[1] Kister, H.: Distillation Design (McGraw-Hill Education, New York) 1992Google Scholar
[2] Szabó, L.; Németh, S.; Szeifert, F.: Separation of multicomponent mixtures, Hung. J. Ind. Chem., 2011 39(2), 295–300Google Scholar
[3] Toth, A.J.; Gergely, F.; Mizsey, P.: Physicochemical treatment of pharmaceutical wastewater: distillation and membrane processes, Per. Pol. Chem. Eng., 2011 55(2), 59–67 DOI 10.3311/pp.ch.2011-2.03CrossrefGoogle Scholar
[4] Mizsey, P.; Toth, A.J.: Application of the principles of industrial ecology for the treatment of process waste-waters with physicochemical tools, Indust. Ecol., 2012 1(1), 101–125Google Scholar
[5] Mizsey, P.; Szanyi, A.; Raab, A.; Manczinger, J.; Fonyo, Z.: Intensification of a solvent recovery technology through the use of hybrid equipment, Comp. Aided Chem. Eng., 2002 10(1), 121–126 10.1016/S1570-7946(02)80048-7Google Scholar
[6] Szanyi, A.; Mizsey, P.; Fonyo, Z.: Novel hybrid separation processes for solvent recovery based on positioning the extractive heterogeneous-azeotropic distillation, Chem. Eng. Proc., 2004 43(3), 327–338 DOI 10.1016/S0255-2701(03)00132-6CrossrefGoogle Scholar
[7] Szanyi, A.; Mizsey, P.; Fonyo, Z.: Optimisation of nonideal separation structures based on extractive heterogeneous azeotropic distillation, Ind. Eng. Chem. Res., 2004 43(26), 8269–8274 DOI 10.1021/ie049575lCrossrefGoogle Scholar
[8] Szanyi, A.; Mizsey, P.; Fonyo, Z.: Separation of highly non-ideal quaternary mixtures with extractive heterogeneous-azeotropic distillation, Chem. Biochem. Eng. Q., 2005 19(2), 111–121Google Scholar
[9] Szanyi, A.: Separation of non-ideal quaternary mixtures with novel hybrid processes based on extractive heterogeneous-azeotropic distillation (PhD Dissertation, BME, Budapest) 2005Google Scholar
[10] Franke, M.; Gorak, A.; Strube, J.: Design and optimisation of hybrid separation processes, Chem. Eng. Tech., 2004 76(3), 199–210 DOI 10.1002/cite.200406150CrossrefGoogle Scholar
[11] Skiborowski, M.; Harwardt, A.; Marquardt, W.: Conceptual design of distillation-based hybrid separation processes, Annu. Rev. Chem. Biomol. Eng., 2013 4(1), 45–68 DOI 10.1146/annurev-chembioeng-061010-114129CrossrefGoogle Scholar
[12] Skiborowski, M.; Harwardt, A.; Marquardt, W.: Conceptual Design of Azeotropic distillation processes (in Eds.: Gorak, A.; Sorensenm, E.; Distillation: Fundamentals and principles, Academic Press, Aachen, Germany) 2014, Chapter 8, p. 321Google Scholar
[13] Wijesinghe, A.M.J.C.: Development of industrial complexes of special rectification techniques for solvent recovery (PhD dissertation, Lomonosov Institute of Fine Chemical Engineering, Moscow) 1985Google Scholar
[14] Raab, A.: Separation of highly non-ideal mixtures for solvent recovery (MSc Thesis, BME, Budapest) 2001Google Scholar
[15] Abrams, D.S.; Prausnitz, J.M.: Statistical thermodynamics of liquid mixtures: A new expression for the excess gibbs energy of partly or completely miscible systems, AIChE J., 1975 21(1), 116–128 DOI 10.1002/aic.690210115CrossrefGoogle Scholar
[16] Egner, K.; Gaube, J.; Pfennig, A.: GEQUAC, an excess Gibbs energy model describing associating and non-associating liquid mixtures by a new model concept for functional groups, Fluid Phase Equilib., 1999 158–160, 381–389 DOI 10.1016/S0378-3812(99)00137-5CrossrefGoogle Scholar
[17] Klamt, A.; Krooshof, G.J.P.; Taylor, R.: COSMOSPACE: Alternative to conventional activity-coefficient models, AIChE J., 2002 48(10), 2332–2349 DOI 10.1002/aic.690481023CrossrefGoogle Scholar
[18] Wiśniewska-Goclowska, B.; Malanowski, S.X.K.: A new modification of the UNIQUAC equation including temperature dependent parameters, Fluid Phase Equilib., 2001 180(1–2), 103–113 DOI 10.1016/S0378-3812(00)00514-8CrossrefGoogle Scholar
[19] Fredenslund, A.; Jones, R.L.; Prausnitz, J.M.: Group-contribution estimation of activity coefficients in non-ideal liquid mixtures, AIChE J., 1975 21(6), 1086–1099 DOI 10.1002/aic.690210607CrossrefGoogle Scholar
[20] Akita, K.; Yoshida, Y.: Phase-equilibria in methanol-ethyl acetate-water system, J. Chem. Eng. Data, 1963 8(1), 484–490 DOI 10.1021/je60019a003CrossrefGoogle Scholar
[21] Gmehling, J.; Menke, J.; Krafczyk, J.; Fischer, K.: Azeotropic data (Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim, Germany) 1994Google Scholar
[22] Gmehling, J.; Onken, U.; Rarey-Nies, J. R.: Vapor-liquid equilibrium data collection (Dechema, Virginia, USA) 1978Google Scholar
[23] Marsden, C.: Solvents And Allied Substances Manual With Solubility Chart (Cleaver-Hume and Elsevier, London) 1954Google Scholar
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