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dc.contributor.authorChiou, CBen_US
dc.contributor.authorLu, DCen_US
dc.contributor.authorWang, CCen_US
dc.date.accessioned2014-12-08T15:02:20Z-
dc.date.available2014-12-08T15:02:20Z-
dc.date.issued1996-10-01en_US
dc.identifier.issn1359-4311en_US
dc.identifier.urihttp://dx.doi.org/10.1016/1359-4311(95)00089-5en_US
dc.identifier.urihttp://hdl.handle.net/11536/1011-
dc.description.abstractBased on the two-phase separated model, a detailed one-dimensional model for binary mixtures had been proposed to study the in-tube evaporation in a horizontal tube. The present model can predict the detailed variation of the composition, temperature, heat transfer rate and pressure drop of various binary mixtures under constant heat flux, counter-flow, or parallel-flow conditions. The predicted results agree favorably with the Takamatsu et al. [Int. J. Neat Mass Transfer 36, 3555-3563 (1993)] and Jung et al. [Exp. Heat Transfer 2, 237-255 (1989)] experimental data. Also, it is found that the full evaporation of the non-azeotropic refrigerants may require a corresponding temperature higher than the saturation temperature of the less volatile component. The non-linear variation of the property plays an important role in the heat transfer and pressure drop characteristics of the refrigerant mixtures. Copyright (C) 1996 Elsevier Science Ltd.en_US
dc.language.isoen_USen_US
dc.subjectnon-azeotropic refrigerantsen_US
dc.subjectevaporationen_US
dc.subjectmodelen_US
dc.titleAnalysis of evaporation of non-azeotropic refrigerants in a horizontal tubeen_US
dc.typeArticleen_US
dc.identifier.doi10.1016/1359-4311(95)00089-5en_US
dc.identifier.journalAPPLIED THERMAL ENGINEERINGen_US
dc.citation.volume16en_US
dc.citation.issue10en_US
dc.citation.spage817en_US
dc.citation.epage827en_US
dc.contributor.department機械工程學系zh_TW
dc.contributor.departmentDepartment of Mechanical Engineeringen_US
dc.identifier.wosnumberWOS:A1996VB16500004-
dc.citation.woscount7-
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