High-pressure fluid phase equilibria: experimental methods and systems investigated (1994–1999)

M Christov, R Dohrn - Fluid Phase Equilibria, 2002 - Elsevier
As a continuation of an earlier review, a compilation of systems for which high-pressure
phase equilibrium data have been published between 1994 and 1999 is given. Vapor–liquid …

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

JN Jaubert, F Mutelet - Fluid Phase Equilibria, 2004 - Elsevier
A group contribution method allowing the estimation of the temperature dependent binary
interaction parameters (kij (T)) for the widely used Peng–Robinson equation of state (EOS) …

Benchmark database containing binary-system-high-quality-certified data for cross-comparing thermodynamic models and assessing their accuracy

JN Jaubert, Y Le Guennec… - Industrial & …, 2020 - ACS Publications
In the last two centuries, equations of state (EoSs) have become a key tool for the correlation
and prediction of thermodynamic properties of fluids. They not only can be applied to pure …

Carbon dioxide-induced melting point depression of biodegradable semicrystalline polymers

Z Lian, SA Epstein, CW Blenk, AD Shine - The Journal of supercritical fluids, 2006 - Elsevier
The melting point depression of semicrystalline polymers exposed to a compressed fluid
allows certain biodegradable polymers to be processed in the molten state using carbon …

Wax phase equilibria: developing a thermodynamic model using a systematic approach

HY Ji, B Tohidi, A Danesh, AC Todd - Fluid Phase Equilibria, 2004 - Elsevier
Reservoir hydrocarbon fluids contain heavy paraffins that may form solid phases of wax at
low temperatures. Problems associated with wax formation and deposition are a major …

Solubilities of solid n‐alkanes in methane: Data analysis and models assessment

M Campestrini, P Stringari - AIChE Journal, 2018 - Wiley Online Library
This article reviews the results of experiments underway since 1950 studying the solid
solubility of n‐alkanes (from ethane up to n‐triacontane) in methane and the factors …

Modeling the cloud curves and the solubility of gases in amorphous and semicrystalline polyethylene with the SAFT-VR approach and Flory theory of crystallization

P Paricaud, A Galindo, G Jackson - Industrial & engineering …, 2004 - ACS Publications
The statistical associating fluid theory for potentials of variable range SAFT-VR [Gil-Villegas,
A.; et al. J. Chem. Phys. 1997, 106, 4168] is used to examine the fluid-phase behavior of …

Prediction of dew points and liquid dropouts of gas condensate mixtures

N Novak, V Louli, S Skouras, E Voutsas - Fluid Phase Equilibria, 2018 - Elsevier
Thermodynamic modeling of reservoir fluids behavior is of great importance for the oil and
gas industry. For design and safe operation purposes, it is necessary to have an accurate …

Vapor–liquid equilibria calculation for asymmetric systems using Patel–Teja equation of state with a new mixing rule

J Gao, LD Li, ZY Zhu, SG Ru - Fluid Phase Equilibria, 2004 - Elsevier
The cubic equation of state (EoS) of Patel and Teja with a new mixing rule, which is based
on the assumption that the excess Helmholtz energy at infinite pressure is zero, was …

Prediction of solid–fluid phase diagrams of light gases–heavy paraffin systems up to 200 MPa using an equation of state–GE model

J Pauly, JL Daridon, JAP Coutinho, N Lindeloff… - Fluid Phase …, 2000 - Elsevier
This paper presents a procedure for the simultaneous prediction of fluid–fluid and solid–fluid
equilibria of light gases–heavy hydrocarbons systems under pressure. The fluid phases …