[1] Meng L., Duan Y.Y., Prediction of the Second Cross Virial Coefficients of Nonpolar Binary Mixtures, Fluid Phase Equilib., 238, p. 229 (2005).
[2] Abbott M.M., Cubic Equations of State: An Interpretative Review, Adv. In Chem. Ser., 182, p. 47 (1979).
[3] Shan V.M., Lin Y.L., Cochran H.D., A Generalized Quartic Equation of State, Fluid Phase Equilib, 116, p. 87 (1996).
[4] Benedict M., Webb GB., Rubin L.C., An Empirical Equation for Thermodynamic Properties of Light Hydrocarbons and Their Mixtures: I.Methane, Ethane, Propane, and n-Butane, J. Chem. Phys, 8, p. 334 (1940).
[5] Benedict M., Webb G.B., Rubin L.C.,II. Mixtures of Methane, Ethane, Propane and n-Butane, J. Chem. Phys., 10, p. 747 (1942).
[6] Kedge C.J., Trebble M.A., Development of a New Empirical Non-Cubic Equation of State, Fluid Phase Equilib., 219, p. 158 (1999).
[7] SetzmanU., Wagner W., A New Method for Optimizing the Structure of Thermodynamic Correlation Equations, Int. J. Thermophys, 10, p. 1103 (1989).
[8] Prausnitz J.M., Lichtenthaler R.N., de Azevedo E.G., “Molecular Thermodynamics of Fluid Phase Equilibria”, 3rd Ed, N. J, Prentice-Hall (1999).
[9] Morrison G, McLinden M.O., Azeotropy in Refrigerant Mixtures, Int. J. Refring, 16, p. 129 (1993).
[10] Plyasunov A.V., Shock E.L., Wood R.H., Second Cross Virial Coefficients, J. Chem. Eng. Data, 48,
p. 1463 (2003).
[11] Lee B.I., Kesler M.G., A Generalized Thermodynamic Correlation Based on Three-Parameter Corresponding States, AICHE. J., 21, p. 510 (1975).
[12] Benedict M., Webb G.B., Rubin L.C., An Emprirical Equation for Thermodynamic Properties of Light Hydrocarbons and Their Mixtures, Chem. Eng. Prog., 47, p. 419 (1951).
[13] Mohebbi A., Mohammadikhah R.,A Simple Equation of State for Calculating the Compressibility Factor of Pure Fluids Based on the Virial EOS, J. Phys. Chem: An Ind. J., 2 (1), p. 1 (2007).
[14] Pitzer K.S., Curl R.F., The Volumetric and Thermodynamic Properties of fluids. III. Empirical Equation for the Second Virial Coefficient, J. Am. Chem. Soc., 79, 2369 (1957).
[15] Vetere A., An Improved Method to Predict the Second Virial. Coefficients of Pure Compounds, Fluid Phase Equilib, 164, p. 49 (1999).
[16] Caligaris R.E., Henderson D., Third Virial Coefficients of Ar+Kr and Kr+Xe Mixtures, Molec.Phys, 30, p. 1853 (1975).
[17] Reddy M.R., O´Shea S.F., Cardini G., Analytical Approximations to Virial Coefficients for Pure and Mixed Systems, Molec. Phys, 57, p. 841 (1985).
[18] Johnston H.L., Weimer H.R., Low Pressure Data of State of Nitric Oxide and of Nitrous Oxide Between Their Boiling Points and Room Temperature, J. Am. Chem. Soc, 56, p. 625 (1934).
[19] Nicola G.D., Giuliani G., Polonara F., Stryjek R., Second and Third Virial Coefficients for the R41+N_{2}O System, Fluid Phase Equilib., 228, p. 373 (2005).
[20] Tsonopoulos G., Second Virial Coefficients of Polar Holoalkanes, AICHE. J., 21, p. 827 (1975).
[21] Meng L., Duan Y.Y., Li L., Correlations for Second and Third Virial Coefficients of Pure Fluids, Fluid Phase Equilib., 226, p. 109 (2004).
[22] Janecek J., Boublik T., The Second Virial Coefficient of Polar Rod-Like Molecules, Fluid Phase Equilib., 212, p. 349 (2003).
[23] Pires A.P., Mohamed R.S., Mansoori G.A., An Equation of State for Property Prediction of Alcohol-Hydrocarbon and Water-Hydrocarbon Systems, J. Pet. Sci. & Eng., 32, p. 103 (2001).
[24] Perry R.H., Green D.W., Maloney J.O., “Perry's Chemical Engineer's Hand book”, 7th Ed. Mc Graw Hill,New York, (1997).
[25] “Physical Properties”, DIPPR^{®}801 Database (2005 release),BrighamYoungUniversity, (2005).
[26] Heijmen T.G.A., Moszynski R., van der Avoird A., Second Dielectric Virial Coefficient of Helium Gas: Quantum-Statistical Calculations from an Ab Initio Interaction-Induced Polarizability,
Chem. Phys. Lett., 247 (4-6), p. 440 (1995).
[27] De Haan M., Kinetic Derivation of the Second Virial Coefficient for a Quantum Gas, Physica A, 7
0 (3), p. 571 (1991).
[28] Vogl F., Hall K.R., Capressiblity Data and Virial Coefficients for Helium, Neon and One Mixture, Physica, 59 (3), p. 529 (1972).
[29] Erratum R., Gerber S., Huber H., Ab Initio Calculation of the Second Virial Coefficient of Neon and the Potnetial Energy Curve of Ne_{2}, Mol. Phys., 156, p. 395 (1991).
[30] Meng L., Duan Y.Y., An Extended Correlation for Second Virial Coefficients of Associated and Quantum Fluids, Fluid Phase Equilib., 258, p. 29 (2007).
[31] Holleran E., Improved Virial Coefficients, Fluid Phase Equilib., 251, p. 29 (2007).
[32] Dymond J.H., Marsh K.N., Wilhoit R.C., Wong K.C., “Virial Coefficients of Pure Gases and Mixtures”, Vol. A, in: Virial Coefficients of Pure Gases,Springer–Verlag,Berlin, (2002).
[33] Allen M.P., Tildesley D.J., “Computer Simulation of Liquids”, Clarendon Press,Oxford, pp. 22, (1986).
[34] Poling B.E., Prausnitz J.M., O Connel J.P., “The Properties of Gases & Liquids”, 5th Ed, McGraw Hill,New York, (2001).
[35] Matias A., Nunes A., Casimiro T., DuarteC.M.M., Solubility of Coenzyme Q10 in Supercritical Carbon Dioxide, J. Supercrit Fluids, 28, 201 (2004).
[36] Torres R.E., Silva G.A.L., Estrada M.R., Hall K.R., Boyle Temperatures for Pure Substances, Fluid Phase Equilib, 258, p. 148 (2007).
[37] Powles J.G., The Boyle Line, J. Phys, 16, p. 503 (1983).
[38] Pitzer K.S., “Thermodynamics”, 3rd Ed, McGraw Hill,New York, (1995).
[39] Modell M., Reid R.D., “Thermodynamics and its Applications”, 2nd Ed, Prentice-Hall, Inc. (1983).
[40] Peng D.Y., Rabinson D.B., J. Ind. Eng. Chem. Fundamen, 15, p. 59 (1976).
[41] Soave G., Equilibrium Constants from a Modified Redich-Kwong Equation of State, J. Chem. Eng. Sci., 27, p. 1197 (1972).
[42] McGlashan M.L., Potter D.J., An Apparatus for the Measurement of the Second Virial Coefficients of Vapours; The Second Viral Coefficients of Some n-Alkanes and of Some Mixtures of n-Alkanes, Proc. R. Soc. A, 267, p. 478 (1962).
[43] Nicola G.D., Giuliani G., Ricci R., Stryjek R., PVT Properties of Dinitrogen Monoxide, J. Chem. Eng. Data, 49, 213 (2004).
[44] D'Amore A., Nicola G.D., Polonara F., Stryjek R., Virial Coefficients from Burnett Measurements for the Carbon Dioxide + Fluoromethane System, J. Chem. Eng Data, 48, p. 440 (2003).
[45] Evans R.B., Watson G.M., Compressibility Factors of n-Butane Mixtures in the Gas phase, J. Chem. Eng. Data Series., 1, p. 67(1956).
[46] Warowny W., Second and Third Virial Coefficient for (Acetonitrile + n-Butane), J. Chem. Thermodynamics, 30, p. 167 (1998).
[47] Holleran E., A Virial Interrelation for Temperatures from About 1.0 to 2.7 Times the Critical Temperature, Fluid Phase Equilib., 239, p. 30 (2006).
[48] Span R., Lemmon E., Jacobsen R., Wagner W., Yokozeki A., A Referemce Equation of State for the Thermodynamic Properties of Nitrogen for Temperatures from 63.151 to 1000 K and Pressures to 2200 MPa, J. Phys. Chem. Ref. Data, 28, p. 1361 (2000).