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dc.contributor.authorWang, Chi-Chuanen_US
dc.date.accessioned2014-12-08T15:29:25Z-
dc.date.available2014-12-08T15:29:25Z-
dc.date.issued2013-03-01en_US
dc.identifier.issn1364-0321en_US
dc.identifier.urihttp://dx.doi.org/10.1016/j.rser.2012.11.049en_US
dc.identifier.urihttp://hdl.handle.net/11536/21193-
dc.description.abstractThis study provides an overview about the two-phase heat transfer performance for HFO-1234yf which is made to substitute R-134a. Based on the limited information, it is found that the nucleate boiling heat transfer coefficient (HTC) and convective boiling HTC for HFO-1234yf are comparable to R-134a provided q < 200 kW m(-2). The critical heat flux for HFO-1234yf is about 20-40% lower than that of R-134a. For external condensation, the only database shows that the HTC between HFO-1234yf and R-134a is also negligible. However, it is found that the major thermophysical properties influencing condensing HTC suggest a lower HTC of HFO-1234yf For in-tube condensation, it is found that the condensation HTCs for HFO-1234yf are inferior to those of R-134a, and the difference increases with the rise of vapor quality. The predictive correlations applicable for pressured drop for HFO-1234yf are not consistent, it is probably attributed to the difference in tube diameter in the publications. (C) 2012 Elsevier Ltd. All rights reserved.en_US
dc.language.isoen_USen_US
dc.subjectHFO-1234yfen_US
dc.subjectR-134aen_US
dc.subjectTwo-phase heat transfer coefficienten_US
dc.subjectPressure dropen_US
dc.subjectFlow patternen_US
dc.titleAn overview for the heat transfer performance of HFO-1234yfen_US
dc.typeReviewen_US
dc.identifier.doi10.1016/j.rser.2012.11.049en_US
dc.identifier.journalRENEWABLE & SUSTAINABLE ENERGY REVIEWSen_US
dc.citation.volume19en_US
dc.citation.issueen_US
dc.citation.spage444en_US
dc.citation.epage453en_US
dc.contributor.department機械工程學系zh_TW
dc.contributor.departmentDepartment of Mechanical Engineeringen_US
dc.identifier.wosnumberWOS:000314905000033-
dc.citation.woscount5-
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