[1]. Kontogeorgis G. M., Voutsas E., Yakoumis I., and Tassios D. P., “An equation of state for associating fluid”, Ind. Eng. Chem. Res., Vol. 35, pp. 4310-4318, 1996.##
[2]. Kontogeorgis G. M., Michelsen M. L.; Folas G. K., Derawi S., Solms N. V. and Stenby E. H., “Ten years with the CPA equation of state. part 1. pure compounds and self-associating systems”, Ind. Eng. Chem. Res., Vol. 45, No. 14, pp. 4855-4868, 2006.##
[3]. Folas G. K., Kontogeorgis G. M., Michelsen M. L. and Stenby E. H., “Application of the cubic-plus-association(CPA) equation of state to complex mixtures with aromatic hydrocarbons”, Ind. Eng. Chem. Res., Vol. 45, No. 4, pp. 1527-1538, 2006.##
[4]. Yakoumis I. V., Kontogeorgis G. M., Voutsas E. C., Hendriks E. M., and Tassios D. P., “Prediction of phase equilibria in binary aqueous systems containing alkanes”, Cycloalkanes, and Alkenes with the Cubic-plus-Association Equation of State., Ind. Eng. Chem. Res., Vol. 37, pp. 4175-4182, 1998.##
[5]. Kontogeorgis G. M., Yakoumis I. V., Meijer H., Hendriks E. M., and Moorwood T., “Multicomponent phase equilibrium calculations for water-methanol-alkane mixtures”, Fluid Phase Equilib., Vol. 201, pp. 158-160., 1999.##
[6]. Queimada A. J., Miqueuc C., Marrucho I. M., Kontogeorgis G. M., and Coutinho J. A. P., “Modeling vapor–liquid interfaces with the gradient theory in combination with the CPA equation of state”, Fluid Phase Equilib., Vol. 228–229, pp. 479–485, 2005.##
[7]. Kaarsholm M., Derawi S. O., Michelsen M. L., and Kontogeorgis G. M., “Extension of the Cubic-plus-Association (CPA) Equation of State to Amines”, Ind. Eng. Chem. Res., Vol. 44, pp. 4406-4413., 2005.##
[8]. Oliveira, M. B., Queimada, A. J., Coutinho, J. A. P., “Mutual solubilities of hydrocarbons and waterwith the CPA EoS, Fluid Phase Equilib., Vol. 258, pp. 58–66., 2007.##
[9]. Park S. J., Gmehllng J., Isobaric Vapor-Liquid Equilibrium Data for the Binary Systems 1, 3, 5-Trimet hylbenzene/N-Formylmorpholine and m-Xylene/N-Formylmorpholine., J. Chem. Eng. Data, Vol. 34, pp. 399-401, 1989. ##
[10]. Huang X., Xia S., Ma P., Song S., Ma B., “Vapor–liquid equilibrium of N-Formylmorpholine with toluene and xylene at 101.33 kPa”, J. Chem. Eng. Data, Vol. 53, pp. 252–255, 2008.##
[11]. Huang S. H., Radosz M., “Equation of state for small, large, polydisperse, and associating molecules”, Ind. Eng. Chem. Res., Vol. 29, pp. 2284-2294, 1990.##
[12]. Nelder J. A. and Mead. R., “A simplex method for function minimization”. Computer Journal, Vol. 7, pp. 308-313, 1965.##
[13]. Physical and Chemical Properties Division National Institute of Standards and Technology, Boulder, Colorado 80305, April, U.S. Department of Commerce, 2007##
[14]. VonNiederhausern D., M., Wilson G. M., and Giles N. F., “Critical point and vapor Pressure measurements for 17 compounds by a low residence time flow method”, J. Chem. Eng. Data, Vol. 51, pp. 1990-1995, 2006.##
[15]. Oliveira M. B., Teles A. R. R., Queimada A. J., Coutinho J. A. P., “Phase equilibria of glycerol containing systems and their description with the cubic-plus-association (CPA) equation of state”, Fluid Phase Equilib., Vol. 280, pp. 22-29, 2009.##
[16]. Yin. W., Ding. S., Xia. S., Ma. P., Huang. X., and Zhu. Z., “Cosolvent selection for benzene-cyclohexane separation in extractive distillation”, J. Chem. Eng. Data, Vol. 55, pp. 3274–3277, 2010.##
[17]. Kontogeorgis G. M., Folas G. K., Su N. M., Solms N. V., Michelsen M. L., Stenby E. H., “Modeling of associating mixtures for applications in the oil & gas and chemical industry”, Fluid Phase Equilib., Vol. 261, pp. 205-211, 2007.##
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