Open Access
Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles
Volume 71, Numéro 1, January–February 2016
Numéro d'article 5
Nombre de pages 12
Publié en ligne 22 janvier 2016
  • Ahmed T. (1989) Hydrocarbon phase behavior, Gulf Publishing Houston, pp.356–359 [Google Scholar]
  • Avaullee L., Trassy L., Neau E., Jaubert J.N. (1997a) Equation of state and group contribution for the estimation of thermodynamic parameters of heavy hydrocarbons Thermodynamic modeling for petroleum fluids I, Fluid Phase Equilibria 139, 155–170. [CrossRef] [Google Scholar]
  • Avaullee L., Neau E., Jaubert J.N. (1997b) Thermodynamic modeling for petroleum fluids IIPrediction of PVT properties of oils and gases by fitting one or two parameters to the saturation pressures of reservoir fluids, Fluid Phase Equilibria 139, 171–203. [CrossRef] [Google Scholar]
  • Avaullee L., Neau E., Jaubert J.N. (1997c) Thermodynamic modeling for petroleum fluids III. Reservoir fluid saturation pressures. A complete PVT property estimation Application to swelling test, Fluid Phase Equilibria 141, 87–104. [CrossRef] [Google Scholar]
  • Avaullee L., Duchet-Suchaux P., Durandeau M., Jaubert J.N. (2001) A new approach in correlating the oil thermodynamic properties, Journal of Petroleum Science and Engineering 30, 43–65. [CrossRef] [Google Scholar]
  • Carreón-Calderón B., Uribe-Vargas V., Ramírez Jaramillo E., Ramírez de Santiago M. (2012) Thermodynamic Characterization of Undefined Petroleum Fractions using Group Contribution Methods, Ind. Eng. Chem. Res. 51, 14188–14198. [CrossRef] [Google Scholar]
  • Coats K.H., Smart G.T. (1986) Application of a regression-based EOS PVT program to laboratory data, SPE Reservoir Eng. 1, 03, 277–299. [Google Scholar]
  • Dahl S., Michelsen M.L. (1990) High pressure vapour-liquid equilibrium with a UNIFAC-based equation of state, AIChE J. 36, 1829–1836. [CrossRef] [Google Scholar]
  • Elsharkawy A.M. (2002) Predicting the dew point pressure for gas condensate reservoirs: empirical models and equations of state, Fluid Phase Equilib. 193, 147–165. [CrossRef] [Google Scholar]
  • Elbro H.S., Fredenslund A., Rasmussen P. (1991) Group contribution method for the prediction of liquid densities as a function of temperature for solvents, oligomers, and polymers, Ind. Eng. Chem. Res. 30, 12, 2576–2582. [CrossRef] [Google Scholar]
  • Horstmann S., Jabłoniec A., Krafczyk J., Fischera K., Gmehling J. (2005) PSRK group contribution equation of state: comprehensive revision and extension IV, including critical constants and function parameters for 1000 components, Fluid Phase Equilib. 227, 2, 157–164. [CrossRef] [Google Scholar]
  • Hosein R., McCain W.Jr (2007) Extended analysis for gas condensate systems, SPE Annual Technical Conference and Exhibitionheld in Anaheim, California USA, 11–14 Nov, SPE-110152, SPE Reservoir Evaluation & Engineering 12, 01, 159–166. [CrossRef] [Google Scholar]
  • Ihmels ECh, Gmehling J. (2003) Extension and revision of the group contribution method GCVOL for the prediction of pure compound liquid densities, Ind. Eng. Chem. Res. 42, 2, 408–412. [CrossRef] [Google Scholar]
  • Jaubert J.N., Mutelet F. (2004) VLE predictions with the Peng-Robinson equation of state and temperature dependent kij calculated through a group contribution method, Fluid Phase Equilib. 224, 285–304. [CrossRef] [Google Scholar]
  • Jaubert J.N., Privat R., Mutelet F. (2010) Predicting the Phase Equilibria of Synthetic Petroleum Fluids with the PPR78 Approach, AIChE J. 56, 3225–3235. [CrossRef] [Google Scholar]
  • Jöback K.G., Reid R.C. (1987) Estimation of Pure-Component Properties from Group-Contributions, Chem. Eng. Commun. 57, 233–243. [CrossRef] [Google Scholar]
  • Kesler M.G., Lee B.I. (1976) Improve prediction of enthalpy of fractions, Hydrocarb Process. 55, 153–158. [Google Scholar]
  • Marrero J., Gani R. (2001) Group-contribution based estimation of pure component properties, Fluid Phase Equilib. 183–184, 183–208. [CrossRef] [Google Scholar]
  • Merrill R.C., Hartman K.J., Creek J.L. (1994) A comparison of equation of state tuning methods, presented at the SPE 69th Annual Technical Conference and Exhibition, New Orleans, LA, SPE 28589. [Google Scholar]
  • Merrill R.C., Newley T.M.J. (1993) A systematic investigation into the most suitable data for development of equation of state for petroleum reservoir fluids, Fluid Phase Equilib. 82, 101–110. [CrossRef] [Google Scholar]
  • Pedersen K.S., Christensen P.L. (2007) Phase Behavior of Petroleum Reservoir Fluids, Taylor & Francis Group, New York. [Google Scholar]
  • Pedersen K.S., Thomassen Q., Riazi M.R., Daubert T.E. (1980) Prediction of the composition of Petroleum Fractions, Ind. Eng. Chem. Process Dev. 19, 289–294. [Google Scholar]
  • Pedersen K.S., Blilie A.L., Meisingset K.K. (1992) PVT Calculations on petroleum reservoir fluid using measured and estimated composition data for the plus fraction, I&EC Research 31, 5, 1378–1383. [Google Scholar]
  • Peneloux A., Rauzy E., Fréze R. (1982) A consistent correction for Redlich-Kwong-Soave volumes, Fluid Phase Equilib. 8, 1, 7–23. [Google Scholar]
  • Peng D.Y., Robinson D.B. (1976) A New Two-Constant Equation of State, Ind. Chem. Fundam. 15, 1, 59–64. [Google Scholar]
  • Poling B.E., Prausnitz J.M., O’Connell J.P. (2001) The Properties of Gases and Liquids, 5th edn., McGraw-Hill International Edition, Singapore. [Google Scholar]
  • Riazi M.R., Daubert T.E. (1980) Simplify property predictions, Hydrocarb Process. 59, 115–116. [Google Scholar]
  • Riazi M.R., Daubert T.E. (1987) Characterization parameters for petroleum fractions, Ind. Eng. Chem. Res. 26, 755. [CrossRef] [Google Scholar]
  • Ruzicka V., Fredenslund A., Rasmussen P. (1983) Representation of petroleum fractions by group contribution, Ind. Eng. Chem. Process Des. Dev. 22, 1, 49–53. [CrossRef] [Google Scholar]
  • Sim W.J., Daubert T.E. (1980) Prediction of vapor-liquid equilibria of undefined mixture, Proces. Des. Dev. 19, 380. [Google Scholar]
  • Sinayuc C., Gumrah F. Predicting the critical properties of heptanes-plus in gas condensates: Genetic algorithms as an optimization toll (2004) Petroleum Society’s 5th Canadian International Petroleum Conference (55th Annual Technical Meeting), Calgary Alberta, Canada, 8-10 June [Google Scholar]
  • Slot-Petersen C. (1989) A systematic and consistent approach to determine binary interaction coefficients for Peng-Robinson equation of state, SPE 16941, SPE Reservoir Engineering 4, 4, 488–494. [CrossRef] [Google Scholar]
  • Soave G. (1972) Equilibrium constants from a modified Redlich-Kwong equation of state, Chem. Eng. Sci. 27, 1197–1203. [CrossRef] [Google Scholar]
  • Soreide I. (1989) Improved phase behavior predictions of petroleum reservoir fluids from a cubic equation of state, Doktor. Ing Thesis, Department of Petroleum Engineering Norwegian Institute of technology (NTH), Trondheim, Norway. [Google Scholar]
  • Whitson C.H. (1983) Characterizing hydrocarbon plus fractions, Soc. Pet. Eng. J. 23, 4, 683–694. [Google Scholar]
  • Whitson C.H. (1984) Effect of C7+ characterization on equations of state predictions, Soc. Pet. Eng. J. 24, 6, 685–694. [CrossRef] [Google Scholar]
  • Whitson C.H., Anderson T.F., Soreide I. (1990) Application of gamma distribution model to molecular weight and boiling point data for petroleum fractions, Chem. Eng. Comm. 96, 259. [CrossRef] [Google Scholar]
  • Wong D.S.H., Sandler S.I.A. (1992) A theoretically correct mixing rule for cubic equations of state, AIChE J. 38, 671–680. [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.