Pool boiling of R515A, R1234ze(E), and R1233zd(E) on a reentrant cavity surface

•Pool boiling performance of R515A, R1234ze(E), and R1233zd(E) on Turbo-ESP were presented.•A pool boiling model was modified to predict boiling performance on the Turbo-ESP surface.•The boiling performance of R515A had roughly a 14 % larger heat flux than that of R1234ze(E).•The heat flux of R1233z...

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Veröffentlicht in:International journal of heat and mass transfer 2020-11, Vol.161, p.120252, Article 120252
Hauptverfasser: Kedzierski, M.A., Lin, L.
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description •Pool boiling performance of R515A, R1234ze(E), and R1233zd(E) on Turbo-ESP were presented.•A pool boiling model was modified to predict boiling performance on the Turbo-ESP surface.•The boiling performance of R515A had roughly a 14 % larger heat flux than that of R1234ze(E).•The heat flux of R1233zd(E) was roughly 18 % larger than that for R123. This paper quantifies the pool boiling performance of R515A, R1234ze(E), and R1233zd(E) on a flattened, horizontal Turbo-ESP surface for air-conditioning. The measured boiling curve for R515A had roughly a 14 % larger heat flux than that of R1234ze(E) for heat fluxes greater than 45 kWm−2. For heat fluxes between 14 kWm−2 and 85 kWm−2, R515A and R1234ze(E) exhibited a heat flux that was 33 % and 17 % larger than that for R134a. The heat flux of R1233zd(E) was roughly 18 % larger than that for R123 between 30 kWm−2 and 87 kWm−2. A pool boiling model that was previously developed for pure and mixed refrigerants on the Turbo-ESP surface was improved by nondimensionalizing the model constants and improving their statistical significance. The model was used to show that the vapor Prandtl number and the product of the latent heat and vapor density significantly influenced the boiling heat flux.
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This paper quantifies the pool boiling performance of R515A, R1234ze(E), and R1233zd(E) on a flattened, horizontal Turbo-ESP surface for air-conditioning. The measured boiling curve for R515A had roughly a 14 % larger heat flux than that of R1234ze(E) for heat fluxes greater than 45 kWm−2. For heat fluxes between 14 kWm−2 and 85 kWm−2, R515A and R1234ze(E) exhibited a heat flux that was 33 % and 17 % larger than that for R134a. The heat flux of R1233zd(E) was roughly 18 % larger than that for R123 between 30 kWm−2 and 87 kWm−2. A pool boiling model that was previously developed for pure and mixed refrigerants on the Turbo-ESP surface was improved by nondimensionalizing the model constants and improving their statistical significance. 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This paper quantifies the pool boiling performance of R515A, R1234ze(E), and R1233zd(E) on a flattened, horizontal Turbo-ESP surface for air-conditioning. The measured boiling curve for R515A had roughly a 14 % larger heat flux than that of R1234ze(E) for heat fluxes greater than 45 kWm−2. For heat fluxes between 14 kWm−2 and 85 kWm−2, R515A and R1234ze(E) exhibited a heat flux that was 33 % and 17 % larger than that for R134a. The heat flux of R1233zd(E) was roughly 18 % larger than that for R123 between 30 kWm−2 and 87 kWm−2. A pool boiling model that was previously developed for pure and mixed refrigerants on the Turbo-ESP surface was improved by nondimensionalizing the model constants and improving their statistical significance. The model was used to show that the vapor Prandtl number and the product of the latent heat and vapor density significantly influenced the boiling heat flux.</description><subject>Air conditioning</subject><subject>Boiling</subject><subject>Enhanced heat transfer</subject><subject>Heat flux</subject><subject>Heat transfer</subject><subject>Latent heat</subject><subject>Prandtl number</subject><subject>Refrigerants</subject><subject>Structured surface</subject><subject>Vapor density</subject><issn>0017-9310</issn><issn>1879-2189</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2020</creationdate><recordtype>article</recordtype><recordid>eNqNkEtLAzEUhYMoWKv_IeCmQqcmmZlksrNIfVGoFF2HTB6aoZ3UZFpof70Z686Nm3s5nMO53A-AEUYTjDC9bSau-TSyW8sYuyDbaE2YEESSnWZJTsAAV4xnBFf8FAwQwizjOUbn4CLGppeooAOwePV-BWvvVq79gN7CZYnL6RguMcmLgxnNbsZQtvpH5wedNPQtlDAY0_ZnO6jkznV7GLfBSmUuwZmVq2iufvcQvD_M3u6fsvni8fl-Os9UzlCXMalKxEnNSiqtKZGtSE0JrYpCUqI5o1zaihmDCc6VJhxVFFVM0Tq3vKJa50NwfezdBP-1NbETjd-GNp0UpKAII0o4Sam7Y0oFH2MwVmyCW8uwFxiJHqNoxF-MoscojhhTxcuxwqRvdi65UTnTKqNdMKoT2rv_l30DNwGDLg</recordid><startdate>202011</startdate><enddate>202011</enddate><creator>Kedzierski, M.A.</creator><creator>Lin, L.</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>H8D</scope><scope>KR7</scope><scope>L7M</scope></search><sort><creationdate>202011</creationdate><title>Pool boiling of R515A, R1234ze(E), and R1233zd(E) on a reentrant cavity surface</title><author>Kedzierski, M.A. ; Lin, L.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c370t-7ac5092b756afe50f82b626844a62d9769af87ee1213cd29086087c6b3f986dd3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2020</creationdate><topic>Air conditioning</topic><topic>Boiling</topic><topic>Enhanced heat transfer</topic><topic>Heat flux</topic><topic>Heat transfer</topic><topic>Latent heat</topic><topic>Prandtl number</topic><topic>Refrigerants</topic><topic>Structured surface</topic><topic>Vapor density</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Kedzierski, M.A.</creatorcontrib><creatorcontrib>Lin, L.</creatorcontrib><collection>CrossRef</collection><collection>Mechanical &amp; Transportation Engineering 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><jtitle>International journal of heat and mass transfer</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Kedzierski, M.A.</au><au>Lin, L.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Pool boiling of R515A, R1234ze(E), and R1233zd(E) on a reentrant cavity surface</atitle><jtitle>International journal of heat and mass transfer</jtitle><date>2020-11</date><risdate>2020</risdate><volume>161</volume><spage>120252</spage><pages>120252-</pages><artnum>120252</artnum><issn>0017-9310</issn><eissn>1879-2189</eissn><abstract>•Pool boiling performance of R515A, R1234ze(E), and R1233zd(E) on Turbo-ESP were presented.•A pool boiling model was modified to predict boiling performance on the Turbo-ESP surface.•The boiling performance of R515A had roughly a 14 % larger heat flux than that of R1234ze(E).•The heat flux of R1233zd(E) was roughly 18 % larger than that for R123. This paper quantifies the pool boiling performance of R515A, R1234ze(E), and R1233zd(E) on a flattened, horizontal Turbo-ESP surface for air-conditioning. The measured boiling curve for R515A had roughly a 14 % larger heat flux than that of R1234ze(E) for heat fluxes greater than 45 kWm−2. For heat fluxes between 14 kWm−2 and 85 kWm−2, R515A and R1234ze(E) exhibited a heat flux that was 33 % and 17 % larger than that for R134a. The heat flux of R1233zd(E) was roughly 18 % larger than that for R123 between 30 kWm−2 and 87 kWm−2. A pool boiling model that was previously developed for pure and mixed refrigerants on the Turbo-ESP surface was improved by nondimensionalizing the model constants and improving their statistical significance. The model was used to show that the vapor Prandtl number and the product of the latent heat and vapor density significantly influenced the boiling heat flux.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ijheatmasstransfer.2020.120252</doi></addata></record>
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subjects Air conditioning
Boiling
Enhanced heat transfer
Heat flux
Heat transfer
Latent heat
Prandtl number
Refrigerants
Structured surface
Vapor density
title Pool boiling of R515A, R1234ze(E), and R1233zd(E) on a reentrant cavity surface
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