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Description of the real gas isentropic changes for an ammonia-water vapor mixture

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dc.contributor.author Kouremenos, DA en
dc.contributor.author Kakatsios, XK en
dc.contributor.author Floratos, OE en
dc.date.accessioned 2014-03-01T01:11:52Z
dc.date.available 2014-03-01T01:11:52Z
dc.date.issued 1996 en
dc.identifier.issn 0001-5970 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/11835
dc.subject Binary Mixture en
dc.subject Heat Pump en
dc.subject Water Vapor en
dc.subject.classification Mechanics en
dc.subject.other Ammonia en
dc.subject.other Computer software en
dc.subject.other Entropy en
dc.subject.other Equations of state en
dc.subject.other Gases en
dc.subject.other Gibbs free energy en
dc.subject.other Mixtures en
dc.subject.other Numerical analysis en
dc.subject.other Pressure effects en
dc.subject.other Thermal effects en
dc.subject.other Thermal expansion en
dc.subject.other Vapors en
dc.subject.other Ammonia water vapor mixture en
dc.subject.other Computer program ISENEXPR en
dc.subject.other Isentropic expansion en
dc.subject.other Thermodynamic changes en
dc.subject.other Thermodynamic relation en
dc.subject.other Thermodynamics en
dc.title Description of the real gas isentropic changes for an ammonia-water vapor mixture en
heal.type journalArticle en
heal.identifier.primary 10.1007/BF01171420 en
heal.identifier.secondary http://dx.doi.org/10.1007/BF01171420 en
heal.language English en
heal.publicationDate 1996 en
heal.abstract The NH3-H2O binary mixture is used extensively in industrial refrigeration or heat-pump applications while it is a candidate for future units working with resorption-compression [1]. In this paper, the thermodynamic changes of an ammonia-water mixture in the vapor phase, along an isentropic expansion, have been calculated numerically for a starting point with a temperature of 800 degrees C and initial pressures of 20, 30, 40, and 50 bar. For this purpose, a special computer program, ISENEXPR, has been developed. The thermodynamic relations used were obtained in terms of the Gibbs free energy equation for the gas phase of pure components [1], [3], [6] and the entropy was held constant with an accuracy better than 0.000001 kJ/kgK. The runs performed for isentropic expansions showed a dependence of the isentropic on the both exponents initial pressure and NH3 mass fraction xi, while the other properties depend on varying degrees upon xi. Results are given in the form of diagrams, describing the isentropic change of the NH3-H2O gas phase mixture. en
heal.publisher SPRINGER-VERLAG WIEN en
heal.journalName Acta Mechanica en
dc.identifier.doi 10.1007/BF01171420 en
dc.identifier.isi ISI:A1996UV15500005 en
dc.identifier.volume 116 en
dc.identifier.issue 1-4 en
dc.identifier.spage 61 en
dc.identifier.epage 73 en


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