Journal ArticleDOI
High-pressure vapour-liquid equilibria in binary mixtures of carbon dioxide and benzene compounds: experimental data for mixtures with ethylbenzene, isopropylbenzene, 1,2,4-trimethylbenzene, 1,3,5-trimethylbenzene, ethenylbenzene and isopropenylbenzene, and their correlation with the generalized Bender and Skjold-Jørgensen's group contribution equation of state
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TLDR
Bamberger et al. as mentioned in this paper studied the high-pressure vapour-liquid Equilibria in binary mixtures of carbon dioxide and benzene compounds and correlated the experimental results with a generalized Bender equation of state and the GC-EOS by Skjold-Jorgensen.About:
This article is published in Fluid Phase Equilibria.The article was published on 1994-06-15. It has received 43 citations till now. The article focuses on the topics: Ethylbenzene & Equation of state.read more
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High-pressure (vapor+liquid) equilibrium in binary mixtures of (carbon dioxide+water or acetic acid) at temperatures from 313 to 353 K
TL;DR: Chao et al. as discussed by the authors used the modified Peng-Robinson equation of state and the mixing rule of Panagiotopoulos and Reid to predict the high-pressure (vapor+liquid) equilibrium of binary systems of carbon dioxide.
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High-pressure fluid-phase equilibria: Experimental methods and systems investigated (1988–1993)
Ralf Dohrn,Gerd Brunner +1 more
TL;DR: In this article, a compilation of high-pressure phase equilibrium data has been given, where the reference, the temperature and pressure range of the data, and the experimental method used for the measurements is given in 39 tables.
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Predicting the phase equilibria of CO2+hydrocarbon systems with the PPR78 model (PR EOS and kij calculated through a group contribution method)
TL;DR: In this article, a group contribution method was developed to estimate the temperature dependent binary interaction parameters (kij(T)) for the widely used Peng-Robinson equation of state (EOS), which was called PPR78 (predictive 1978, Peng Robinson EOS).
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Phase equilibria in mixtures of fatty oils and derivatives with near critical fluids using the GC-EOS model
TL;DR: In this paper, the Group Contribution Equation of State (GC-EOS) was applied to model high-pressure phase equilibria in mixtures of fatty oils and acid alkyl esters with supercritical fluids.
References
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Journal ArticleDOI
Gas solubility calculations. II. Application of a new group-contribution equation of state
TL;DR: In this article, the generalized van der Waals partition function was used to predict high-pressure vapor-liquid equilibria and the Henry's constants in mixed solvents.
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Group contribution equation of state (GC-EOS): a predictive method for phase equilibrium computations over wide ranges of temperature and pressures up to 30 MPa
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Equilibrium phase compositions, phase densities, and interfacial tensions for CO sub 2 + hydrocarbon systems; CO sub 2 + n-butane + n-decane
TL;DR: In this paper, the ternary system CO{sub 2} + n-butane + ndecane at 160°degrees F was measured on a mixture of constant overall molar composition with phase densities and interfacial tensions.
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Statistical thermodynamics of mixtures. A new version for the theory of conformal solution
G. Ali Mansoori,Thomas W. Leland +1 more
TL;DR: In this article, a new method for the calculation of thermodynamic properties of simple fluid mixtures constitutes an extension of the approach defined earlier as the “van der Waals” conformal solution theory, made possible by advances in the analytical representation of the thermodynamics properties of a mixture of hard spheres which permit the properties to be calculated directly, without the use of a reference fluid.