Addition of the hydrogen sulfide group to the PPR 78, Model (Predictive 1978, Peng-Robinson equation of state with temperature dependent kij- calculated through a group contribution method)

Industrial and Engineering Chemistry Research

Volumn 47, Issue 24, 2008, Pages 10041-10052

  Privat, Romain ^a   Mutelet, Fabrice ^a   Jaubert, Jean Noël ^a  

^a UNIVERSITÉ DE LORRAINE   (France)

Author keywords

[No Author keywords available]

Indexed keywords

BINARY INTERACTION PARAMETERS; EXPERIMENTAL DATUM; GROUP-CONTRIBUTION METHODS; PENG-ROBINSON EQUATION OF STATE; TEMPERATURE DEPENDENTS;

CARBON DIOXIDE; EQUATIONS OF STATE; ETHANE; HYDROGEN; METHANE; SULFUR DETERMINATION;

HYDROGEN SULFIDE;

EID: 64549104739     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie800799z     Document Type: Article

References (61)

1. Jaubert, J. N.; Mutelet, F. VLE predictions with the Peng-Robinson equation of state and temperature dependent kij calculated through a group contribution method. Fluid Phase Equilib. 2004, 224 (2), 285-304.
2. Jaubert, J. N.; Vitu, S.; Mutelet, F.; Corriou, J. P. Extension of the PPR78 model (Predictive 1978. Peng Robinson EOS with temperature dependent kij calculated through a group contribution method, to systems containing aromatic compounds. Fluid Phase Equilib. 2005, 237 (1-2), 193-211.
3. Vitu, S.; Jaubert, J. N.; Mutelet, F. Extension of the PPR78 model (Predictive 1978, Peng Robinson EOS with temperature dependent kij calculated through a group contribution method) to systems containing naphtenic compounds. Fluid Phase Equilib. 2006, 24.?, 9-28.
4. 2 + hydrocarbon systems with the PPR78 model (PR EOS and kij calculated through a group contribution method).J Supercrit. Fluids2008, 45 1), 1-26.
5. Privat, R.; Jaubert, J. N.; Mutelet, F. Addition of the Nitrogen group to the PPR78 model (Predictive 1978, Peng-Robinson EOS with temperature dependent kij calculated through a group contribution method). Ind. Eng. Chem. Res. 2008, 47 (6), 2033-2048.
6. Privat. R.; Jaubert, J. N.: Mutelet. F. Addition of the sulfhydryl group (-SH) to the PPR78 model (Predictive 1978, Peng-Robinson'EOS with temperature dependent kijcalculated through a group contribution method). J.Chem. Thermodyn. 2008, 40 (9), 1331-1341.
7. Privat, R.; Jaubert, J. N.; Mutelet, F. Use of the PPR78 model to predict new equilibrium data of binary systems involving hydrocarbons and nitrogen. Comparison with other GCEOS. Ind. Eng. Chem. Res. 2008, 47, 7483-7489.
8. 2 in branched alkanes in order to extend the PPR78 model (Predictive 1978, eng Robinson EOS widi temperature dependent kij calculated through a group contribution method) to such systems. Fluid Phase Equilib. 2005, 238 (2), 157-168.
9. Vitu, S.; Jaubert, J. N.; Pauly, J.; Daridon, J. L.; Barth, D. Bubble and Dew Points of Carbon Dioxide + a Five-Component Synthetic Mixture: Experimental Data and Modeling with the PPR78 Model. .J. Chem. Eng. Data 2007, 52 (5), 1851-1855.
10. 2 + isopropyl cyclohexane binary mixtures at elevated pressures. J. Suvererit. Fluids 2008, 44 (2), 155-163.
11. Vitu, S.; Jaubert, J. N.; Pauly, J.; Daridon, J. L. High-pressure phase behaviour of the binary system {C02 + cis-decalin} from 292.75 to 373.75 K. J.Chem. Thermodyn.'2008, 40 (9), 1358-1363.
12. 2-fish oils) phase behavior. Ind. Eng. Chem. Res. 1999, 38, 3162-3171.
13. 2 and fatty acids. Ind. Eng. Chem. Res. 1999, 38, 5011-5018.
14. Jaubert, J. N.; Borg, P.; Coniglio, L.; Barth. D. Phase equilibria measurements and modeling of EPA and DHA ethyl esters in supercritical carbon dioxide. J.Supercrit. Fluids. 2001. 20, 145-155.
15. Robinson, D. B.; Peng. D. Y. The characterization of the heptanes and heavier fractions for the GPA Peng-Robinson programs; Gas Processors Association, Research Report RR-28, 1978.
16. Poling, B. E., Prausnitz, J. M.; O'Connell, J. P. The properties of gases and liquids, 5di ed.; Mc Graw Hill: New York, 2000.
17. Kalra, H.; Krishnan, T. R.; Robinson, D. B. Equilibrium-phase properties of carbon dioxide-butane and nitrogen-hydrogen sulfide systems at subambient temperatures. J. Chem. Eng. Data 1976, 21 (2), 222-225.
18. Besserer, G. J.; Robinson, D. B. Equilibrium-phase properties of nitrogen-hvdrogen sulfide system. J. Chem. Eng. Data 1975. 20 (2), 157-161.
19. Wilson, G. M.; Cunningham, J. R.; Nielsen, P. F. Enthalpy and Phase Boundary Measurements on Mixtures of Nitrogen with Methane, Carbon Dioxide and Hydrogen Sulfide. Gas Processors Association, Research Report RR-24, 1977.
20. Bierlein, J. A.; Kay, W. B. Phase-equilibrium properties of system carbon dioxide-hydrogen sulfide. J. ind. Eng. Chem. 1953, 45, 618-624.
21. Sobocinski, D. P.; Kurata, F. Heterogeneous phase equilibriums of the hydrogen sulfide-carbon dioxide system. AIChE J. 1949, J, 545-551.
22. Stouffer. C. E.; Kellerman, S. J.; Hall, K. R.; Holste, J. C; Gammon. B. E.; Marsh, K. N. Densities of Carbon Dioxide + Hydrogen Sulfide Mixtures from 220 to 450 K at Pressures up to 25 MPa. J, Chem. Eng. Data 2001, 46 (5), 1309-1318.
23. Yarym-Agaev, N. L.; Afanasenko, L. D.; Matvienko, V. G.; Ryabkin, Y. Y.; Tolmacheva, G. B. Gas-liquid equilibrium in the methane- hydrogen sulfide system below 273 K. Ukr. Khim. Z. 1991, 57 (7), 701-704.
24. Robinson, D. B.; Lorenzo, A. P.; Macrygeorges, C. A. The carbon dioxide-hydrogen sulfide-methane system. Can. J. Chem. Eng. 1959, 37, 212-217.
25. Kohn, J. P.; Kurata, F. Volumetric behavior of the CH4-H2S system at low temperatures and high pressures. .J. (hem. Eng. Data 1959, 4, 33-36.
26. Kohn, J. P.; Kurata, F. Heterogeneous phase equilibriums of the methane-hydrogen sulfide system. AlChE J. 1958, 4, 211-217.
27. Reamer, H. H.; Sage, B. H.; Lacey, W. N. Phase equilibria in hydrocarbon systems. Volumetric and phase behavior of the methane- hydrogen sulfide system. J. Ind. Eng. Chem. 1951, 43, 976-981.
28. Robinson, D. B.; Bailey, J. A. The carbon dioxide-hydrogen sulfide-methane system. Can. J. Chem. Eng. 1957. 35, 151-158.
29. Morris, J. S.; Byers, C. H. Critical-region vapor-liquid equilibrium of the methane-carbon dioxide-hydrogen sulfide system; Oak Ridge National Laboratory Report ORNL/TM-10806, 1990.
30. Personal data.
31. Rivollet, F.; Jarne, C.: Richon, D. PρT and VLE for Ethane + Hydrogen Sulfide from (254.05 to 363.21) K at Pressures up to 20 MPa. J.Chem. Eng. Data 2005. 50 (6), 1883-1890.
32. Kalra, H.; Robinson, D. B.; Krishnan, T. R. The equilibrium phase properties of the ethane-hydrogen sulfide system at subambient temperatures. J.Chem. Eng. Data 1977, 22 (1), 85-88.
33. Kay, W. B.; Brice, D. B. Liquid-vapor equilibrium relations in ethane-hydrogen sulfide system. .J. Ind. Eng. Chem. 1953, 45, 615-618.
34. Lobo, L. Q.; Ferreira, A. G. M.; Fonseca, I. M. A.; Senra, A. M. P. Vapour pressure and excess Gibbs free energy of binary mixtures of hydrogen sulphide with ethane, propane, and n-butane at temperature of 182.33 K. J.Chem. Thermodyn. 2006, 38 (12), 1651-1654.
35. Jou, F. Y.; Caroll, J. J.; Mather, A. E. Azeotropy and critical behavior in the system propane-hydrogen sulfide. Fluid Phase Equilib. 1995. 109 (2), 235-244.
36. Kay, W. B.; Rambosek, G. M. Liquid-vapor equilibrium relations in binary systems. Propane-hydrogen sulfide systems. J. Ind. Eng. Chem. 1953, 45, 221-226.
37. Brewer, J.; Rodewald, N.; Kurata, F. Phase equilibriums of the propane-hydrogen sulfide system from the cricondontherm to the solid-liquid- vapor region. AIChE J. 1961, 7, 13-16.
38. Gilliland, E. R.; Scheeline, H. W. High-pressure vapor-liquid equilibrium for the systems propylene-isobutane and propane-hydrogen sulfide. J.Ind. Eng. Chem. 1940, 32, 48-54.
39. Steckel, F. Vapor-liquid equilibria under pressure of some binary hvdrogen sulfi de-containing svstems. Sven. Kem. Tidskr. 1945. 57. 209-216.
40. Leu, A. D.; Robinson, D. B. Equilibrium phase properties of the n-butane-hydrogen sulfide and isobutane-hydrogen sulfide binary systems. J.Chem. Eng. Data 1989, 34 3), 315-319.
41. Robinson, D. B.; Besserer, G. J. Equilibrium phase properties of the isobutane-hydrogen sulfide system. J. Chem. Eng. Jpn. 1975, 8 (1),11-15.
42. Robinson, D. B.; Besserer, G. J. The Equilibrium Phase Properties of the Binary Systems: Nitrogen-Hydrogen Sulfide, Isobutane-Hydrogen Sulfide, Isobutane-Carbon Dioxide, Isohutane-Ethane; Gas Processors Association, Research Report RR-7, 1972.
43. Leu, A. D.; Robinson, D. B. High-pressure vapor-liquid equilibrium phase properties of the isopentane-hydrogen sulfide and neopentane-hydrogen sulfide binary systems.J. Chem. Eng. Data 1992, 37 (1), 14-17.
44. Reamer, H. H.; Sage, B. H.; Lacey, W. N. Phase equilibria in hydrocarbon systems. Volumetric and phase behavior of pentane-hydrogen sulfide system'. J.Ind. Eng. Chem. 1953. 45, 1805-1809.
45. Laugier, S.; Richon, D. Vapor-Liquid Equilibria for Hydrogen Sulfide + Hexane, + Cyclohexane, + Benzene, + Pentadecane, and + (Hexane + Pentadecane).J.Chem.Eng.Data 1995,153-159.
46. King, M. B.; Al-Najjar, H. The solubilities of carbon dioxide, hydrogen sulfide, and propane in some normal alkane solvents. I. Experimental determinations in the range 15-70 °C and comparison with ideal solution values. Chem. Eng. Sci. 1977, 32 (10), 1241-1246.
47. Ng, H. J.; Kalra, H.; Robinson, D. B.; Kubota, H. Equilibrium phase properties of the toluene-hydrogen sulfide and heptane-hydrogen sulfide binary systems. J. Chem. Eng. Data 1980, 25 (1), 51-55.
48. Robinson, D. B.; Kalra, H. The Equilibrium Phase Properties of Selected Binary Systems: n-Heptane-Hydrogen Sulfide, n-Heptane-Carbon Dioxide and i-Butane-Nitrogen; Gas Processors Association, Research Report RR-18, 1976.
49. Yokoyama, C; Usui, A.; Takahashi, S. Solubility of hydrogen sulfide in isooctane, n-decane, n-tridecane, n-hexadecane and squalane at temperatures from 323 to 523 K and pressures up to 1.6 MPa. Fluid Phase Eguilib. 1993, 85, 257-269.
50. Eakin, B. E.; DeVaney, W. E. Vapor-liquid equilibrium in hydrogen-hydrogen sulfide-carbon-9 hydrocarbon systems. AIChE Symp. Ser. 1974, 70 (140), 80-90.
51. Reamer, H. H.; Selleck, F. T.; Sage, B. H.; Lacey, W. N. Phase equilibria in hydrocarbon systems. Volumetric and phase behavior of pentane-hydrogen sulfide system. J. Ind. Eng. Chem. 1953, 45, 1810-1812.
52. Feng, G. X.; Mather, A. E. Solubility of hydrogen sulfide in n-dodecane. Fluid Phase Equilib. 1993, 87 (2).'341-346.
53. Feng, G. X.; Mather, A. E. Solubility of hydrogen sulfide in n-hexadecane at elevated pressure. Can. J. Chem. Eng. 1993, 71 (2), 327-328.
54. Feng, G. X.; Mather, A. E. Solubility of hydrogen sulfide in n-eicosane at elevated pressure. .J. Chem. Eng. Data 1992, 37 (4), 412-413.
55. Fischer, K.; Chen, J.; Petri, M.; Gmehling, J. Solubility of H2S and C02 in N-octyl-2-pyrrolidone and of H2S in methanol and benzene. AIChE J. 2002, 48 (4), 887-893.
56. Huang, S. S. S.; Robinson, D. B. Vapor-liquid equilibrium in selected aromatic binary systems: m-xylene - hydrogen sulfide and mesitylene-hydrogen sulfide. Fluid Phase Equilib. 1984, 17 (3), 373-382.
57. Richon, D.; Laugier, S.; Renon, H. High-pressure vapor-liquid equilibrium data for binary mixtures containing molecular nitrogen, carbon dioxide, hydrogen sulfide and an aromatic hydrocarbon or propylcyclohex-ane in the range 313-473 K. J.Chem. Eng. Data 1992, 37 (2), 264-268.
58. Tsiklis, D. S.; Svetlova, G. M. The solubility of gases in cyclohexane. Zh Fiz. Khim. 1958, 32, 1476-1480.
59. Ng, H. J.; Robinson, D. B. The equilibrium phase properties of selected naphthenic binary systems: carbon dioxide-methylcyclohexane, hydrogen sulfide-methylcyclohexane. Fluid Phase Equilib. 1979. 2 (4), 283-292.
60. Robinson, D. B.; Huang, S. S. S.; Leu, A. D. Equilibrium Phase Properties of Selected Napthenic Binary Systems: Methyl cyclohexane - Nitrogen, Ethylcyclohexane-Hydrogen Sulfide, n-Propylcyclohexane-Hydrogen Sulfide; Gas Processors Association, Research Report RR-51, 1981.
61. Van Konynenburg, P. H.; Scott, R. L. Critical lines and phase equilibriums in binary Van der Waals mixtures. Philos. Trans. R. Soc. London, Ser A. 1980, '298, 495-540.