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Home All issues Volume 62 / No 5 (September-October 2007) Oil & Gas Science and Technology - Rev. IFP, 62 5 (2007) 707-714 References
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Issue
Oil & Gas Science and Technology - Rev. IFP
Volume 62, Number 5, September-October 2007
Page(s) 707 - 714
DOI https://doi.org/10.2516/ogst:2007050
Published online 26 September 2007
  • Avila, S.,Blanco, S.T.,Velasco, I.,Rauzy, E. and Otin, S. (2002a) Thermodynamic Properties of Synthetic Natural Gases. 1. Dew Point Curves of Synthetic Natural Gases and Their Mixtures with Water and Methanol. Measurement and Correlation. Ind. Eng. Chem. Res., 41, 3714-3721. [Google Scholar]
  • Avila, S.,Blanco, S.T.,Velasco, I.,Rauzy, E. and Otin, S. (2002b) Thermodynamic Properties of Synthetic Natural Gases. 2. Dew Point Curves of Synthetic Natural Gases and Their Mixtures with Water and Methanol. Measurement and Correlation. Energ. Fuel, 16, 928-934. [CrossRef] [Google Scholar]
  • Blanco, S.T.,Avila, S.,Velasco, I.,Rauzy, E. and Otín, S. (2000) Dew Points of Ternary Methane plus Ethane plus Butane and Quaternary Methane plus Ethane plus Butane plus Water Mixtures: Measurement and Correlation. Fluid Phase Equilibr., 171, 233-242. [CrossRef] [Google Scholar]
  • Castier, M. (1999) Automatic Implementation of Thermodynamic Models Using Computer Algebra. Comput. Chem. Eng., 23, 1229-1245. [CrossRef] [Google Scholar]
  • Castier, M. and Sandler, S.I. (1997) Critical Points with the Wong-Sandler Mixing Rule. Part I: Calculations with the Van der Waals Equation of State. Chem. Eng. Sci., 52, 3393-3399. [CrossRef] [Google Scholar]
  • Chapman, W.G.,Gubbins, K.E.,Jackson, G. and Radosz, M. (1990) New Reference Equation of State for Associating Liquids. Ind. Eng. Chem. Res., 29, 1709-1721. [CrossRef] [Google Scholar]
  • Cismondi, M. and Mollerup, J. (2005) Development and Application of a Three-Parameter RK-PR Equation of State. Fluid Phase Equilibr., 232, 74-89. [Google Scholar]
  • de Hemptinne, J.C.,Mougin, P.,Barreau, A.,Ruffine, L.,Tamouza, S. and Inchekel, R. (2006) Application to Petroleum Engineering of Statistical Thermodynamics-Based Equations of State. Oil Gas Sci. Technol., 61, 363-386. [CrossRef] [EDP Sciences] [Google Scholar]
  • Gross, J. and Sadowski, G. (2001) Perturbed-Chain SAFT: an Equation of State Based on a Perturbation Theory for Chain Molecules. Ind. Eng. Chem. Res., 40, 1244-1260. [CrossRef] [Google Scholar]
  • Heidemann, R.A. and Khalil, A.M. (1980) The Calculation of Critical Points. AIChE J., 26, 769-779. [Google Scholar]
  • Hicks, C.P. and Young, C.L. (1977) Theoretical Predictions of Phase Behaviour at High Temperatures and Pressures for Non-Polar Mixtures: 1. Computer Solution Techniques and Stability Tests. J. Chem. Soc., Faraday II, 73, 597-612. [CrossRef] [MathSciNet] [Google Scholar]
  • Huang, Q. and Guo, T.-M. (1995) Prediction of the Critical Points of Natural Gas Mixtures by Rigorous and Semi-Empirical Methods. J. Petrol. Sci. Eng., 13, 233-245. [CrossRef] [Google Scholar]
  • Jarne, C.,Avila, S.,Blanco, S.T.,Rauzy, E.,Otin, S. and Velasco, I. (2004) Thermodynamic Properties of Synthetic Natural Gases. 5. Dew Point Curves of Synthetic Natural Gases and Their Mixtures with Water and With Water and Methanol: Measurement and Correlation. Ind. Eng. Chem. Res., 43, 209-217. [CrossRef] [Google Scholar]
  • Kim, C.-H.Vimalchand, P.,Donohue, M.D. and Sandler, S.I. (1986) Local Composition Model for Chain-Like Molecules: A New Simplified Version of the Perturbed Hard-Chain Theory. AIChE J., 32, 1726-1734. [CrossRef] [Google Scholar]
  • Martinez, S.A. and Hall, K.R. (2006) Thermodynamic Properties of Light Synthetic Natural Gas Mixtures Using the RK-PR Cubic Equation of State. Ind. Eng. Chem. Res., 45, 3684-3692. [CrossRef] [Google Scholar]
  • Michelsen, M.L. (1982) The Isothermal Flash Problem. I. Stability Analysis. Fluid Phase Equilibr., 9, 1-19. [Google Scholar]
  • MFormula rch, Formula .,Nasrifar, Kh.,Bolland, O.,Solbraa, E.,Fredheim, A.O. and Gjertsen, L.H. (2006) Measurement and Modeling of Hydrocarbon Dew Points for Five Synthetic Natural Gas Mixtures. Fluid Phase Equilibr., 239, 138-145. [CrossRef] [Google Scholar]
  • Nasrifar, K. and Bolland, O. (2006) Prediction of Thermodynamic Properties of Natural Gas Mixtures Using 10 Equations of State Including a New Cubic Two-Constant Equation of State. J. Petrol. Sci. Eng., 51, 253-266. [Google Scholar]
  • Nasrifar, K.,Bolland, O. and Moshfeghian, M. (2005) Predicting Natural Gas Dew Points from 15 Equations of State. Energ. Fuel, 19, 561-572. [Google Scholar]
  • Patel, N.C. and Teja, A.S. (1982) A New Cubic Equation of State for Fluids and Fluid Mixtures. Chem. Eng. Sci., 37, 463-473. [CrossRef] [Google Scholar]
  • Peng, D.Y. and Robinson, D.B. (1976) A New Two-Constant Equation of State. Ind. Eng. Chem. Fundamentals, 15, 59-64. [Google Scholar]
  • Poling, B.E., Prausnitz, J.M. and O'Connell, J.P. (2000) The Properties of Gases and Liquids, McGraw-Hill, New York. [Google Scholar]
  • Urlic, L.E.,Florusse, L.J.,Straver, E.J.M.,Degrange, S. and Peters, C.J. (2003) Phase and Interfacial Tension Behavior of Certain Model Gas Condensates: Measurements and Modeling. Transport Porous Med., 52, 141-157. [CrossRef] [Google Scholar]
  • Valderrama, J.O. (2003) The State of the Cubic Equations of State. Ind. Eng. Chem. Res., 42, 1603-1618. [CrossRef] [Google Scholar]
  • Voulgaris, M.E., Peters, C.J. and de SwaanArons, J. (1998) Prediction of the Condensation Behavior of Natural Gas: A Comparative Study of the Peng-Robinson and the Simplified-Perturbed-Hard-Chain Theory Equations of State. Ind. Eng. Chem. Res., 37, 1696-1706. [CrossRef] [Google Scholar]

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