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dc.contributor.authorKuo, CSen_US
dc.contributor.authorWang, CCen_US
dc.date.accessioned2019-04-02T05:58:30Z-
dc.date.available2019-04-02T05:58:30Z-
dc.date.issued1996-08-01en_US
dc.identifier.issn1359-4311en_US
dc.identifier.urihttp://dx.doi.org/10.1016/1359-4311(95)00076-3en_US
dc.identifier.urihttp://hdl.handle.net/11536/149229-
dc.description.abstractThe two-phase heat transfer coefficient and pressure drop characteristics of refrigerant R22 and R407C (a mixture of R32/R125/R134a, 23%/25%/52%) in a micro-fin tube with nominal diameter 9.52 mm were presented in this study. Experimental data were taken at an evaporation pressure of 600 kPa. The mass flux was between 100 and 300 kg/m(2) . s and the heat fluxes were between 6 and 14 kW/m(2). Experimental data were presented in the form of length-averaged heat transfer coefficients and frictional pressure gradients. The effect of heat flux and mass flux on the heat transfer coefficients were also reported in the present investigation. It is found that the heat transfer coefficients for R407C are considerably lower than R22 (50 similar to 80% less), and the pressure drop of R407C is 30 similar to 50% lower as compared to R22. Copyright (C) 1996 Elsevier Science Ltden_US
dc.language.isoen_USen_US
dc.subjectR407Cen_US
dc.subjectheat transfer coefficientsen_US
dc.subjectevaporatoren_US
dc.titleHorizontal flow boiling of R22 and R407C in a 9.52mm micro-fin tubeen_US
dc.typeArticleen_US
dc.identifier.doi10.1016/1359-4311(95)00076-3en_US
dc.identifier.journalAPPLIED THERMAL ENGINEERINGen_US
dc.citation.volume16en_US
dc.citation.spage719en_US
dc.citation.epage731en_US
dc.contributor.department機械工程學系zh_TW
dc.contributor.departmentDepartment of Mechanical Engineeringen_US
dc.identifier.wosnumberWOS:A1996UU98400007en_US
dc.citation.woscount32en_US
Appears in Collections:Articles