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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