Relationship between the binary interaction parameters (kij) of the Peng-Robinson and those of the Soave-Redlich-Kwong equations of state: Application to the definition of the PR2SRK model

Fluid Phase Equilibria

Volumn 295, Issue 1, 2010, Pages 26-37

  Jaubert, Jean Noël ^a   Privat, Romain ^a  

^a UNIVERSITÉ DE LORRAINE   (France)

Author keywords

Binary interaction parameters; Constant packing fraction mixing rules; Cubic equation of state; Peng Robinson Soave Redlich Kwong; Predictive model; Van Laar Gibbs excess energy model

Indexed keywords

BINARY MIXTURES; BINS; FUNCTIONS; GIBBS FREE ENERGY; MIXING; PHASE EQUILIBRIA;

BINARY INTERACTION PARAMETER; CUBIC EQUATION OF STATE; GIBBS-EXCESS ENERGY MODELS; MIXING RULES; PREDICTIVE MODELING; SOAVE-REDLICH-KWONG;

EQUATIONS OF STATE;

EID: 77954887431     PISSN: 03783812     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.fluid.2010.03.037     Document Type: Article

References (28)

1. D.B. Robinson, D.Y. Peng, The characterization of the heptanes and heavier fractions for the GPA Peng-Robinson programs, Gas processors association, Research report RR-28, 1978, (booklet only sold by the GPA= gas processors association).
2. G. Soave, Chem. Eng. Sci. 27 (1972) 1197-1203.
3. J.-N. Jaubert, F. Mutelet, Fluid Phase Equilib. 224 (2) (2004) 285-304.
4. J.-N. Jaubert, S. Vitu, F. Mutelet, J.-P. Corriou, Fluid Phase Equilib. 237 (1/2) (2005) 193-211.
5. S. Vitu, J.-N. Jaubert, F. Mutelet, Fluid Phase Equilib. 243 (2006) 9-28.
6. S. Vitu, R. Privat, J.-N. Jaubert, F. Mutelet, J. Supercrit. Fluids 45 (1) (2008) 1-26.
7. R. Privat, J.-N. Jaubert, F. Mutelet, Ind. Eng. Chem. Res. 47 (6) (2008) 2033-2048.
8. R. Privat, J.-N. Jaubert, F. Mutelet, J. Chem. Thermodyn. 40 (2008) 1331-1341.
9. R. Privat, F. Mutelet, J.-N. Jaubert, Ind. Eng. Chem. Res. 47 (2008) 10041-10052.
10. R. Privat, J.-N. Jaubert, F. Mutelet, Ind. Eng. Chem. Res. 47 (2008) 7483-7489.
11. J.Jaubert, R. Privat, F. Mutelet. Predicting the phase equilibria of synthetic petroleum fluids with the PPR78 approach (2010)AIChE Journal ,56(12),3225-3235 ,doi:10.1002/aic.12232.
12. F. Mutelet, S. Vitu, R. Privat, J.-N. Jaubert, Fluid Phase Equilib. 238 (2005) 157-168.
13. S. Vitu, J.-N. Jaubert, J. Pauly, J.-L. Daridon, D. Barth, J. Chem. Eng. Data 52 (2007) 1851-1855.
14. S. Vitu, J.-N. Jaubert, J. Pauly, J.-L. Daridon, D. Barth, J. Supercrit. Fluids 44 (2) (2008) 155-163.
15. S. Vitu, J.-N. Jaubert, J. Pauly, J.-L. Daridon, J. Chem. Thermodyn. 40 (2008) 1358-1363.
16. R. Privat, F. Garcia, J.-N. Jaubert, M. Moliere, J. Eng. Gas Turbine Power (2010), doi:10.1115/1.4000610.
17. E.A. Guggenheim, Mixtures, Oxford University Press, Oxford, 1952.
18. A. Péneloux, W. Abdoul, E. Rauzy, Fluid Phase Equilib. 47 (2-3) (1989) 115-132.
19. E. Fransson, L. Vamling, J. Vidal, Chem. Eng. Sci. 48 (1993) 1753-1759.
20. P.M. Mathias, T.W. Copeman, Fluid Phase Equilib. 13 (1983) 91-108.
21. D.Y. Peng, D.B. Robinson, Ind. Eng. Chem. Fundam. 15 (1976) 59-64.
22. O. Redlich, E.L. Derr, G.J. Pierotti, J. Am. Chem. Soc. 81 (1959) 2283-2285.
23. H.V. Kehiaian, K. Sosnkowska-Kehiaian, R. Hryniewicz, J. Chim. Phys. Phys. Chim. Biol. 68 (6) (1971) 922-934.
24. W. Abdoul, E. Rauzy, A. Péneloux, Fluid Phase Equilib. 68 (1991) 47-102.
25. J.-N. Jaubert, L. Coniglio, F. Denet, Ind. Eng. Chem. Res. 38 (1999) 3162-3171.
26. J.-N. Jaubert, L. Coniglio, Ind. Eng. Chem. Res. 38 (1999) 5011-5018.
27. J.-N. Jaubert, P. Borg, L. Coniglio, D. Barth, J. Supercrit. Fluids 20 (2001) 145-155.
28. P.H. Van Konynenburg, R.L. Scott, Philos. Trans. R. Soc. Lond. Ser. A 298 (1980) 495-540.