Prediction of the volumetric properties of hydrocarbons with an improved volume translation method;Prédiction des propriétés volumétriques des hydrocarbures par une translation de volume améliorée

Revue de l'Institute Francais du Petrole

Volumn 52, Issue 6, 1997, Pages 609-623

  Ungerer, P ^a   Batut, C ^a  

^a IFP ENERGIES NOUVELLES   (France)

Author keywords

[No Author keywords available]

Indexed keywords

AROMATIC HYDROCARBONS; DENSITY OF LIQUIDS; EQUATIONS OF STATE OF LIQUIDS; MOLECULAR WEIGHT; PARAFFINS; THERMAL EFFECTS;

MOLAR VOLUME; PENG-ROBINSON EQUATION OF STATE; VOLUME TRANSLATION METHOD;

PETROLEUM RESERVOIR EVALUATION;

EID: 0031276718     PISSN: 00202274     EISSN: None     Source Type: Journal    
DOI: 10.2516/ogst:1997062     Document Type: Article

References (19)

1. Arnaud J.F. (1995), Caractérisantion des propriétés physiques et thermodyamiques des fluides pétroliers àhaute pression. Thèse de doctorat, université de Pau.
2. Arnaud J.F., P. Ungerer, E. Behar, G. Moracchini et J. Sanchez (1996), Excess volumes and saturation pressures for the system methane + n-tetracosane at 374 K. Representation by improved EOS mixing rules. Fluid Phase Equilibria, 124, p. 177-207.
3. Chou G.F. et J.M. Prausnitz (1989), A phenomenological correctio• to an equation of state for the critical region. AIChE J., 35, p. 1487-1496.
4. Coniglio L. (1993), Estimation des propriétés thermophysiques des hydrocarbures lourds. Thèse doctorat, université d'Aix-Marseille.
5. CRC Handbook of Chemistru and Physics (1990-1991), édité par D.R. Lide, CRC Press.
6. De Hemptinne J.C. et P. Ungerer (1995), Accuracy of the volumetric predictions of some important equations of state for hydrocarbons, including a modified version of the Lee-Kesler method. Fluid Phase Equilibria, 106, p. 81-109.
7. Doolittle A.K. (1964), Specific volumes of n-alkanes. J. chem. Eng. Data 9, P. 275-279.
8. Goodwin R.D. (1988), Benzene thermophysical properties from 279 to 900 K at pressures to 1000 bar. J. Phys. Chem. Ref. Data, 17, p. 1541-1634
9. Levelt-Sengers J.M.H., G. Morrison et R.F. Chang (1983), Critical behaviour in fluids and fluid mixtures. Fluid Phase Equilibria, 14, p. 19-44.
10. 20. and their predictions for higher ones. Fluid Phase Equilibria, 56, p. 119-14O.
11. Mathias P.M., T. Naheiri et E.M. Oh (1989), A density correction for the Peng-Robinson equation of state. Fluid Phase Equilibria, 47, p. 115-132.
12. Péaeloux A., E. Rauzy et R. Frèze (1982), A consistent correction for Redlich-Kwong-Soave volumes. Fluid Phase Equilibria, 8, p. 7-21.
13. Peng D.Y. et D.B. Robinson (1976), A new two-constant equation of state. Ind. Eng. Chem. Fundam., 15, p. 59-64.
14. Reamer H. et B. Sage (1957), Phase equilibria in hydrocarbon Systems, volumetric behavior of cyclohexane. Chem. Eng. Data, Series 2, p. 9.
15. Soave G. (1972), Equilibrium constants for a modified Redlich-Kwong equation of state. Chem. Eng. Sci., 27, p. 1197-1203.
16. Soreide I. (1989), Improved phase behaviour predictions of petroleum reservoir fluids from a cubic equation of state Thèse, université de Trondheim.
17. Stewart D.E., B.H. Sage, W.N. Lacey (1942), Volumetric behaviour of n-hexane in the liquid phase. Ind. Eng. Chem., 46, p. 2529-2531.
18. Ungerer P. et C. Batut (1996), Méthode pour modéliser avec précision les propriétés volumétriques de fluides et notamment des hydrocarbures. Brevet français no 96/13 563.
19. Zhou H., B. Lagourette, J. Alliez, P. Xans, F. Montel (1990), Extension of the Simha equation of slate to the calculation of the density of n-alkanes-benzene and alkylbenzene mixtures. Fluid Phase Equilibria, 59, p. 309-328.