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dc.contributor.authorVelasco Maíllo, Santiago 
dc.contributor.authorWhite Sánchez, Juan Antonio 
dc.date.accessioned2019-09-06T07:47:21Z
dc.date.available2019-09-06T07:47:21Z
dc.date.issued2019-08
dc.identifier.citationEnergies 2019, 12, 3266; doi:10.3390/en12173266es_ES
dc.identifier.urihttp://hdl.handle.net/10366/139836
dc.description.abstract[EN]Recently, we proposed an approximate expression for the liquid–vapor saturation curves of pure fluids in a temperature–entropy diagram that requires the use of parameters related to the molar heat capacity along the vapor branch of the saturation curve. In the present work, we establish a connection between these parameters and the ideal-gas isobaric molar heat capacity. The resulting new approximation yields good results for most working fluids in Organic Rankine Cycles, improving the previous approximation for very dry fluids. The ideal-gas isobaric molar heat capacity can be obtained from most Thermophysical Properties databases for a very large number of substances for which the present approximation scheme can be applied.es_ES
dc.description.sponsorshipJunta de. Castilla y leónes_ES
dc.format.mimetypeapplication/pdf
dc.language.isoenges_ES
dc.publisherMDPIes_ES
dc.rightsAttribution 4.0 Internacional*
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/*
dc.subjectORC working fluidses_ES
dc.subjectTemperature–entropy saturation curvees_ES
dc.subjectSaturation propertieses_ES
dc.subjectWet and dry fluidses_ES
dc.subjectIdeal-gas heat capacityes_ES
dc.titleApproximating the Temperature–Entropy Saturation Curve of ORC Working Fluids From the Ideal Gas Isobaric Heat Capacityes_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.subject.unesco2213 Termodinámicaes_ES
dc.identifier.doi10.3390/en12173266
dc.relation.projectIDSA017P17.es_ES
dc.rights.accessRightsinfo:eu-repo/semantics/openAccesses_ES


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