Vapour-liquid equilibria for argon-methane system.

dc.contributor.author	Maitra, Kalyan Kumar.
dc.date.accessioned	2009-04-17T16:02:08Z
dc.date.available	2009-04-17T16:02:08Z
dc.date.created	1966
dc.date.issued	1966
dc.degree.level	Masters
dc.degree.name	M.Sc.
dc.description.abstract	An apparatus for the determination of vapour-liquid equilibrium data at low temperatures was built and employed. The vapour-liquid equilibrium data for the argon-methane system were obtained at three isothermal conditions, namely, at 122.66, 132.52 and 143.16°K. The experimental equilibrium data were correlated with two constant Redlich-Kister equations. The liquid phase fugacity coefficients for pure methane were calculated from the experimental data. An attempt was made using the theory of interaction and cavitation to predict Henry's law constants.
dc.format.extent	94 p.
dc.identifier.citation	Source: Masters Abstracts International, Volume: 45-06, page: 3211.
dc.identifier.uri	http://hdl.handle.net/10393/10795
dc.identifier.uri	http://dx.doi.org/10.20381/ruor-17012
dc.publisher	University of Ottawa (Canada)
dc.subject.classification	Engineering, Chemical.
dc.title	Vapour-liquid equilibria for argon-methane system.
dc.type	Thesis

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