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Vapor-liquid equilibrium relations of binary systems propane-n-octane and butane-n-octane

Webster B. Kay, +2 more
- 01 Jul 1974 - 
- Vol. 19, Iss: 3, pp 275-280
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This article is published in Journal of Chemical & Engineering Data.The article was published on 1974-07-01. It has received 44 citations till now. The article focuses on the topics: Equilibrium thermodynamics & Thermodynamic equilibrium.

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VLE predictions with the Peng–Robinson equation of state and temperature dependent kij calculated through a group contribution method

TL;DR: In this paper, a group contribution method for the estimation of the temperature dependent binary interaction parameters (kij(T)) for the widely used Peng-Robinson equation of state (EOS) is proposed.
Journal ArticleDOI

Volume expansion in relation to the gas–antisolvent process

TL;DR: In this article, an alternative definition of liquid-phase volume expansion is proposed for the selection of the optimum pressure for a gas-antisolvent (GAS) process, based on the Peng-Robinson equation of state.
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Global Fluid Phase Equilibria and Critical Phenomena of Selected Mixtures Using the Crossover Soft-SAFT Equation

TL;DR: The new equation of state to mixtures is proved to be a powerful tool to study the global phase behavior of complex systems, as well as other thermodynamic properties of very challenging mixtures.
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Universal Mixing Rule for Cubic Equations of State Applicable to Symmetric and Asymmetric Systems: Results with the Peng−Robinson Equation of State

TL;DR: A mixing rule for cubic equations of state (CEoS) applicable to all types of system asymmetries referred to hereafter as the universal mixing rule (UMR) is proposed in this article.
Journal ArticleDOI

A simplified method for calculating saturated liquid densities

TL;DR: In this article, a simplification for the Nasrifar-Moshfeghian (NM) liquid density correlation has been developed, which uses one characteristic parameter for each compound and suggests a value of zero for generalization purpose.
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