The three isentropic exponents of wet steam

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dc.contributor.author Paradissiadis, I en
dc.date.accessioned 2014-03-01T01:07:00Z
dc.date.available 2014-03-01T01:07:00Z
dc.date.issued 1987 en
dc.identifier.issn 0015-7899 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/9729
dc.subject.classification Engineering, Multidisciplinary en
dc.subject.classification Engineering, Mechanical en
dc.subject.other GASES en
dc.subject.other MIXTURES en
dc.subject.other VAPORS en
dc.subject.other WATER en
dc.subject.other DRY STEAM en
dc.subject.other IDEAL GAS en
dc.subject.other ISENTROPIC EXPONENTS en
dc.subject.other REAL GASES en
dc.subject.other WET STEAM en
dc.subject.other STEAM en
dc.title The three isentropic exponents of wet steam en
heal.type journalArticle en
heal.identifier.primary 10.1007/BF02560949 en
heal.identifier.secondary http://dx.doi.org/10.1007/BF02560949 en
heal.language English en
heal.publicationDate 1987 en
heal.abstract Real gas isentropic changes may be described using the three well known ideal gas relations, pvk =const, p(1-k)Tk=const and Tvk-1=const, where exponent k has for each equation a different value kp, ν, kp, T and kT, ν respectively. In this paper the three isentropic exponents theory for real gases is extended to the two phase region. As an application the numerical values of the three exponents are calculated for wet steam. © 1987 VDI Verlag GmbH. en
heal.publisher Springer-Verlag en
heal.journalName Forschung im Ingenieurwesen en
dc.identifier.doi 10.1007/BF02560949 en
dc.identifier.isi ISI:A1987K733800006 en
dc.identifier.volume 53 en
dc.identifier.issue 5 en
dc.identifier.spage 159 en
dc.identifier.epage 161 en

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