Open Access
Issue
Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles
Volume 66, Number 6, November-December 2011
Page(s) 1025 - 1033
DOI https://doi.org/10.2516/ogst/2011101
Published online 28 September 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]
  • Ahmed T. (1989) Hydrocarbon Phase Behavior, Gulf Publishing, Houston.
  • 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.
  • 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]
  • 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. [CrossRef]
  • Danesh A. (1998) PVT and Phase Behavior of Petroleum ReservoirFluids, Elsevier science, Netherlands.
  • 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]
  • 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.
  • 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.
  • 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.
  • Katz D.L. (1983) Overview of Phase Behavior of Oil and Gas Production, J. Petrol. Technol. 35, 6, 1205-1214.
  • 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.
  • 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]
  • 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.
  • 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.
  • 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. [CrossRef]
  • Patel N., Teja A. (1982) A New Equation of State for Fluids and Fluid Mixtures, Chem. Eng. Sci. 37, 3, 463-473. [CrossRef]
  • Pedersen K.S., Thomassen P., Fredenslund A. (1989) The Properties of Oils and Natural Gases, Gulf Publishing, Houston.
  • Pedersen K.S., Thomassen P., Fredenslund A. (1982) Phase equilibria and separation processes, Report SEP 8207, Inst. for Kemiteknik, Denmark Tekniske Hojskole.
  • Peneloux A., Rausy E., Freze R. (1982) A Consistent Correction for Redlich-Kwong-Soave Volumes, J. Fluid Phase Equilibria 8, 7-23. [CrossRef]
  • 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]
  • Riazi M.R. (1997) A Continuous Model for C7+ Fraction Characterization of Petroleum Fluids, Ind. Eng. Chem. Res. 36, 10, 4299-4307. [NASA ADS] [CrossRef] [MathSciNet] [PubMed]
  • Riazi M.R., Daubert T.E. (1987) Characterizing Parameters for Petroleum Fractions, Ind. Eng. Chem. Res. 26, 24, 755-759. [NASA ADS] [CrossRef] [MathSciNet] [PubMed]
  • Robinson D.B., Peng D. (1976) A New Two-Constant Equation of State, Ind. Eng. Chem. Fund. 19, 1, 59-64.
  • Schmidt G., Wenzel H. (1980) A Modified Van Der Waals Type Equation of State, Chem. Eng. Sci. 135, 1503-1512. [CrossRef]
  • 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.
  • 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.
  • Soave G. (1972) Equilibrium Constants from a Modified Redlich-Kwong Equation of State, Chem. Eng. Sci. 27, 1197-1203. [CrossRef]
  • 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.
  • 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]

Current usage metrics show cumulative count of Article Views (full-text article views including HTML views, PDF and ePub downloads, according to the available data) and Abstracts Views on Vision4Press platform.

Data correspond to usage on the plateform after 2015. The current usage metrics is available 48-96 hours after online publication and is updated daily on week days.

Initial download of the metrics may take a while.