ogst
Accueil Tous les numéros Volume 66 / Numéro 6 (November-December 2011) Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles, 66 6 (2011) 1025-1033 Références
Open Access
Numéro
Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles
Volume 66, Numéro 6, November-December 2011
Page(s) 1025 - 1033
DOI https://doi.org/10.2516/ogst/2011101
Publié en ligne 28 septembre 2011
  • Abrishami Y., Hatamian H., Dawe R.A. (1997) Tuning of Peng-Robinson Equation of State for Simulation of Compositional Change in Flue Gas Injection Processes, J. Fluid Phase Equilibria 139, 219-254. [CrossRef] [Google Scholar]
  • Ahmed T. (1989) Hydrocarbon Phase Behavior, Gulf Publishing, Houston. [Google Scholar]
  • Ahmed T., Cady G., Story A. (1985) A Generalized Correlation for Characterizing the Hydrocarbon Heavy Fractions, SPE paper 14266, 60th SPE Annual Conference, Las Vegas, USA, September 22-25. [Google Scholar]
  • Almehaideb R.A., Al-Khanbashi A.S., Abdulkarim M., Maher A.A. (2000) EOS Tuning to Model Full-field Crude Oil Properties Using Multiple Well Fluid PVT Analysis, J. Petrol. Sci. Eng. 26, 291-300. [CrossRef] [Google Scholar]
  • Coats K.H., Smart G.T. (1986) Application of a Regression-Based EOS PVT Program to Laboratory Data, SPE Reserv. Eng. 1, 3, 277–299. [Google Scholar]
  • Danesh A. (1998) PVT and Phase Behavior of Petroleum ReservoirFluids, Elsevier science, Netherlands. [Google Scholar]
  • Graboski M.S., Daubert T.E. (1978) A Modified Soave Equation of State for Phase Equilibrium Calculations 1-Hydrocarbon Systems, Ind. Eng. Chem. Process Des. Dev. 17, 4, 443-448. [CrossRef] [Google Scholar]
  • Heyen G. (1983) A Cubic Equation of State with Extended Range of Application, Proc. 2nd World Congress Chem. Eng., Montreal, Canada, October 4-9, pp. 41-46. [Google Scholar]
  • Hong K.C. (1982) Lumped Component Characterization of Crude Oils for Compositional Simulation, SPE/DOE paper 10691, 3rd Joint Symposium on EOR, Tulsa, Oklahoma, April 4-7. [Google Scholar]
  • Jhaveri B.S., Youngren G.K. (1984) Three Parameter Modification of the Peng–Robinson Equation of State to Improve Volumetric Predictions, SPE paper 13118, 59th SPE Annual Technical Congress, Houston, USA. [Google Scholar]
  • Katz D.L. (1983) Overview of Phase Behavior of Oil and Gas Production, J. Petrol. Technol. 35, 6, 1205-1214. [Google Scholar]
  • Katz D.L., Firoozabadi A. (1978) Predicting Phase Behavior of Condensate/Crude-Oil Systems Using Methane Interaction Coefficients, J. Petrol. Technol. 30, 11, 1649-1655. [Google Scholar]
  • Kubic W.L.J. (1982) A Modification of the Martin Equation of State for Calculating Vapor-Liquid Equilibria, J. Fluid Phase Equilibria 9, 1, 79-97. [CrossRef] [Google Scholar]
  • Lee S. et al. (1979) Experimental and Theoretical Studies on the Fluid Properties Required for Simulation of Thermal Processes, SPE paper 8393, presented at the SPE 54th Annual Technical Conference, Las Vegas, NV, September 23-26. [Google Scholar]
  • Merrill R.C., Hartman K.J., Creek J.L. (1994) A Comparison of Equation of State Tuning Methods, SPE paper 28589, SPE 69th Annual Technical Conference and Exhibition, New Orleans, USA. [Google Scholar]
  • Merrill R.C., Newley T.M.J. (1993) A Systematic Investigation into the most Suitable Data for the Development of Equations of State for Petroleum Reservoir Fluids, J. Fluid Phase Equilibria 82, 101-110. [Google Scholar]
  • Patel N., Teja A. (1982) A New Equation of State for Fluids and Fluid Mixtures, Chem. Eng. Sci. 37, 3, 463-473. [CrossRef] [Google Scholar]
  • Pedersen K.S., Thomassen P., Fredenslund A. (1989) The Properties of Oils and Natural Gases, Gulf Publishing, Houston. [Google Scholar]
  • Pedersen K.S., Thomassen P., Fredenslund A. (1982) Phase equilibria and separation processes, Report SEP 8207, Inst. for Kemiteknik, Denmark Tekniske Hojskole. [Google Scholar]
  • Peneloux A., Rausy E., Freze R. (1982) A Consistent Correction for Redlich-Kwong-Soave Volumes, J. Fluid Phase Equilibria 8, 7-23. [CrossRef] [Google Scholar]
  • Redlich O., Kwong J. (1949) On the Thermodynamics of Solutions-An Equation of State-Fugacities of Gaseous Solutions, Chem. Rev. 44, 233-247. [CrossRef] [PubMed] [Google Scholar]
  • Riazi M.R. (1997) A Continuous Model for C7+ Fraction Characterization of Petroleum Fluids, Ind. Eng. Chem. Res. 36, 10, 4299-4307. [Google Scholar]
  • Riazi M.R., Daubert T.E. (1987) Characterizing Parameters for Petroleum Fractions, Ind. Eng. Chem. Res. 26, 24, 755-759. [Google Scholar]
  • Robinson D.B., Peng D. (1976) A New Two-Constant Equation of State, Ind. Eng. Chem. Fund. 19, 1, 59-64. [Google Scholar]
  • Schmidt G., Wenzel H. (1980) A Modified Van Der Waals Type Equation of State, Chem. Eng. Sci. 135, 1503-1512. [CrossRef] [Google Scholar]
  • Sim W.J., Daubert T.E. (1980) Prediction of Vapor-Liquid Equilibria of Undefined Mixtures, Ind. Eng. Chem. Process Des. Dev. 19, 3, 380-393. [Google Scholar]
  • Slot-Peterson C. (1987) A Systematic and Consistent Approach to Determine Binary Interaction Coefficients for the Peng–Robinson Equation of State, SPE paper 16941, 62nd SPE Annual Technical Conference, Dallas, USA, 27-30. [Google Scholar]
  • Soave G. (1972) Equilibrium Constants from a Modified Redlich-Kwong Equation of State, Chem. Eng. Sci. 27, 1197-1203. [CrossRef] [Google Scholar]
  • Whitson C.H., Anderson T.F., Soreide I. (1988) C7+Characterization of Related Equilibrium Fluids Using the Gamma Distribution, AIChE Spring Meeting, New Orleans, USA, March 6-10. [Google Scholar]
  • Xu D., Danesh A., Todd A.C. (1992) An Accelerated Successive Substitution Method for Calculation of Multi-Component Fluids, Fluid Phase Equilibria 72, 15-24. [CrossRef] [Google Scholar]

Les statistiques affichées correspondent au cumul d'une part des vues des résumés de l'article et d'autre part des vues et téléchargements de l'article plein-texte (PDF, Full-HTML, ePub... selon les formats disponibles) sur la platefome Vision4Press.

Les statistiques sont disponibles avec un délai de 48 à 96 heures et sont mises à jour quotidiennement en semaine.

Le chargement des statistiques peut être long.