The three isentropic exponents of wet steam

Paradissiadis, I

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