Prediction of hydrocarbon densities at extreme conditions using volume-translated SRK and PR equations of state fit to high temperature, high pressure PVT data
Mark McHugh
Fluid Phase Equilibria, 2012
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Experimental measurements and equation of state modeling of liquid densities for long-chain n-alkanes at pressures to 265MPa and temperatures to 523K
Babatunde Bamgbade, Mark McHugh
Fluid Phase Equilibria, 2011
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Modeling VLE of H 2 + Hydrocarbon Mixtures Using a Group Contribution SAFT with a k ij Correlation Method Based on London’s Theory
Pascal TOBALY
Energy & Fuels, 2009
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Equation of state modeling of high-pressure, high-temperature hydrocarbon density data
Mark McHugh
The Journal of Supercritical Fluids, 2010
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Liquid Density and Critical Properties of Hydrocarbons Estimated from Molecular Structure
Roumiana P Stateva, Georgi Cholakov
Journal of Chemical & Engineering Data, 2002
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Modeling Phase Equilibria of Asymmetric Mixtures Using a Group-Contribution SAFT (GC-SAFT) with a k ij Correlation Method Based on Londonʼs Theory. 2. Application to Binary Mixtures Containing Aromatic Hydrocarbons, n Alkanes, CO 2 , N 2 , and H 2 S
Pascal TOBALY
Industrial & Engineering Chemistry Research, 2008
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Implementation of the critical point-based revised PC-SAFT for modelling thermodynamic properties of aromatic and haloaromatic compounds
Ilya Polishuk
The Journal of Supercritical Fluids, 2015
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Liquid Densities of Xylene Isomers and 2-Methylnaphthalene at Temperatures to 523 K and Pressures to 265 MPa: Experimental Determination and Equation of State Modeling
Babatunde Bamgbade, Mark McHugh
Industrial & Engineering Chemistry Research, 2013
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New Procedure for Enhancing the Transferability of Statistical Associating Fluid Theory (SAFT) Molecular Parameters: The Role of Derivative Properties
Felix Llovell
Industrial & Engineering Chemistry Research
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An improved group contribution method for PC-SAFT applied to branched alkanes: Data analysis and parameterization
Whestside Babe
Fluid Phase Equilibria, 2018
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Use of PC-SAFT for Global Phase Diagrams in Binary Mixtures Relevant to Natural Gases. 3. Alkane + Non-Hydrocarbons
Kenneth Hall
Industrial & Engineering Chemistry Research, 2007
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Modeling Phase Equilibria of Asymmetric Mixtures Using a Group-Contribution SAFT (GC-SAFT) with a k ij Correlation Method Based on London’s Theory. 1. Application to CO 2 + n Alkane, Methane + n Alkane, and Ethane + n Alkane Systems
Pascal TOBALY
Industrial & Engineering Chemistry Research, 2008
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Liquid Density of Pure Alkanes and Halogenated Alkanes in a Corresponding States Format
Sergio Bobbo
1998
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Liquid Density of Alkanes and Halogenated Alkanes Mixtures in a Corresponding States Format
M. Grigiante
1998
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Predicting the High-Pressure Phase Equilibria of Methane + n -Hexane Using the SAFT-VR Approach
Clare McCabe, Alejandro Gil-villegas
The Journal of Physical Chemistry B, 1998
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High-Pressure Soybean Oil Biodiesel Density: Experimental Measurements, Correlation by Tait Equation, and Perturbed Chain SAFT (PC-SAFT) Modeling
rachid aitbelale
Journal of Chemical & Engineering Data, 2019
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GC-PPC-SAFT Equation of State for VLE and LLE of Hydrocarbons and Oxygenated Compounds. Sensitivity Analysis
Jean-Charles de Hemptinne
Industrial & Engineering Chemistry Research, 2013
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Modelling of pure components high pressures densities using CK-SAFT and PC-SAFT equations
Journal of the Serbian Chemical Society
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Thermodynamic modeling for petroleum fluids I. Equation of state and group contribution for the estimation of thermodynamic parameters of heavy hydrocarbons
Laurent AVAULLEE
Fluid Phase Equilibria, 1997
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Implementation of PC-SAFT and SAFT+Cubic for modeling thermodynamic properties of haloalkanes. I. 11 halomethanes
Rostislav Potievsky, Erez Assor, Ilya Polishuk
Fluid Phase Equilibria, 2012
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Prediction of molecular weight and density of n-alkanes (C 6–C 44
Hilal Yucel
Analytica Chimica Acta, 2005
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Conventional and machine learning improved prediction of hydrocarbon density using volumetranslation at high-pressure high-temperature conditions
Preye D . Orodu
Energy Sources Part A: Recovery, Utilization, and Environmental Effects, 2021
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Density calculation of liquid organic compounds using a simple equation of state up to high pressures
Seyed Soheil Mansouri
Journal of Molecular Liquids, 2011
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Generalization of SAFT+Cubic equation of state for predicting and correlating thermodynamic properties of heavy organic substances
Ilya Polishuk
The Journal of Supercritical Fluids, 2012
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Critical parameters optimized for accurate phase behavior modeling for heavy n-alkanes up to C100 using the Peng–Robinson equation of state
Ashutosh K U M A R Pandey
Fluid Phase Equilibria, 2012
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