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Evaporation heat transfer characteristics of R-245fa in a shell and plate heat exchanger for very-high-temperature heat pumps

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dc.contributor.authorSong, Kang Sub-
dc.contributor.authorYun, Sungho-
dc.contributor.authorLee, DongChan-
dc.contributor.authorKim, Kibong-
dc.contributor.authorKim, Yongchan-
dc.date.accessioned2021-08-31T04:42:37Z-
dc.date.available2021-08-31T04:42:37Z-
dc.date.created2021-06-19-
dc.date.issued2020-04-
dc.identifier.issn0017-9310-
dc.identifier.urihttps://scholar.korea.ac.kr/handle/2021.sw.korea/56734-
dc.description.abstractA shell and plate heat exchanger (SPHE) has been introduced for use in very-high-temperature heat pumps (VHTHPs). However, studies on the evaporation heat transfer characteristics of refrigerants in SPHEs for use in VHTHPs are very limited. In this study, the evaporation heat transfer characteristics of R-245fa in the SPHE are measured and analyzed by varying the saturation temperature, mass flux, heat flux, mean vapor quality, and fluid direction. Experiments are conducted under high temperatures of 60-80 degrees C for VHTHP applications. The evaporation heat transfer coefficient increases as the mass flux and mean vapor quality increase, whereas it decreases as the heat flux increases. The two-phase frictional pressure drop increases as the mass flux and mean vapor quality increase. The heat transfer performance of the upward flow in the SPHE is better than that of the downward flow. In addition, empirical correlations of the Nusselt number and two-phase friction factor of R-245fa in the SPHE are derived. (C) 2020 Elsevier Ltd. All rights reserved.-
dc.languageEnglish-
dc.language.isoen-
dc.publisherPERGAMON-ELSEVIER SCIENCE LTD-
dc.subjectPRESSURE-DROP-
dc.subjectHYDRAULIC PERFORMANCE-
dc.subjectREFRIGERANT R-134A-
dc.subjectFLOW PATTERN-
dc.subjectCONDENSATION-
dc.subjectR245FA-
dc.subjectR-410A-
dc.subjectR410A-
dc.titleEvaporation heat transfer characteristics of R-245fa in a shell and plate heat exchanger for very-high-temperature heat pumps-
dc.typeArticle-
dc.contributor.affiliatedAuthorKim, Yongchan-
dc.identifier.doi10.1016/j.ijheatmasstransfer.2020.119408-
dc.identifier.scopusid2-s2.0-85078663097-
dc.identifier.wosid000521512400037-
dc.identifier.bibliographicCitationINTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, v.151-
dc.relation.isPartOfINTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER-
dc.citation.titleINTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER-
dc.citation.volume151-
dc.type.rimsART-
dc.type.docTypeArticle-
dc.description.journalClass1-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.relation.journalResearchAreaThermodynamics-
dc.relation.journalResearchAreaEngineering-
dc.relation.journalResearchAreaMechanics-
dc.relation.journalWebOfScienceCategoryThermodynamics-
dc.relation.journalWebOfScienceCategoryEngineering, Mechanical-
dc.relation.journalWebOfScienceCategoryMechanics-
dc.subject.keywordPlusPRESSURE-DROP-
dc.subject.keywordPlusHYDRAULIC PERFORMANCE-
dc.subject.keywordPlusREFRIGERANT R-134A-
dc.subject.keywordPlusFLOW PATTERN-
dc.subject.keywordPlusCONDENSATION-
dc.subject.keywordPlusR245FA-
dc.subject.keywordPlusR-410A-
dc.subject.keywordPlusR410A-
dc.subject.keywordAuthorVery-high-temperature heat pump-
dc.subject.keywordAuthorShell and plate heat exchanger-
dc.subject.keywordAuthorR-245fa-
dc.subject.keywordAuthorEvaporation heat transfer-
dc.subject.keywordAuthorTwo-phase pressure drop-
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