Calculation of critical points for multicomponent mixtures containing hydrocarbon and nonhydrocarbon components with the PC-SAFT equation of state

Fluid Phase Equilibria

Volumn 265, Issue 1-2, 2008, Pages 192-204

  Justo García, Daimler N ^a   García Sánchez, Fernando ^a   Díaz Ramírez, Nestor L ^b   Romero Martínez, Ascención ^a  

^a INSTITUTO MEXICANO DEL PETRÓLEO   (Mexico)

^b INSTITUTO POLITÉCNICO NACIONAL   (Mexico)

Author keywords

Critical point; Equation of state; Helmholtz energy; PC SAFT; Tangent plane distance

Indexed keywords

COMPUTATION THEORY; HELMHOLTZ EQUATION; HYDROCARBONS; PHASE EQUILIBRIA;

CRITICAL POINT; HELMHOLTZ ENERGY; TANGENT PLANE DISTANCE;

EQUATIONS OF STATE;

COMPUTATION THEORY; EQUATIONS OF STATE; HELMHOLTZ EQUATION; HYDROCARBONS; PHASE EQUILIBRIA;

EID: 39749133507     PISSN: 03783812     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.fluid.2007.12.006     Document Type: Article

References (157)

1. Peng D.-Y., and Robinson D.B. A rigorous method for predicting the critical properties of multicomponent systems from an equation of state. AIChE J. 23 (1977) 137-144
2. Heidemann R.A., and Khalil A.M. The calculation of critical points. AIChE J. 26 (1980) 769-779
3. Baker L.E., and Luks K.D. Critical point and saturation pressure calculations for multicomponent mixtures. Soc. Pet. Eng. J. 20 (1980) 15-24
4. Michelsen M.L. Calculation of critical points and phase boundaries in the critical region. Fluid Phase Equilib. 16 (1984) 57-76
5. Nagarajan N.R., Cullick A.S., and Griewank A. New strategy for phase equilibria and critical point calculations by thermodynamic energy analysis. Part II. Critical point calculations. Fluid Phase Equilib. 62 (1991) 211-223
6. Ting P.D., Joyce P.C., Jog P.K., Chapman W.G., and Thies M.C. Phase equilibrium modeling of mixtures of long-chain and short-chain alkanes using Peng-Robinson and SAFT. Fluid Phase Equilib. 206 (2003) 267-286
7. Ghosh A., Chapman W.G., and French R.N. Gas solubility in hydrocarbons-a SAFT-based approach. Fluid Phase Equilib. 209 (2003) 229-243
8. García-Sánchez F., Eliosa-Jiménez G., Silva-Oliver G., and Vázquez-Román R. Vapor-liquid equilibria of nitrogen-hydrocarbon systems using the PC-SAFT equation of state. Fluid Phase Equilib. 217 (2004) 241-253
9. Gross J., and Sadowski G. Application of the perturbed-chain SAFT equation of state to associating systems. Ind. Eng. Chem. Res. 41 (2002) 5510-5515
10. Tumakaka F., and Sadowski G. Application of the perturbed-chain SAFT equation of state to polar systems. Fluid Phase Equilib. 217 (2004) 233-239
11. Dominik A., Chapman W.G., Kleiner M., and Sadowski G. Modeling of polar systems with the perturbed-chain SAFT equation of state. Investigation of the performance of two polar terms. Ind. Eng. Chem. Res. 44 (2005) 6928-6938
12. Karakatsani E.K., Spyriouni T., and Economou I.G. Extended statistical associating fluid theory (SAFT) equations of state for dipolar fluids. AIChE J. 51 (2005) 2328-2342
13. Gross J. An equation-of-state contribution for polar components: quadrupolar molecules. AIChE J. 51 (2005) 2556-2568
14. Gross J. An equation-of-state contribution for polar components: dipolar molecules. AIChE J. 52 (2006) 1194-1204
15. Gross J., and Sadowski G. Modeling polymers systems using the perturbed-chain statistical associating fluid theory equation of state. Ind. Eng. Chem. Res. 41 (2002) 1084-1093
16. Gross J., Spuhl O., Tumakaka F., and Sadowski G. Modeling copolymer systems using the perturbed-chain SAFT equation of state. Ind. Eng. Chem. Res. 42 (2003) 1266-1274
17. Gross J., and Sadowski G. Perturbed-chain SAFT: an equation of state based on a perturbation theory for chain molecules. Ind. Eng. Chem. Res. 40 (2001) 1244-1260
18. Quiñones-Cisneros S.E. Barotropic phenomena in complex phase behaviour. Phys. Chem. Chem. Phys. 6 (2004) 2307-2313
19. García J., Lugo L., and Fernández J. Phase equilibria, PVT behavior, and critical phenomena in carbon dioxide + n-alkane mixtures using the perturbed-chain statistical associating fluid theory approach. Ind. Eng. Chem. Res. 43 (2004) 8345-8353
20. Heidemann R.A., Krenz R.A., and Laursen T. Spinodal curves and critical points in mixtures containing polydisperse polymers with many components. Fluid Phase Equilib. 228-229 (2005) 239-245
21. Arce P., and Aznar M. Modeling of critical lines and regions for binary and ternary mixtures using non-cubic and cubic equations of state. J. Supercrit. Fluids 42 (2007) 1-26
22. Peng D.-Y., and Robinson D.B. A new two constant equation of state. Ind. Eng. Chem. Fundam. 15 (1976) 59-64
23. Valderrama J.O. A generalized Patel-Teja equation of state for polar and nonpolar fluids and their mixtures. J. Chem. Eng. Jpn. 23 (1990) 87-91
24. Kim C.M., Vimalchand P., Donohue M.D., and Sandler S.I. Local composition model for chainlike molecules: a new simplified version of the perturbed hard chain theory. AIChE J. 32 (1986) 1726-1734
25. Alfradique M.F., and Castier M. Critical points of hydrocarbon mixtures with the Peng-Robinson, SAFT, and PC-SAFT equations of state. Fluid Phase Equilib. 257 (2007) 78-101
26. Voutsas E.C., Pappa G.D., Maguolas K., and Tassios D.P. Vapor-liquid equilibrium modeling of alkane systems with equations of state: "simplicity versus complexity". Fluid Phase Equilib. 240 (2006) 127-139
27. Huang S.H., and Radosz M. Equation of state for small, large, polydisperse, and associating molecules. Ind. Eng. Chem. Res. 29 (1990) 2284-2294
28. Cismondi M., Brignole E.A., and Mollerup J. Rescaling of three-parameters equation of state: PC-SAFT and SPHCT. Fluid Phase Equilib. 234 (2005) 108-121
29. Michelsen M.L., and Heidemann R.A. Calculation of tri-critical points. Fluid Phase Equilib. 39 (1988) 53-74
30. Wilkinson J.H. The Algebraic Eigenvalue Problem (1965), Clarendon, Oxford
31. Peters G., and Wilkinson J.H. Inverse iteration, ill-conditioned equations and Newton's method. SIAM Rev. 21 (1979) 339-360
32. Kohse B.F., and Heidemann R.A. Computation of tricritical points in ternary systems. AIChE J. 39 (1993) 1242-1256
33. Press W.H., Teukolsky S.A., Vetterling W.T., and Flannery B.P. Numerical Recipes in FORTRAN: The Art of Scientific Computing. 2nd ed. (1992), Cambridge University Press
34. Chen S., and Kreglewski A. Applications of the augmented van der Waals theory of fluids. I. Pure fluids. Ber. Bunsen. Phys. Chem. 81 (1977) 1048-1052
35. Chapman W.G., Jackson G., and Gubbins K.E. Phase equilibria of associating fluid chain molecules with multiple bonding sites. Mol. Phys. 65 (1988) 1057-1079
36. Chapman W.G., Gubbins K.E., Jackson G., and Radosz M. New reference equation of state for associating liquids. Ind. Eng. Chem. Res. 29 (1990) 1709-1721
37. Nelder J.A., and Mead R.A. A simplex method for function minimization. Comput. J. 7 (1965) 308-313
38. Wegstein J.H. Accelerating convergence for iterative processes. Commun. Assoc. Comp. Mach. 1 (1958) 9-13
39. Justo-García D.N., García-Sánchez F., Águila-Hernández J., and Eustaquio-Rincón R. Application of the simulated annealing technique to the calculation of critical points of multicomponent mixtures with cubic equations of state. Fluid Phase Equilib. 264 (2008) 164-173
40. Kolář P., and Kojima K. Prediction of critical points in multicomponent systems using the PSRK group contribution equation of state. Fluid Phase Equilib. 118 (1995) 175-200
41. García-Sánchez F., Ruiz-Cortina J.L., Lira-Galeana C., and Ponce-Ramírez L. Critical point calculations for oil reservoir fluid systems using the SPHCT equation of state. Fluid Phase Equilib. 81 (1992) 39-84
42. Holderbaum T., and Gmehling J. PSRK: a group contribution equation of state based on UNIFAC. Fluid Phase Equilib. 70 (1991) 251-265
43. Wichterle I., and Kobayashi R. Vapor-liquid equilibrium of methane-ethane system at low temperatures and high pressures. J. Chem. Eng. Data 17 (1972) 9-12
44. Wichterle I., and Kobayashi R. Vapor-liquid equilibrium of methane-ethane-propane system at low temperatures and high pressures. J. Chem. Eng. Data 17 (1972) 13-18
45. Davalos J., Anderson W.R., Phelps R.E., and Kidnay A.J. Liquid-vapor equilibria at 250.00 K for systems containing methane, ethane and carbon dioxide. J. Chem. Eng. Data 21 (1976) 81-84
46. Miller R.C., Kidnay A.J., and Hiza M.J. Liquid + vapor equilibria in methane + ethane and in methane + ethane from 150.00 to 190.00 K. J. Chem. Thermodyn. 9 (1977) 167-178
47. Reamer H.H., Sage B.H., and Lacey W.N. Phase equilibria inhydrocarbon systems. Volumetric and phase behavior of the methane-propane system. Ind. Eng. Chem. 42 (1950) 534-539
48. Wichterle I., and Kobayashi R. Vapor-liquid equilibrium of methane-propane system at low temperatures and high pressures. J. Chem. Eng. Data 17 (1972) 4-9
49. Olds R.H., Sage B.H., and Lacey W.N. Phase equilibria in hydrocarbon systems. Volumetric and phase behavior of methane-isobutane system. Ind. Eng. Chem. 34 (1942) 1008-1013
50. Sage B.H., Hicks B.L., and Lacey W.N. Phase equilibria in hydrocarbon systems. The methane-n-butane system in the two-phase region. Ind. Eng. Chem. 32 (1940) 1085-1092
51. Roberts L.R., Wang R.H., Azarnoosh A., and McKetta J.J. Methane-n-butane system in the two-phase region. J. Chem. Eng. Data 7 (1962) 484-485
52. Kahre L.C. Low-temperature K data for methane-n-butane. J. Chem. Eng. Data 19 (1974) 67-71
53. Elliot D.G., Chen R.J.J., Chappelear P.S., and Kobayashi R. Vapor-liquid equilibrium of methane-n-butane system at low temperatures and high pressures. J. Chem. Eng. Data 19 (1974) 71-77
54. Amick E.H., Johnson W.B., and Dodge B.F. P-V-T-x relationships for the system methane-isopentane. Chem. Eng. Prog. Symp. Ser. No. 3 48 (1952) 65-72
55. Prodany N.W., and Williams B. Vapor-liquid equilibria in methane-hydrocarbon systems. J. Chem. Eng. Data 16 (1971) 1-6
56. Sage B.H., Reamer H.H., Olds R.H., and Lacey W.N. Phase equilibria in hydrocarbon systems. Volumetric and phase behavior of the methane-n-pentane system. Ind. Eng. Chem. 34 (1942) 1108-1117
57. Kahre L.C. Low-temperature K data for methane-n-pentane. J. Chem. Eng. Data 20 (1975) 363-367
58. Chu T.-C., Chen R.J.J., Chappelear P.S., and Kobayashi R. Vapor-liquid equilibrium of methane-n-pentane system at low temperatures and high pressures. J. Chem. Eng. Data 21 (1976) 41-44
59. Reiff W.-E., Peters-Gerth P., and Lucas K. A static apparatus for (vapour-liquid) equilibrium measurements at high temperatures and pressures. J. Chem. Thermodyn. 19 (1987) 467-477
60. Shim J., and Kohn J.P. Multiphase and volumetric equilibria of the methane-n-hexane binary system between -110° and 150 °C. J. Chem. Eng. Data 7 (1962) 3-8
61. Gunn R.D., McKetta J.J., and Ata N. Measurement and prediction of high-pressure phase equilibria with a dilute component in the gas phase: the methane-n-hexane system. AIChE J. 20 (1974) 347-353
62. Lin Y.-N., Chen R.J.J., Chappelear P.S., and Kobayashi R. Vapor-liquid equilibrium of the methane-n-hexane system at low temperature. J. Chem. Eng. Data 22 (1977) 402-408
63. Srivastan S., Darwish N.A., Gasem K.A.M., and Robinson R.L. Solubility of methane in hexane, decane, and dodecane at temperatures from 311 to 423 K and pressures to 10.4 MPa. J. Chem. Eng. Data 37 (1992) 516-520
64. Uribe-Vargas V., and Trejo A. Vapor-liquid equilibrium in an equimolar hexane + decane mixture at temperatures of 258, 273, and 298 K and pressures to 20 MPa. Fluid Phase Equilib. 220 (2004) 137-145
65. Reamer H.H., Sage B.H., and Lacey W.N. Phase equilibria in hydrocarbon systems. Volumetric and phase behavior of the methane-heptane system. Ind. Eng. Chem., Chem. Eng. Data Ser. 1 (1956) 29-42
66. Chang H.L., Hurt L.J., and Kobayashi R. Vapor-liquid equilibria of light hydrocarbon at low temperatures and high pressures: the methane-n-heptane system. AIChE J. 12 (1966) 1212-1216
67. Kohn J.P., and Bradish W.F. Multiphase and volumetric equilibria of the methane-n-octane system at temperatures between -110 and 150 °C. J. Chem. Eng. Data 9 (1964) 5-8
68. Shipman L.M., and Kohn J.P. Heterogeneous phase and volumetric equilibrium in the methane-n-nonane system. J. Chem. Eng. Data 11 (1966) 176-180
69. Rousseaux P., Richon D., and Renon H. A static method for determination of vapour-liquid equilibria at high pressures and temperatures using a new variable volume cell. Fluid Phase Equilib. 11 (1983) 153-168
70. Reamer H.H., Olds R.H., Sage B.H., and Lacey W.N. Phase equilibria in hydrocarbon systems. Volumetric and phase behavior of the methane-n-decane system. Ind. Eng. Chem. 34 (1942) 1526-1531
71. Koonce K.T., and Kobayashi R. A method for determining the solubility of gases in relatively nonvolatile liquids: the solubility of methane in n-decane. J. Chem. Eng. Data 9 (1964) 490-494
72. Lin H.-H., Sebastian H.M., Simnick J.J., and Chao K.-C. Gas-liquid equilibrium in binary mixtures of methane with n-decane, benzene, and toulene. J. Chem. Eng. Data 24 (1979) 146-149
73. Matschke D.E., and Thodos G. Vapor-liquid equilibria for the ethane-propane system. J. Chem. Eng. Data 7 (1962) 232-324
74. Uchytil P., and Wichterle I. Liquid-vapour critical region of the most volatile component of a ternary system. I. Vapour-liquid equilibria in the ethane-propane-n-butane system. Fluid Phase Equilib. 15 (1983) 209-217
75. Blanc C.J., and Setier J.-C.B. Vapor-liquid equilibria for the ethane-propane system at low temperature. Chem. Eng. Data 33 (1988) 111-115
76. Besserer G.J., and Robinson D.B. Equilibrium-phase properties of i-butane-ethane. J. Chem. Eng. Data 18 (1973) 301-304
77. Kay W.B. Liquid-vapor equilibrium relations in binary systems. The ethane-n-butane system. Ind. Eng. Chem. 32 (1940) 353-357
78. Dingrani J.G., and Thodos G. Vapor-liquid equilibrium behavior of the ethane-n-butane-n-hexane system. Can. J. Chem. Eng. 56 (1978) 616-623
79. Mehra V.S., and Thodos G. Vapor-liquid Equilibrium in the system ethane-n-butane system. J. Chem. Eng. Data 10 (1978) 307-309
80. Lhotak V., and Wichterle I. Vapour-liquid equilibria in the ethane-n-butane system at high pressures. Fluid Phase Equilib. 6 (1981) 229-235
81. Reamer H.H., Sage B.H., and Lacey W.N. Phase equilibria in hydrocarbon systems. Volumetric and phase behavior of the ethane-n-pentane system. J. Chem. Eng. Data 5 (1960) 44-50
82. Zais E.J., and Silberberg I.H. Vapor-liquid equilibria in the ethane-n-hexane system. J. Chem. Eng. Data 15 (1970) 253-256
83. Ohgaki K., Sano F., and Katayama T. Isothermal vapor-liquid equilibrium data for binary systems containing ethane at high pressures. J. Chem. Eng. Data 21 (1976) 55-58
84. Kay W.B. Liquid-vapor phase equilibrium relations in the ethane-n-heptane system. Ind. Eng. Chem. 30 (1938) 459-465
85. S.P. Dastur. Experimental vapor-liquid equilibrium study for the ethane-n-pentane-n-heptane system. Prediction of the K-values for ternary and quaternary systems. Doctoral Dissertation, Northwestern Univ. Evanston, Illinois, 1964.
86. Rodrigues A.B.J., McCaffrey Jr. D.S., and Kohn J.P. Heterogeneous phase and volumetric equilibrium in the ethane-n-octane. J. Chem. Eng. Data 13 (1968) 164-168
87. Reamer H.H., and Sage B.H. Phase equilibria in hydrocarbon systems. Volumetric and phase behavior of the ethane-n-decane system. J. Chem. Eng. Data 7 (1962) 161-168
88. Bufkin B.A., Robinson Jr. R.L., Estrera S.S., and Luks K.D. Solubility of ethane in n-decane at pressures to 8.2 MPa and temperatures from 278 to 411 K. J. Chem. Eng. Data 31 (1986) 412-423
89. Hipkin H. Vapor-liquid equilibrium data for propane-isobutane. AIChE J. 12 (1966) 484-487
90. Kay W.B. Vapor-liquid equilibrium relations of binary systems. Propane-n-alkane systems: n-butane and n-pentane. J. Chem. Eng. Data 15 (1970) 46-52
91. Vaughan W.E., and Collins F.C. P-V-T-x relations of the system propane-isopentane. Ind. Eng. Chem. 34 (1942) 885-890
92. Sage B.H., and Lacey W.N. Phase equilibria in hydrocarbon systems. Propane-n-pentane system. Ind. Eng. Chem. 32 (1940) 992-996
93. Kay W.B. Vapor-liquid equilibrium relations of binary systems. Propane-n-alkane systems: n-hexane and n-heptane. J. Chem. Eng. Data 16 (1971) 137-139
94. Kay W.B., Genco J., and Fichtner D.A. Vapor-liquid relationships of binary systems. Propane-n-octane and n-butane-n-octane. J. Chem. Eng. Data 19 (1974) 275-280
95. Reamer H.H., and Sage B.H. Phase equilibria in hydrocarbon systems. Volumetric and phase behavior of the propane-n-decane system. J. Chem. Eng. Data 11 (1966) 17-24
96. Kay W.B., Hoffman R.L., and Davies O. Vapor-liquid equilibrium relationships of binary systems. n-Butane-n-pentane and n-butane-n-hexane. J. Chem. Eng. Data 20 (1975) 333-338
97. L.W. Cummins. D.Sc. Thesis, Mass. Inst. Tech, 1933.
98. Kay W.B. Liquid-vapor equilibrium relations in binary systems. n-Butane-n-heptane system. Ind. Eng. Chem. 33 (1941) 590-594
99. Reamer H.H., and Sage B.H. Phase equilibria in hydrocarbon systems. Phase behavior in the n-butane-n-decane system. J. Chem. Eng. Data 9 (1964) 24-28
100. Donelly H.G., and Katz D.L. Phase equilibria in the carbon dioxide-methane system. Ind. Eng. Chem. 46 (1954) 511-517
101. Neumann A., and Walch W. Vapor-liquid equilibria of carbon dioxide/methane at low temperatures and in the region of low carbon dioxide mole fractions. Chem. Eng. Technol. 40 (1968) 241
102. 2 system at low temperatures. J. Chem. Eng. Data 23 (1978) 135-139
103. Somait F.A., and Kidnay A.J. Liquid-vapor equilibria at 270.00 K for systems containing nitrogen, methane, and carbon dioxide. J. Chem. Eng. Data 23 (1978) 301-305
104. 4 system. J. Chem. Eng. Data 22 (1983) 372-380
105. Wei S.-W., Brown T.S., Kidnay A.J., and Sloan E.D. Vapor + liquid equilibria for the ternary methane + ethane + carbon dioxide at 230 K and its constituent binaries at temperatures from 207 to 270 K. J. Chem. Eng. Data 40 (1995) 726-731
106. Webster L.A., and Kidnay A.J. Vapor-liquid equilibria for the methane-propane-carbon dioxide system at 230 and 270 K. J. Chem. Eng. Data 46 (2001) 759-764
107. Gugnoni R.J., Eldridge J.W., Okay V.C., and Lee T.J. Carbon dioxide-ethane phase equilibria and densities from experimental measurements and the B-W-R equation. AIChE J. 20 (1974) 357-362
108. 2 system. J. Chem. Soc., Faraday Trans. I 70 (1974) 1653-1660
109. Haman S.E.M., and Lu B.C.-Y. Vapor-liquid equilibrium in the ethane-carbon dioxide system. Can. J. Chem. Eng. 52 (1974) 283-286
110. Nagahama K., Konishi H., Hoshino D., and Hirata M. Binary vapor-liquid equilibria of carbon dioxide-light hydrocarbons at low temperature. J. Chem. Eng. Jpn. 7 (1974) 323-329
111. Robinson D.B., and Kalra H. The phase behavior of selected hydrocarbon-non-hydrocarbon systems. Proc. 53rd Annual GPA Convention. Denver, Colorado (1974) 14-20
112. Ohgaki K., and Katayama T. Isothermal vapor-liquid equilibrium data for the ethane-carbon dioxide system at high pressures. Fluid Phase Equilib. 1 (1977) 27-32
113. Brown T.S., Kidnay A.J., and Sloan E.D. Vapor-liquid equilibria in the carbon dioxide-ethane system. Fluid Phase Equilib. 40 (1988) 169-184
114. Poettmann F.H., and Katz D.L. Phase behavior of binary carbon dioxide-paraffin systems. Ind. Eng. Chem. 37 (1945) 847-853
115. Reamer H.H., Sage B.H., and Lacey W.N. Phase equilibria in hydrocarbon systems. Volumetric and phase equilibria of the propane-carbon dioxide system. Ind. Eng. Chem. 43 (1951) 2515-2520
116. Akers W.W., Kelley R.E., and Lipscomb T.G. Low temperature phase equilibria of the carbon dioxide-propane system. Ind. Eng. Chem. 46 (1954) 2535-2536
117. Haman S.E.M., and Lu B.C.-Y. Isothermal vapor-liquid equilibria in the binary system propane-carbon dioxide. J. Chem. Eng. Data 21 (1976) 200-204
118. Niesen V.G., and Rainwater J.C. Critical locus, (vapor + liquid) equilibria, and coexisting densities of (carbon dioxide + propane) at temperatures from 311 to 361 K. J. Chem. Thermodyn. 22 (1990) 777-795
119. Yucelen B., and Kidnay A.J. Vapor-liquid equilibria in the nitrogen + carbon dioxide + propane system from 240 to 330 K at pressures to 15 MPa. J. Chem. Eng. Data 44 (1999) 926-931
120. Besserer G.J., and Robinson D.B. Equilibrium-phase properties of n-pentane-carbon dioxide system. J. Chem. Eng. Data 18 (1973) 416-419
121. Leu A.-D., and Robinson D.B. Equilibrium phase properties of the n-butane-carbon dioxide and isobutene-carbon dioxide binary systems. J. Chem. Eng. Data 32 (1987) 444-447
122. Weber L.A. Simple apparatus for vapor-liquid equilibrium measurements with data for the binary systems of carbon dioxide with n-butane and isobutane. J. Chem. Eng. Data 34 (1989) 171-175
123. Kalra H., Krishnan T.R., and Robinson D.B. Equilibrium phase properties of carbon dioxide-n-butane and nitrogen-hydrogen sulfide systems at subambient temperatures. J. Chem. Eng. Data 21 (1976) 222-225
124. 2 + n-butane. J. Chem. Eng. Data 30 (1985) 485-491
125. Shibata S.K., and Sandler S.I. High-pressure vapor-liquid equilibria involving mixtures of nitrogen, carbon dioxide, and n-butane. J. Chem. Eng. Data 34 (1989) 291-298
126. Niesen V.G. (Vapor + liquid) equilibria and coexistence densities of (carbon dioxide + n-butane) at 311 to 395 K. J. Chem. Thermodyn. 21 (1989) 915-923
127. Pozo M.E., Zollweg J.A., and Streett W.B. Vapor-liquid equilibrium in the binary system carbon-dioxide + n-butane. J. Chem. Eng. Data 34 (1989) 324-328
128. T.S. Brown, Experimental and calculated vapor-liquid and fluid-fluid equilibria in natural gas systems. Ph.D Thesis. Colorado School of Mines, Golden. Colorado, 1990.
129. Besserer G.J., and Robinson D.B. Equilibrium phase properties of isopentane-carbon dioxide system. J. Chem. Eng. Data 20 (1975) 93-96
130. Leu A.-D., and Robinson D.B. Equilibrium phase properties of selected carbon dioxide binary systems: n-pentane-carbon dioxide and isopentane-carbon dioxide. J. Chem. Eng. Data 32 (1987) 447-450
131. Cheng H., Pozo M.E., Zollweg J.A., and Streett W.B. Vapor-liquid equilibrium in the system carbon dioxide + n-pentane from 252 to 458 K at pressures to 10 MPa. J. Chem. Eng. Data 34 (1989) 319-323
132. Im U.K., and Kurata F. Heterogeneous phase behavior of carbon dioxide in n-hexane and n-heptane at low temperatures. J. Chem. Eng. Data 16 (1971) 412-415
133. Ohgaki K., and Katayama T. Isothermal vapor-liquid equilibrium data for binary systems containing carbon dioxide at high pressures: methanol-carbon dioxide, n-hexane-carbon dioxide, and benzene-carbon dioxide systems. J. Chem. Eng. Data 21 (1976) 53-55
134. Li Y.-H., Dillard K.H., and Robinson Jr. R.L. Vapor-liquid phase equilibrium for carbon dioxide-n-hexane at 40, 80, and 120 °C. J. Chem. Eng. Data 26 (1981) 53-55
135. Kaminishi G.-I., Yokoyama C., and Takahashi S. Vapor pressures of binary mixtures of carbon dioxide with benzene, n-hexane, and cyclohexane up to 7 MPa. Fluid Phase Equilib. 34 (1987) 83-99
136. Wagner Z., and Wichterle I. High-pressure vapour-liquid equilibrium in systems containing carbon dioxide, 1-hexene, and n-hexane. Fluid Phase Equilib. 33 (1987) 109-123
137. Kalra H., Kubota H., Robinson D.B., and Ng H.-J. Equilibrium phase properties of the carbon dioxide-n-heptane system. J. Chem. Eng. Data 23 (1978) 317-321
138. Stewart W.C., and Nielsen R.F. Phase equilibria for mixtures of carbon dioxide and several normal saturated hydrocarbons. Prod. Monthly (1954) 27-32
139. King M.B., Alderson D.A., Fallah F.H., Kassim D.M., Kassim A.M., Sheldom J.R., and Mahmud R.S. Some vapor/liquid and vapor/solid equilibrium measurements of relevance for supercritical extraction operations and their correlation. In: Paulaitis, et al. (Ed). Chemical Engineering at Supercritical Conditions (1983), Ann Arbor Sci. Publishers
140. Weng W.L., and Lee M.J. Vapor-liquid equilibrium of the octane/carbon dioxide, and octane/ethylene systems. J. Chem. Eng. Data 37 (1992) 213-215
141. 2 system. J. Chem. Eng. Data 8 (1963) 508-513
142. Sebastian H.M., Simnick J.J., Lin H.-M., and Chao K.-C. Vapor-liquid equilibrium in binary mixtures of carbon dioxide + n-decane and carbon dioxide + n-hexadecane. J. Chem. Eng. Data 25 (1980) 138-140
143. B. Bufkin, High-pressure solubilities of carbon dioxide and ethane in selected paraffinic, naphthenic and aromatic solvents. M.Sc. Thesis, Oklahoma State University, 1986.
144. Nagarajan N., and Robinson Jr. R.L. Equilibrium phase compositions, phase densities, and interfacial tensions for CO2 + hydrocarbon systems. 2. CO2 + n-decane. J. Chem. Eng. Data 31 (1986) 168-171
145. 2/n-decane/tetralin at 71.1 and 104.4 °C. J. Chem. Eng. Data 35 (1990) 26-29
146. Zenner G.H., and Dana L.I. Liquid-vapor equilibrium compositions of carbon dioxide-nitrogen mixtures. Chem. Eng. Prog. Symp. Ser. No. 59 44 (1963) 36-41
147. Yorizane M., Yoshimura S., Masuoka H., Miyano Y., and Kakimoto Y. New procedure for vapor-liquid equilibria. Nitrogen + carbon dioxide, methane + freon 22, and methane + freon 12. J. Chem. Eng. Data 30 (1985) 174-176
148. Brown T.S., Sloan E.D., and Kidnay A.J. Vapor-liquid equilibria in the nitrogen + carbon dioxide + ethane system. Fluid Phase Equilib. 51 (1989) 299-313
149. Ekiner O., and Thodos G. Critical temperatures and pressures of the ethane-n-butane-n-heptane system. J. Chem. Eng. Data 13 (1968) 304-306
150. Ekiner O., and Thodos G. Critical temperatures and critical pressures for the ethane-n-pentane-n-heptane system. J. Chem. Eng. Data 11 (1966) 457-460
151. Yarborough L., and Smith R.L. Solvent and driving gas compositions for miscible slug displacement. Soc. Pet. Eng. J. 10 (1970) 298-305
152. Etter D.O., and Kay W.B. Critical properties of mixtures of normal paraffin hydrocarbons. J. Chem. Eng. Data 6 (1961) 409-413
153. O. Ekiner, Critical temperatures and pressures for multicomponent hydrocarbon systems. Ph.D. Thesis, Northwestern University, Evanston, Illinois, 1965.
154. Gonzalez M.H., and Lee A.L. Dew and bubble points of simulated natural gases. J. Chem. Eng. Data 13 (1968) 172-176
155. D.W. Hissong, A thermodynamic analysis of the critical properties of hydrocarbon mixtures. Ph.D. Thesis, Ohio State University, Ohio, 1968.
156. Hanson G.H., and Brown G.G. Vapor-liquid equilibria in mixtures of volatile paraffins. Ind. Eng. Chem. 37 (1945) 821-825
157. Davis P.C., Bertuzzi A.F., Gore T.L., and Kurata F. The phase and volumetric behavior of natural gases at low temperatures and high pressures. Pet. Trans. AIME 201 (1954) 245-250