Vapour-liquid equilibria in the systems carbon tetrachloride-toluene and n-pentane-benzene.

dc.contributor.author	Wang, Jack Li-Hsien.
dc.date.accessioned	2009-04-17T15:56:17Z
dc.date.available	2009-04-17T15:56:17Z
dc.date.created	1971
dc.date.issued	1971
dc.degree.level	Masters
dc.degree.name	M.A.Sc.
dc.description.abstract	A modified recirculation Dvorak and Boublik still was used in the equilibrium determination. The vapour-liquid equilibria in the systems carbon tetrachloride-toluene were studied at five isothermal conditions. Liquid activity coefficients were evaluated. The values of gamma were close to unity. The vapour-liquid equilibria in the systems n-pentane-benzene were studied at four isothermal conditions. Liquid activity coefficients were also evaluated. Liquid-vapour equilibria at isobaric conditions were correlated using the data of heat of mixing at 25°C and the experimental ln gamma values obtained from this work. The In gamma values were correlated by means of the three-constant Redlich-Kister equation for the binary systems.
dc.format.extent	96 p.
dc.identifier.citation	Source: Masters Abstracts International, Volume: 45-06, page: 3215.
dc.identifier.uri	http://hdl.handle.net/10393/10476
dc.identifier.uri	http://dx.doi.org/10.20381/ruor-16844
dc.publisher	University of Ottawa (Canada)
dc.subject.classification	Engineering, Chemical.
dc.title	Vapour-liquid equilibria in the systems carbon tetrachloride-toluene and n-pentane-benzene.
dc.type	Thesis

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