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Accueil Tous les numéros Oil & Gas Science and Technology - Rev. IFP, 55 5 (2000) 511-522 Article's citations

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Examining the Prediction of Vapor-Liquid Equilibria through Comparative Analysis: Deep Learning versus Classical Cubic and Associating Fluid Theory Approaches

Muhammad Naveed Khan, Pramod Warrier, Babar Zaman and Cornelius Peters
Journal of the Turkish Chemical Society Section B: Chemical Engineering 8 (1) 11 (2025)
https://doi.org/10.58692/jotcsb.1545110

Wellbore and Reservoir Thermodynamic Appraisal in Acid Gas Injection for EOR Operations

Anna Samnioti, Eirini Maria Kanakaki, Evangelia Koffa, et al.
Energies 16 (5) 2392 (2023)
https://doi.org/10.3390/en16052392

The role of cross-association between carbon dioxide and hydrogen sulfide using the SAFT-VR Mie equation of state

André F. Gonçalves, Marcelo Castier and Luís F.M. Franco
Fluid Phase Equilibria 559 113493 (2022)
https://doi.org/10.1016/j.fluid.2022.113493

Peng-Robinson equation of state: 40 years through cubics

Juan Sebastian Lopez-Echeverry, Simon Reif-Acherman and Eduard Araujo-Lopez
Fluid Phase Equilibria 447 39 (2017)
https://doi.org/10.1016/j.fluid.2017.05.007

Managing Experimental-Data Shortfalls for Fair Screening at Concept Selection: Case Study To Estimate How Acid-Gas Injection Affects Asphaltene-Precipitation Behavior

Hideharu Yonebayashi, Katsumo Takabayashi, Ryo Iizuka and Slavko Tosic
Oil and Gas Facilities 5 (05) (2016)
https://doi.org/10.2118/170585-PA

Modeling phase equilibria for acid gas mixtures using the CPA equation of state. Part IV. Applications to mixtures of CO2 with alkanes

Ioannis Tsivintzelis, Shahid Ali and Georgios M. Kontogeorgis
Fluid Phase Equilibria 397 1 (2015)
https://doi.org/10.1016/j.fluid.2015.03.034

A modified Patel–Teja cubic equation of state: Part I – Generalized model for gases and hydrocarbons

Luis A. Forero G. and Jorge A. Velásquez J.
Fluid Phase Equilibria 342 8 (2013)
https://doi.org/10.1016/j.fluid.2012.12.032

Prediction of volumetric properties of fluids for oil and gas applications

Laura A. Pellegrini, Stefania Moioli, Simone Gamba and Paola Ceragioli
Fluid Phase Equilibria 317 52 (2012)
https://doi.org/10.1016/j.fluid.2011.12.022

Modeling phase equilibria for acid gas mixtures using the CPA equation of state. I. Mixtures with H2S

Ioannis Tsivintzelis, Georgios M. Kontogeorgis, Michael L. Michelsen and Erling H. Stenby
AIChE Journal 56 (11) 2965 (2010)
https://doi.org/10.1002/aic.12207

Hydrogen Sulfide Viscosity Modeling

Kurt A. G. Schmidt, Sergio E. Quiñones-Cisneros, John J. Carroll and Bjørn Kvamme
Energy & Fuels 22 (5) 3424 (2008)
https://doi.org/10.1021/ef700701h

Modeling Phase Equilibria of Asymmetric Mixtures Using a Group-Contribution SAFT (GC-SAFT) with a kij Correlation Method Based on Londonʼs Theory. 2. Application to Binary Mixtures Containing Aromatic Hydrocarbons, n-Alkanes, CO2, N2, and H2S

Dong Nguyen-Huynh, T. K. S. Tran, S. Tamouza, et al.
Industrial & Engineering Chemistry Research 47 (22) 8859 (2008)
https://doi.org/10.1021/ie071644j

Transport coefficients and dynamic properties of hydrogen sulfide from molecular simulation

Carlos Nieto-Draghi, Allan D. Mackie and Josep Bonet Avalos
The Journal of Chemical Physics 123 (1) (2005)
https://doi.org/10.1063/1.1949208