Journal ArticleDOI
Phase Equilibria in Hydrocarbon Systems. Volumetric and Phase Behavior of the Methane-n-Heptane System
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This article is published in Industrial & Engineering Chemistry Chemical & Engineering Data Series.The article was published on 1956-01-01. It has received 85 citations till now. The article focuses on the topics: Heptane & Phase (matter).read more
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A generalized thermodynamic correlation based on three‐parameter corresponding states
Byung Ik Lee,Michael G. Kesler +1 more
TL;DR: In this paper, the volumetric and thermodynamic functions correlated by Pitzer and co-workers were analyzed with improved accuracy by a modified BWR equation of state, which provides a smooth transition between the original tables of Pitzer et al. and more recent extensions to lower temperatures.
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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.
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Prediction of vapor-liquid equilibrium with the LCVM model : a linear combination of the Vidal and Michelsen mixing rules coupled with the original UNIFAC and the t-mPR equation of state
Christos Boukouvalas,Nikolaos Spiliotis,Philippos Coutsikos,Nikolaos Tzouvaras,Dimitrios P. Tassios +4 more
TL;DR: Boukouvalas et al. as discussed by the authors developed a new mixing rule, a linear combination of the Vidal and Michelsen rules, for the attractive term parameter in cubic equations of state (EoS) has been developed, coupled with a translated and modified Peng-Robinson EoS and the original UNIFAC, which leads to the LCVM model which provides successful prediction of vapor-liquid equilibria of nonpolar and polar systems at low and high pressures.
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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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A simple correlation to evaluate binary interaction parameters of the Peng-Robinson equation of state: binary light hydrocarbon systems
TL;DR: Gao et al. as mentioned in this paper proposed a simple correlation to evaluate binary interaction parameters of the Peng-Robinson equation of state for binary light hydrocarbons mixtures, as a function only of critical temperature and compressibility factor.