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Some Observations Regarding the Association Kernel of SAFT-VR-Mie. Is the Molecularly Inspired Contribution Always Necessary?
José Matías Garrido, Esteban Cea-Klapp and Ilya Polishuk Industrial & Engineering Chemistry Research 57(46) 15869 (2018) https://doi.org/10.1021/acs.iecr.8b03789
Epaminondas Voutsas, Nefeli Novak, Vasiliki Louli, Georgia Pappa, Eirini Petropoulou, Christos Boukouvalas, Eleni Panteli and Stathis Skouras 57 (2018) https://doi.org/10.1002/9781119269618.ch3
Equations of State with Group Contribution Binary Interaction Parameters for Calculation of Two-Phase Envelopes for Synthetic and Real Natural Gas Mixtures with Heavy Fractions
Khashayar Nasrifar and Nejat Rahmanian Oil & Gas Sciences and Technology – Revue d’IFP Energies nouvelles 73 7 (2018) https://doi.org/10.2516/ogst/2017044
Calculation of critical points for natural gas mixtures with the GERG-2008 equation of state
Extension of the E-PPR78 equation of state to predict fluid phase equilibria of natural gases containing carbon monoxide, helium-4 and argon
Vincent Plee, Jean-Noël Jaubert, Romain Privat and Philippe Arpentinier Journal of Petroleum Science and Engineering 133 744 (2015) https://doi.org/10.1016/j.petrol.2015.03.025
A modified MMM EOS for high-pressure PVT calculations of heavy hydrocarbons
Thermodynamic and transport property models for carbon capture and sequestration (CCS) processes with emphasis on CO2 transport
Nikolaos I. Diamantonis, Georgios C. Boulougouris, Dimitrios M. Tsangaris, et al. Chemical Engineering Research and Design 91(10) 1793 (2013) https://doi.org/10.1016/j.cherd.2013.06.017
Phase behavior of sour natural gas systems using classical and statistical thermodynamic equations of states
Modeling of three-phase vapor–liquid–liquid equilibria for a natural-gas system rich in nitrogen with the SRK and PC-SAFT EoS
Daimler N. Justo-García, Fernando García-Sánchez, Néstor L. Díaz-Ramírez and Enrique Díaz-Herrera Fluid Phase Equilibria 298(1) 92 (2010) https://doi.org/10.1016/j.fluid.2010.07.012
The Calculation of the Hydrocarbon Dew Point in a Gas Pipeline