.ijrefrig.2020.04.036
format Article
fullrecord <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_journals_2465476671</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S0140700720302681</els_id><sourcerecordid>2465476671</sourcerecordid><originalsourceid>FETCH-LOGICAL-c406t-e0cb73dcb798b1a8e2a4e4df82feb992bb94c8e0e0966aeb91b6bda3908b8cbf3</originalsourceid><addsrcrecordid>eNqFkEFr3DAQhUVpodtN_kIQ9GxnJCuyfGsJSRpYCCzNtUKSx7syXmsryWmTX1-FTc-5zMDw3hveR8gFg5oBk5dj7ceIQ_S7mgOHGkQNjfxAVky1XcVBsY9kBUxA1QK0n8mXlEYA1sKVWpFft1P4Q23wk593dI8m0xzNnAaMNAz0BUOO4egdPfi_eYlIt4w34nm43Dac-jn5Hqmh-xD9S5izmehhmbI_hlhyFotn5NNgpoTnb3tNHm9vfl7_qDYPd_fX3zeVEyBzheBs2_RldMoyo5AbgaIfFB_Qdh23thNOISB0UppyYlba3jQdKKucHZo1-XrKPcbwe8GU9RiWOJeXmgt5JVopW1ZU8qRyMaRUmOlj9AcTnzUD_cpSj_o_S_3KUoPQhWUxfjsZsXR48hh1ch5nh72P6LLug38v4h-tSIIk</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>2465476671</pqid></control><display><type>article</type><title>Flow boiling heat transfer of zeotropic mixture R1234yf/R32 inside a horizontal multiport tube</title><source>Elsevier ScienceDirect Journals Complete</source><creator>Jige, Daisuke ; Kikuchi, Shogo ; Mikajiri, Naoki ; Inoue, Norihiro</creator><creatorcontrib>Jige, Daisuke ; Kikuchi, Shogo ; Mikajiri, Naoki ; Inoue, Norihiro</creatorcontrib><description>•Experimental studies of R1234yf/R32 mixtures were conducted.•Flow boiling heat transfer and pressure drop inside multiport tubes were examined.•Heat transfer and pressure drops of mixtures and pure components were compared.•Effects of mass flux, heat flux, and quality on flow boiling were clarified.•A predictive heat transfer correlation for refrigerant mixtures was proposed. The flow boiling heat transfer and pressure drop of zeotropic binary mixture R1234yf/R32 were experimentally investigated inside a horizontal multiport tube with rectangular minichannels. Local heat transfer coefficients were quantified under mass fluxes in the range 50–400 kgm−2s−1, heat fluxes in the range 5–20 kWm−2, and circulation compositions of 80/20 and 50/50mass%. The obtained heat transfer coefficient of the mixtures were compared with those of pure components under the same experimental conditions. The heat transfer of the mixtures was strongly influenced by mass flux, vapor quality, and mass fraction, whereas the influence of heat flux on heat transfer was small. The heat transfer coefficients of the mixtures were lower than those of the pure components under most conditions owing to mass diffusion resistance and temperature glide; however, the heat transfer coefficients of the mixtures were same or higher than those of R1234yf at high mass flux and high vapor quality regions. The frictional pressure drops of the mixtures increased with increasing mass flux, vapor quality, and mass fraction of R1234yf. The database encompassing more than 900 and 190 for boiling heat transfer coefficient and frictional pressure drop were compared with available previous correlations. Previous correlations underestimated the heat transfer coefficients of the mixtures, especially for data with higher temperature glide and dominant forced convective heat transfer. The proposed correlation shows good agreement with the heat transfer coefficients of the R1234yf/R32 mixtures with mean and mean absolute deviations of −5.0% and 10.3%, respectively.</description><identifier>ISSN: 0140-7007</identifier><identifier>EISSN: 1879-2081</identifier><identifier>DOI: 10.1016/j.ijrefrig.2020.04.036</identifier><language>eng</language><publisher>Paris: Elsevier Ltd</publisher><subject>Binary mixtures ; Boiling ; Boiling flow ; Chute de pression ; Convective heat transfer ; Correlation ; Heat flux ; Heat transfer ; Heat transfer coefficients ; Mini-canal ; Minichannel ; Multiport tube ; Mélange de frigorigènes zéotrope ; Pressure ; Pressure drop ; Temperature ; Transfert de chaleur ; Tube multi-ports ; Vapors ; Zeotropic mixtures ; Zeotropic refrigerant mixture ; Ébullition en écoulement</subject><ispartof>International journal of refrigeration, 2020-11, Vol.119, p.390-400</ispartof><rights>2020</rights><rights>Copyright Elsevier Science Ltd. Nov 2020</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c406t-e0cb73dcb798b1a8e2a4e4df82feb992bb94c8e0e0966aeb91b6bda3908b8cbf3</citedby><cites>FETCH-LOGICAL-c406t-e0cb73dcb798b1a8e2a4e4df82feb992bb94c8e0e0966aeb91b6bda3908b8cbf3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.ijrefrig.2020.04.036$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,27924,27925,45995</link.rule.ids></links><search><creatorcontrib>Jige, Daisuke</creatorcontrib><creatorcontrib>Kikuchi, Shogo</creatorcontrib><creatorcontrib>Mikajiri, Naoki</creatorcontrib><creatorcontrib>Inoue, Norihiro</creatorcontrib><title>Flow boiling heat transfer of zeotropic mixture R1234yf/R32 inside a horizontal multiport tube</title><title>International journal of refrigeration</title><description>•Experimental studies of R1234yf/R32 mixtures were conducted.•Flow boiling heat transfer and pressure drop inside multiport tubes were examined.•Heat transfer and pressure drops of mixtures and pure components were compared.•Effects of mass flux, heat flux, and quality on flow boiling were clarified.•A predictive heat transfer correlation for refrigerant mixtures was proposed. The flow boiling heat transfer and pressure drop of zeotropic binary mixture R1234yf/R32 were experimentally investigated inside a horizontal multiport tube with rectangular minichannels. Local heat transfer coefficients were quantified under mass fluxes in the range 50–400 kgm−2s−1, heat fluxes in the range 5–20 kWm−2, and circulation compositions of 80/20 and 50/50mass%. The obtained heat transfer coefficient of the mixtures were compared with those of pure components under the same experimental conditions. The heat transfer of the mixtures was strongly influenced by mass flux, vapor quality, and mass fraction, whereas the influence of heat flux on heat transfer was small. The heat transfer coefficients of the mixtures were lower than those of the pure components under most conditions owing to mass diffusion resistance and temperature glide; however, the heat transfer coefficients of the mixtures were same or higher than those of R1234yf at high mass flux and high vapor quality regions. The frictional pressure drops of the mixtures increased with increasing mass flux, vapor quality, and mass fraction of R1234yf. The database encompassing more than 900 and 190 for boiling heat transfer coefficient and frictional pressure drop were compared with available previous correlations. Previous correlations underestimated the heat transfer coefficients of the mixtures, especially for data with higher temperature glide and dominant forced convective heat transfer. The proposed correlation shows good agreement with the heat transfer coefficients of the R1234yf/R32 mixtures with mean and mean absolute deviations of −5.0% and 10.3%, respectively.</description><subject>Binary mixtures</subject><subject>Boiling</subject><subject>Boiling flow</subject><subject>Chute de pression</subject><subject>Convective heat transfer</subject><subject>Correlation</subject><subject>Heat flux</subject><subject>Heat transfer</subject><subject>Heat transfer coefficients</subject><subject>Mini-canal</subject><subject>Minichannel</subject><subject>Multiport tube</subject><subject>Mélange de frigorigènes zéotrope</subject><subject>Pressure</subject><subject>Pressure drop</subject><subject>Temperature</subject><subject>Transfert de chaleur</subject><subject>Tube multi-ports</subject><subject>Vapors</subject><subject>Zeotropic mixtures</subject><subject>Zeotropic refrigerant mixture</subject><subject>Ébullition en écoulement</subject><issn>0140-7007</issn><issn>1879-2081</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2020</creationdate><recordtype>article</recordtype><recordid>eNqFkEFr3DAQhUVpodtN_kIQ9GxnJCuyfGsJSRpYCCzNtUKSx7syXmsryWmTX1-FTc-5zMDw3hveR8gFg5oBk5dj7ceIQ_S7mgOHGkQNjfxAVky1XcVBsY9kBUxA1QK0n8mXlEYA1sKVWpFft1P4Q23wk593dI8m0xzNnAaMNAz0BUOO4egdPfi_eYlIt4w34nm43Dac-jn5Hqmh-xD9S5izmehhmbI_hlhyFotn5NNgpoTnb3tNHm9vfl7_qDYPd_fX3zeVEyBzheBs2_RldMoyo5AbgaIfFB_Qdh23thNOISB0UppyYlba3jQdKKucHZo1-XrKPcbwe8GU9RiWOJeXmgt5JVopW1ZU8qRyMaRUmOlj9AcTnzUD_cpSj_o_S_3KUoPQhWUxfjsZsXR48hh1ch5nh72P6LLug38v4h-tSIIk</recordid><startdate>202011</startdate><enddate>202011</enddate><creator>Jige, Daisuke</creator><creator>Kikuchi, Shogo</creator><creator>Mikajiri, Naoki</creator><creator>Inoue, Norihiro</creator><general>Elsevier Ltd</general><general>Elsevier Science Ltd</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7TB</scope><scope>8FD</scope><scope>FR3</scope></search><sort><creationdate>202011</creationdate><title>Flow boiling heat transfer of zeotropic mixture R1234yf/R32 inside a horizontal multiport tube</title><author>Jige, Daisuke ; Kikuchi, Shogo ; Mikajiri, Naoki ; Inoue, Norihiro</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c406t-e0cb73dcb798b1a8e2a4e4df82feb992bb94c8e0e0966aeb91b6bda3908b8cbf3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2020</creationdate><topic>Binary mixtures</topic><topic>Boiling</topic><topic>Boiling flow</topic><topic>Chute de pression</topic><topic>Convective heat transfer</topic><topic>Correlation</topic><topic>Heat flux</topic><topic>Heat transfer</topic><topic>Heat transfer coefficients</topic><topic>Mini-canal</topic><topic>Minichannel</topic><topic>Multiport tube</topic><topic>Mélange de frigorigènes zéotrope</topic><topic>Pressure</topic><topic>Pressure drop</topic><topic>Temperature</topic><topic>Transfert de chaleur</topic><topic>Tube multi-ports</topic><topic>Vapors</topic><topic>Zeotropic mixtures</topic><topic>Zeotropic refrigerant mixture</topic><topic>Ébullition en écoulement</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Jige, Daisuke</creatorcontrib><creatorcontrib>Kikuchi, Shogo</creatorcontrib><creatorcontrib>Mikajiri, Naoki</creatorcontrib><creatorcontrib>Inoue, Norihiro</creatorcontrib><collection>CrossRef</collection><collection>Mechanical &amp; Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><jtitle>International journal of refrigeration</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Jige, Daisuke</au><au>Kikuchi, Shogo</au><au>Mikajiri, Naoki</au><au>Inoue, Norihiro</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Flow boiling heat transfer of zeotropic mixture R1234yf/R32 inside a horizontal multiport tube</atitle><jtitle>International journal of refrigeration</jtitle><date>2020-11</date><risdate>2020</risdate><volume>119</volume><spage>390</spage><epage>400</epage><pages>390-400</pages><issn>0140-7007</issn><eissn>1879-2081</eissn><abstract>•Experimental studies of R1234yf/R32 mixtures were conducted.•Flow boiling heat transfer and pressure drop inside multiport tubes were examined.•Heat transfer and pressure drops of mixtures and pure components were compared.•Effects of mass flux, heat flux, and quality on flow boiling were clarified.•A predictive heat transfer correlation for refrigerant mixtures was proposed. The flow boiling heat transfer and pressure drop of zeotropic binary mixture R1234yf/R32 were experimentally investigated inside a horizontal multiport tube with rectangular minichannels. Local heat transfer coefficients were quantified under mass fluxes in the range 50–400 kgm−2s−1, heat fluxes in the range 5–20 kWm−2, and circulation compositions of 80/20 and 50/50mass%. The obtained heat transfer coefficient of the mixtures were compared with those of pure components under the same experimental conditions. The heat transfer of the mixtures was strongly influenced by mass flux, vapor quality, and mass fraction, whereas the influence of heat flux on heat transfer was small. The heat transfer coefficients of the mixtures were lower than those of the pure components under most conditions owing to mass diffusion resistance and temperature glide; however, the heat transfer coefficients of the mixtures were same or higher than those of R1234yf at high mass flux and high vapor quality regions. The frictional pressure drops of the mixtures increased with increasing mass flux, vapor quality, and mass fraction of R1234yf. The database encompassing more than 900 and 190 for boiling heat transfer coefficient and frictional pressure drop were compared with available previous correlations. Previous correlations underestimated the heat transfer coefficients of the mixtures, especially for data with higher temperature glide and dominant forced convective heat transfer. The proposed correlation shows good agreement with the heat transfer coefficients of the R1234yf/R32 mixtures with mean and mean absolute deviations of −5.0% and 10.3%, respectively.</abstract><cop>Paris</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ijrefrig.2020.04.036</doi><tpages>11</tpages></addata></record>
fulltext fulltext
identifier ISSN: 0140-7007
ispartof International journal of refrigeration, 2020-11, Vol.119, p.390-400
issn 0140-7007
1879-2081
language eng
recordid cdi_proquest_journals_2465476671
source Elsevier ScienceDirect Journals Complete
subjects Binary mixtures
Boiling
Boiling flow
Chute de pression
Convective heat transfer
Correlation
Heat flux
Heat transfer
Heat transfer coefficients
Mini-canal
Minichannel
Multiport tube
Mélange de frigorigènes zéotrope
Pressure
Pressure drop
Temperature
Transfert de chaleur
Tube multi-ports
Vapors
Zeotropic mixtures
Zeotropic refrigerant mixture
Ébullition en écoulement
title Flow boiling heat transfer of zeotropic mixture R1234yf/R32 inside a horizontal multiport tube
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-07T22%3A14%3A20IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Flow%20boiling%20heat%20transfer%20of%20zeotropic%20mixture%20R1234yf/R32%20inside%20a%20horizontal%20multiport%20tube&rft.jtitle=International%20journal%20of%20refrigeration&rft.au=Jige,%20Daisuke&rft.date=2020-11&rft.volume=119&rft.spage=390&rft.epage=400&rft.pages=390-400&rft.issn=0140-7007&rft.eissn=1879-2081&rft_id=info:doi/10.1016/j.ijrefrig.2020.04.036&rft_dat=%3Cproquest_cross%3E2465476671%3C/proquest_cross%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=2465476671&rft_id=info:pmid/&rft_els_id=S0140700720302681&rfr_iscdi=true