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dc.contributor.authorChiou, C. B.en_US
dc.contributor.authorLu, D. C.en_US
dc.contributor.authorChen, C. C.en_US
dc.contributor.authorChu, C. M.en_US
dc.date.accessioned2014-12-08T15:11:52Z-
dc.date.available2014-12-08T15:11:52Z-
dc.date.issued2011-04-01en_US
dc.identifier.issn1359-4311en_US
dc.identifier.urihttp://dx.doi.org/10.1016/j.applthermaleng.2010.10.031en_US
dc.identifier.urihttp://hdl.handle.net/11536/9108-
dc.description.abstractThe evaporation heat transfer coefficient of pure refrigerants R-22 and R-124 in micro-fin tubes were measured at the reduced pressure of 0.15, the mass flux from 100 to 400 kg/m(2) s, the flow quality from 0.1 to 0.9, and the heat flux from 5 to 20 kW/m(2). The evaporation heat transfer coefficient of pure refrigerant in micro-fin tube is 1.5-3.0 times higher than that of smooth tube. In this article, the single phase forced convection heat transfer coefficient of micro-fin tube is introduced to predict the evaporation heat transfer coefficient of pure refrigerant in micro-fin tubes. The present correlations provide reasonable agreement with the experimental data. The prediction values mostly fall within +/- 30%. (C) 2010 Elsevier Ltd. All rights reserved.en_US
dc.language.isoen_USen_US
dc.subjectForced convective boilingen_US
dc.subjectEvaporationen_US
dc.subjectPure refrigeranten_US
dc.subjectMicro-finen_US
dc.subjectCorrelationen_US
dc.titleHeat transfer correlations of forced convective boiling for pure refrigerants in micro-fin tubesen_US
dc.typeArticleen_US
dc.identifier.doi10.1016/j.applthermaleng.2010.10.031en_US
dc.identifier.journalAPPLIED THERMAL ENGINEERINGen_US
dc.citation.volume31en_US
dc.citation.issue5en_US
dc.citation.spage820en_US
dc.citation.epage826en_US
dc.contributor.department機械工程學系zh_TW
dc.contributor.departmentDepartment of Mechanical Engineeringen_US
dc.identifier.wosnumberWOS:000287894300030-
dc.citation.woscount1-
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