Open Access
Issue
Oil & Gas Science and Technology - Rev. IFP
Volume 61, Number 2, March-April 2006
Dossier: Energy-Environment-Economics and Thermodynamics
Page(s) 269 - 276
DOI https://doi.org/10.2516/ogst:2006020
Published online 01 January 2007
  • Da Silva, M.V. and Barbosa, D. (2002) High Pressure Vapor- Liquid Equilibrium Data for the Systems Carbon Dioxide/2- Methyl-1-Propanol and Carbon Dioxide/3-Nethyl-1-Butanol at 288.2, 303.2 and 313.2 K. Fluid Phase Equil., 198, 229-237. [CrossRef]
  • Hartono, R.,Mansoori, G.A. and Suwono, A. (1999) Prediction of Molar Volumes, Vapor Pressures and Supercritical Solubilities of Alkanes by Equation of State. Chem. Eng. Comm., 173, 23-42. [CrossRef]
  • Johnston, K.P.,Ziger, D.H. and Eckert, C.A. (1982) Solubilities of Hydrocarbon Solid in Supercritical Fluids. The Augmented Van der Waals Treatment. Ind. Eng. Chem. Fundam., 21, 191-197. [CrossRef]
  • Laugier, S. and Richon, D. (1996) High-Pressure Vapor-Liquid Equilibria for Ethylene+4-Methyl-1-Pentene and 1-Butene+1- Hexene. J. Chem. Eng. Data, 41, 282-284. [CrossRef]
  • Madras, G.,Kulkarni, C. and Modak, J. (2003) Modeling the Solubilities of Fatty Acids in Supercritical Carbon Dioxide. Fluid Phase Equil., 209, 207-213. [CrossRef]
  • Malanowski, S. and Anderko, A. (1992) Modeling Phase Equilibria, Second Edition, John Wiley, New York.
  • Mohsen-Nia, M.,Modarres, H. and Mansoori, G.A. (1995) A Cubic Equation of State Based on a Simplified Hard-Core Model. Chem. Eng. Comm., 131, 15-31. [CrossRef]
  • Mohsen-Nia, M.,Modarres, H. and Mansoori, G.A. (2003) A Cubic Hard-Core Equation of State. Fluid Phase Equil., 206, 27-39. [CrossRef]
  • Nasrifar, Kh. and Moshfeghian, M. (2004) Application of an Improved Equation of State to Reservoir Fluids: Computation of Minimum Miscibility Pressure. J. Pet. Sci. Eng., 42, 223-234. [CrossRef]
  • Oh, B.C.,Kim, Y.,Shin, H.Y. and Kim, H. (2004) Vapor-Liquid Equilibria for the System 1-Propanol + n-hexane Near the Critical Region. Fluid Phase Equil., 15, 41-46. [CrossRef]
  • 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]
  • Peng, D.Y. and Robinson, D.B. (1976) A New Two-Constant Equation of State. Ind. Eng. Chem. Fundam., 15, 59-64. [CrossRef]
  • Perry, R.H. and Green, D.W. (1988) Perry’s Chemical Engineers’ Handbook, Sixth Edition, McGraw Hill, Tokyo.
  • Redlich, O. and Kwong, J.N.S. (1949) On the Thermodynamics of Solutions, V: An Equation of State. Fugacities of Gaseous Solutions. Chem. Rev., 44, 233-244. [CrossRef] [PubMed]
  • Riazi, M.R. and Mansoori, G.A. (1993) Simple Equation of State accurately Predicts Hydrocarbon Densities. Oil and Gas J., July 12, 108-111.
  • Scurto, A.M.,Lubbers, C.M.,Xu, G. and Brennecke, J.F. (2001) Experimental Measurement and Modeling of the Vapor-Liquid Equilibrium of Carbon Dioxide + Chloroform. Fluid Phase Equil., 190, 135-147. [CrossRef]
  • Smith, B.D. and Srivastava, R. (1986) Thermodynamic Data for Pure Compounds, Elsevier.
  • Soave, G. (1972) Equilibrium Constants from a Modified Redlich-Kwong Equation of State. Chem. Eng. Sci., 72, 1197-1203.
  • Valderrama, J.O. (1990) A Generalized Patel-Teja Equation of State for Polar and Nonpolar Fluids and Mixtures. J. Chem. Eng. Japan, 23, 87-91. [CrossRef]
  • Van der Waals, J.D. (1873) PhD. Dissertation, Leiden.
  • Vargaftik, N.B. (1975) Handbook of Physical Properties of Liquids and Gases (Pure Substances and Mixtures), Second Edition, English Translation, Hemisphere Publication, Washington, DC.
  • Winnick, J. (1997) Chemical Engineering Thermodynamics, John Wiley, New York.

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