References
1. A. Akerberg, CFD analyses of the gas flow inside the vessel of a hot isostatic press, Master of Science Thesis, KTH School of Industrial Engineering and Management, Stockholm, Sweden, 2012.
2. M.A. Trebble and P.R. Bishnoi, “Accuracy and consistency comparisons of ten cubic equations of state for polar and non-polar compounds”, Fluid Phase Equilibria, vol. 29, pp. 465–474, 1986.
3. B.E. Poling, J.M. Prausnitz, and J.P. O’Connell, The Properties of Gases and Liquids, McGraw Hill, international edition, 2007.
4. M.C. Clapeyron, “Mémoire sur la puissance motrice de la chaleur,” Journal de l’École polytechnique, vol. 23, pp. 153–190, 1834 (in French).
5. D.Y. Peng and D. Robinson, “A new two-constant equation of state,” Industrial and Engineering Chemistry: Fundamentals, vol. 15, pp. 59–64, 1976.
6. C.H. Twu, J.E. Coon, and J.R. Cunningham, “A new generalized alpha function for a cubic equation of state, Part 1, Peng–Robinson equation,” Fluid Phase Equilibria, vol. 105, pp. 49–59, 1995.
7. O. Redlich and J.N.S. Kwong, “On the thermodynamics of solutions an equation of state, fugacities of gaseous solutions,” Chem. Rev., vol. 44, no. 1, pp. 233–244, 1949.
8. G. Soave, “Equilibrium constants from a modified Redlich–Kwong equation of state,” Chem. Eng. Sci., vol. 27, no. 6, pp. 1197–1203, 1972.
9. M.S. Graboski and T.E. Daubert, “A modified Soave equation of state for phase equilibrium calculations, 3, systems containing hydrogen,” Ind. Eng. Chem. Process. Des. Dev., vol. 18, no. 2, pp. 300–306, 1979.
10. J.R. Cooper, “Revised Release on the IAPWS Industrial Formulation 1997 for the Thermodynamic Properties of Water and Steam”, The International Association for the Properties of Water and Steam, IAPWS R7-97, 2012.
11. K. Watanabe, “Revised Supplementary Release on Backward Equations for the Functions T(p,h), v(p,h) and T(p,s), v(p,s) for Region 3 of the IAPWS Industrial Formulation 1997 for the Thermodynamic Properties of Water and Steam,” The International Association for the Properties of Water and Steam, Kyoto, Japan, Sep. 2004.
12. F. Marsik, “Supplementary Release on Backward Equations for Specific Volume as a Function of Pressure and Temperature v(p,T) for Region 3 of the IAPWS Industrial Formulation 1997 for the Thermodynamics Properties of Water and Steam,” The International Association for the Properties of Water and Steam, Santorini, Greece, July 2005.
13. K.C. Chao and J.D. Seader, “A general correlation of vapor-liquid equilibria in hydrocarbon mixtures,” AIChE J., vol. 7, no. 4, pp. 598–605, 1961.
14. J.H. Hildebrand and R.L. Scott, “The solubility of non-electrolytes,” J. Phys. Chem., vol. 55, no. 4, pp. 619–620, 1951.
15. H.G. Grayson and C.W. Streed, “Vapor-liquid equilibria for high temperature, high pressure hydrogen-hydrocarbon systems,” 6th World Petroleum Congress, 19–26 June, Frankfurt am Main, Germany, IV, pp. 169–180, 1963.
16. J.H. Hildebrand, J.M. Prausnitz, and R.L. Scott. Regular and Related Solutions, Van Nostrand Reinhold Co., 1970.
17. G.M. Wilson, “Vapor-liquid equilibrium. xi. a new expression for the excess free energy of mixing,” J. Am. Chem. Soc., vol. 86, pp. 127–130, 1964.
18. H. Renon and J.M. Prausnitz, “Local compositions in thermodynamic excess functions for liquid mixtures,” AIChE J., vol. 14, no. 1, pp. 135–144, 1968.
19. D.S. Abrams and J.M. Prausnitz, “Statistical thermodynamics of liquid mixtures: A new expression for the excess Gibbs energy of partly or completely miscible systems,” AIChE J., vol. 21, no. 1, pp. 116–128, 1975.
20. A. Fredenslund, R.L. Jones, and J.M. Prausnitz, “Group-contribution estimation of activity coefficients in nonideal liquid mixtures,” AIChE J., vol. 21, no. 6, pp. 1086–1099, 1975.
21. S. Skjold-Joergensen, B. Kolbe, J. Gmehling, and P. Rasmussen, “Vapor-liquid equilibria by unifac group contribution. revision and extension,” Ind. Eng. Chem. Process. Des. Dev., vol. 18, no. 4, pp. 714–722, 1979.
22. J. Gmehling, P. Rasmussen, and A. Fredenslund, “Vapor-liquid equilibria by unifac group contribution. revision and extension. 2,” Ind. Eng. Chem. Process. Des. Dev., vol. 21, no. 1, pp. 118–127, 1982.
23. E.A. Macedo, U. Weidlich, J. Gmehling, and P. Rasmussen, “Vapor-liquid equilibria by unifac group contribution. 3. Revision and extension,” Ind. Eng. Chem. Process. Des. Dev., vol. 22, no. 4, pp. 676–678, 1983.
24. D. Tiegs, J. Gmehling, P. Rasmussen P, and A. Fredenslund, “Vapor-liquid equilibria by unifac group contribution. 4. Revision and extension,” Ind. Eng. Chem. Process. Des. Dev., vol. 26, no. 1, pp. 159–161, 1987.
25. H.K. Hansen, P. Rasmussen, A. Fredenslund, M. Schiller, and J. Gmehling, “Vapor-liquid equilibria by unifac group contribution. 5. Revision and extension,” Ind. Eng. Chem. Process. Des. Dev., vol. 30, no. 10, pp. 2352–2355, 1991.
26. R. Wittig, J. Lohmann, and J. Gmehling, “Vapor-liquid equilibria by unifac group contribution. 6. Revision and extension,” Ind. Eng. Chem. Process. Des. Dev., vol. 42, no. 1, pp. 183–188, 2003.
27. K. Balslev and J. Abildskov, “Unifac parameters for four new groups,” Ind. Eng. Chem. Res., vol. 41, pp. 2047–2057, 2002.
28. R.W. Hankinson and G.H. Thomson, “A new correlation for saturated densities of liquid and their mixtures,” AIChE J., vol. 25, no. 4, pp. 653–663, 1979.
29. H.G. Rackett, “Equation of state for saturated liquids,” J. Chem. Eng. Data, vol. 15, no. 4, pp. 514–517, 1970.
30. L.I. Stiel and G. Thodos, “The thermal conductivity of nonpolar substances in the dense gaseous and liquid regions,” AIChE J., vol. 10, no. 1, pp. 26–30, 1964.
31. M. Yorizane, S. Yoshimura, H. Masuoka, and H. Yoshida, “Thermal conductivities of binary gas mixtures at high pressures: nitrogen-oxygen, nitrogen-argon, carbon dioxide-argon, and carbon dioxide-methane,” Industrial & Engineering Chemistry Fundamentals, vol. 22, no. 4, pp. 458–463, 1983.
32. A.L. Lindsay and L.A. Bromley, “Thermal conductivity of gas mixtures,” Industrial and Engineering Chemistry, vol. 42, no. 8, pp. 1508–1511, 1950.
33. A. Wassiljewa, “Heat conduction in gas mixtures,” Physikalische Zeitschrift, vol. 5, no. 22, pp. 737–742, 1904.
34. J.R. Cooper, “Release on the IAPS Formulation 1985 for the Thermal Conductivity of Ordinary Water Substance,” The International Association for the Properties of Water and Steam, Berlin, Germany, Sep. 2008.
35. C.R. Wilke, “A viscosity equation for gas mixtures,” J. Chem. Phys., vol. 18, no. 4, pp. 517– 520, 1950.
36. R.S. Brokaw, “Approximate formulas for the viscosity and thermal conductivity of gas mixtures. ii,” J. Chem. Phys., vol. 42, no. 4, pp. 1140–1147, 1965.
37. J.E. Lennard–Jones, “On the determination of molecular fields 1. from the variation of the viscosity of a gas with temperature,” Proceedings of the Royal Society of London. Series A, Containing Papers of a Mathematical and Physical Character, vol. 106, pp. 441–462, 1924.
38. W.H. Stockmayer, “Second virial coefficients of polar gases,” J. Chem. Phys., vol. 9, pp. 398–402, 1941.
39. F.M. Mourits and F.H.A. Rummens, “A critical evaluation of Lennard–Jones and Stockmayer potential parameters and of some correlation methods,” Can. J. Chem. Eng., vol. 55, pp. 3007–3020, 1977.
40. T.A. Davidson, “A Simple and Accurate Method for Calculating Viscosity of Gaseous Mixtures”, Report of Investigations 9456, United States Department of the Interior, Bureau of Mines, 1993.
41. J.A. Jossi, L.I. Stiel, and G. Thodos, “The viscosity of pure substances in the dense gaseous and liquid phases,” AIChE J., vol. 8, no. 1, pp. 59–63, 1962.
42. K.S. Pedersen and P.L. Christensen, “Phase Behavior of Petroleum Reservoir Fluids,” CRC Press/Taylor & Francis Group, 2007.
43. K.S. Pedersen, A. Fredenslund, P.L. Christensen, and P. Thomassen, “Viscosity of crude oils,” Chem. Eng. Sci., vol. 39, no. 6, pp. 1011–1016, 1984.
44. H.J.M. Hanley, W.M. Haynes, and R.D. McCarty, “The viscosity and thermal conductivity coefficients for dense gaseous and liquid methane,” J. Chem. Phys., vol. 6, no. 2, pp. 597–609, 1977.
45. K.S. Pedersen and A. Fredenslund, “An improved corresponding states model for the prediction of oil and gas viscosities and thermal conductivities,” Chem. Eng. Sci., vol. 42, no. 1, pp. 182–186, 1987.
46. R.D. McCarty, “A modified Benedict-Webb-Rubin equation of state for methane using recent experimental data,” Cryogenics, pp. 276–280, May 1974.
47. S. Murad and K.E. Gubbins, “Corresponding states correlation for thermal conductivity of dense fluids,” Chem. Eng. Sci., vol. 32, no. 5, pp. 499–505, 1977.
48. J.R. Cooper, “Revised Release on the IAPWS Formulation 2008 for the Viscosity of Ordinary Water Substance”, The International Association for the Properties of Water and Steam, Berlin, Germany, Sep. 2008.
49. K. Daucik, “Revised Release on the Pressure along the Melting and Sublimation Curves of Ordinary Water Substance”, The International Association for the Properties of Water and Steam, Plzen, Czech Republic, Sep. 2011.
50. J. Gabitto and M. Barrufet, “Experimental and theoretical determination of heavy oil viscosity under reservoir conditions,” Technical reports, Office of Fossil Energy, USDOE Office of Fossil Energy, United States, 2002.
51. A. Missenard, “Conductivité thermique des liquides organiques d’une serie ou d’un ‘groupe de liquides’,” Revue Générale de Thermique, vol. 101, no. 5, pp. 649–660, 1970 (in French).
52. R.L. Rowley, G.L. White, and M. Chiu, “Ternary liquid mixture thermal conductivities,” Chem. Eng. Sci., vol. 43, no. 2, pp. 361–371, 1988.
53. R.L. Rowley, “A local composition model for multicomponent liquid mixture thermal conductivities,” Chem. Eng. Sci., vol. 37, no. 6, pp. 897–904, 1982.
54. W.D. Niven, “The Scientific Papers of James Clerk Maxwell”, Cambridge University Press, 1890.
55. J.C. Maxwell, “On the dynamical theory of gases,” Philos. Trans. R. Soc., vol. 157, pp. 49–88, 1867.
56. J. Stefan, “Uber das Gleichgewicht und die Bewegung, insbesondere die Diffusion von Gasgemengen,” Sitzungsbrichte der Kaiserlichen Akademie der Wissenschaften Wien, 2te Abteilung a, vol. 63, pp. 63–124, 1871.
57. R. Taylor and R. Krishna, “Multicomponent Mass Transfer,” Wiley-Interscience, 1993.
58. E.N. Fuller, P.D. Schettler and J.C. Giddings, “A new method for prediction of binary gas-phase diffusion coefficients,” Industrial and Engineering Chemistry, vol. 5, pp. 19–27, 1966.
59. E.N. Fuller, K. Ensley and J.C. Giddings, “Diffusion of halogenated hydrocarbons in helium. The effect of structure on collision cross sections,” J. Phys. Chem., vol. 73, no. 11, pp. 3679–3685, 1969.
60. C.R. Wilke and C.Y. Lee, “Estimation of diffusion coefficients for gases and vapors,” Industrial and Engineering Chemistry, vol. 47, no. 6, pp. 1253–1257, 1955.
61. P.D. Neufeld, A.R. Janzen, and R.A. Aziz, “Empirical equations to calculate 16 of the transport collision integrals for the Lennard–Jones (12-6) potential,” J. Chem. Phys., vol. 57, pp. 1100–1102, 1972.
62. C.R. Wilke and P. Chang, “Correlation of diffusion coefficients in dilute solutions,” AICHE J., vol. 1, no. 2, pp. 264–270, 1972.
63. W. Hayduk and H. Laudie, “Prediction of diffusion coefficients for nonelectrolytes in dilute aqueous solutions,” AICHE J., vol. 20, no. 3, pp. 611–615, 1974.
64. H.A. Kooijman, “A modification of the Stokes-Einstein equation for diffusivities in dilute binary mixture,” Ind. Eng. Chem., vol. 41, pp. 3326–3328, 2002.
65. M.T. Tyn and W.F Calus, “Diffusion coefficients in dilute binary mixtures,” J. Chem. Eng. Data, vol. 20, no. 1, pp. 106–109, 1975.
66. W.Hayduk and B.S.Minhas, “Correlation for prediction of molecular diffusivities in liquids,” Can. J. Chem. Eng., vol. 60, no. 2, pp. 295–299, 1983.
67. M.A. Siddiqi and K. Lucas, “Correlations for prediction of diffusion in liquids”, Can. J. Chem. Eng., vol. 64, pp. 839–843, 1986.
68. C. Erkey, J.B. Rodden and A. Akgerman, “A correlation for predicting diffusion coefficients in alkanes”, Can. J. Chem. Eng., vol. 68, pp. 661–665, 1990.
69. A. Bondi, “van der Waals Volumes and Radii”, J. Phys. Chem., vol. 68, no. 3, pp. 441-451, 1964.
70. J.O. Hirschfelder, C.F. Curtiss and R.B. Bird, “The Molecular Theory of Gases and Liquids”, Wiley-Interscience, 1964.
71. A. Vignes, “Diffusion in Binary Solutions,” Ind. Eng. Chem. Fundam., vol. 5, pp. 189–199, 1966.
72. J.A. Wesselingh and R. Krishna, “Mass Transfer”, Ellis Horwood Ltd, 1990, ISBN: 0-13-553165-9.
73. H.A. Kooijman and R. Taylor, “Estimation of diffusion coefficients in multicomponent liquid systems”, Ind. Eng. Chem., vol. 30, pp. 1217–1222, 1991.
74. J.A. Wesselingh and A.M. Bollen, “Multicomponent diffusivities from the free volume theory”, Chem. Eng. Res. Des., vol. 75, no. 6, pp. 590–602, 1997.
75. R. Krishna and J.M. van Baten, “The Darken relation for multicomponent diffusion in liquid mixtures of linear alkanes: An investigation using molecular dynamics (MD) simulations,” Ind. Eng. Chem., vol. 44, pp. 6939–6947, 2005.
76. P.H. Winterfeld, L.E. Scriven, and H.T. Davis, “An approximate theory of interfacial tension of multicomponent systems: Applications binary liquid-vapor tensions,” AICHE J., vol. 24, no. 6, pp. 1010–1014, 1978
77. E.C. Carlson, “Don’t Gamble With Physical Properties For Simulation”, Chem. Eng. Prog., vol. 92, no. 10, pp. 35–46, 1996.