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Vapor-liquid equilibria of carbon dioxide-hydrocarbon systems at moderately high pressure

A new vapor-liquid equilibrium apparatus was constructed to measure temperature, pressure, and phase compositions up to 8 MPa. Systems of CO(,2) with 2-methyl-1-pentene, 1-hexene, 1-heptene and m-xylene were studied at 303.15 K, 323.15 K, and 343.15 K. / A general method was proposed for equation of state construction. Two equations of State were constructed. Using critical temperature, critical pressure, critical compressibility factor and acentric factor, these equations can predict saturation properties of normal fluids. / The equations were extended to mixtures using van der Waals' one fluid theory, Lee-Kesler corresponding state approach and a virial-like approach. They had limited predictive abilities compared to cubic equations. / A correlation for third virial coefficients of nonpolar gases was developed. The correlation requires the knowledge of critical temperature, critical pressure and acentric factor and is applicable to mixtures of nonpolar gases including quantum gases. Predictions are in good agreement with reported experimental data.

Identiferoai:union.ndltd.org:LACETR/oai:collectionscanada.gc.ca:QMM.71820
Date January 1983
CreatorsOrbey, Hasan.
PublisherMcGill University
Source SetsLibrary and Archives Canada ETDs Repository / Centre d'archives des thèses électroniques de Bibliothèque et Archives Canada
LanguageEnglish
Detected LanguageEnglish
TypeElectronic Thesis or Dissertation
Formatapplication/pdf
CoverageDoctor of Philosophy (Department of Chemical Engineering.)
RightsAll items in eScholarship@McGill are protected by copyright with all rights reserved unless otherwise indicated.
Relationalephsysno: 000166623, proquestno: AAINK64476, Theses scanned by UMI/ProQuest.

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