1 Li, S.,Huang, D., “Simulation and analysis on multiple steady states of an industrial acetic acid dehydration system”, Chin. J. Chem. Eng., 19 (6), 983-989 (2011).2 Li, C., “Dynamic simulation and analysis of industrial purified terephthalic acid solvent dehydration process”, Chin. J. Chem. Eng., 19 (1), 89-96 (2011).3 Hayden, J.G., O’Connell, J.P., “A generalized method for predicting second virial coefficients”, Ind. Eng. Chem. Proc. Des. Dev., 14 (3), 209-216 (1975).4 Renon, H., Prausnitz, J.M., “Local compositions in thermodynamic excess functions for liquid mixtures”, AIChE J., 14 (1), 135-144 (1968).5 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., 21 (1), 116-128 (1975).6 Vercher, E., Vázquez, M.I., Martínez-Andreu, A., “Isobaric vapor-liquid equilibria for water+acetic acid+lithium acetate”, J. Chem. Eng. Data, 46 (6), 1584-1588 (2001).7 Fu, H., Chen, G.H., Han, S.J., “VLE research of system containing associating components (II)—VLE of binary systems: Acetic acid-Water, Acetic acid-Butanone, Acetic acid-Pentanone and Acetic acid-Propyl acetate”, Chem. Eng. (China), 6, 56-61 (1986). (in Chinese)8 Marek, J., “Vapor-liquid equilibria in mixtures containing an association substance II. Binary mixtures of acetic acid at atmospheric pressure”, Collect. Czech. Chem. Commun., 20, (1955).9 Sawistowski, H., Pilavakis, P.A., “Vapor-liquid equilibrium with association in both phases. Multicomponent systems containing acetic acid”, J. Chem. Eng. Data, 27 (1), 64-71 (1982).10 Perelygin, V.M., Volkov, A.G., “Vapor-liquid phase equilibrium in the systems ethanol-methyl acetate and water-methyl acetate”, Izv. Vyssh. Uchebn. Zaved. Pishch. Tekhnol., 3, 124-126 (1970).11 Xiao, X., Wang, L., Ding, G., Li, X., “Liquid-liquid equilibria for the ternary system water+acetic acid+propyl acetate”, J. Chem. Eng. Data, 51 (2), 582-583 (2005).12 Chiu, H.S., Lee, L.S., “Phase equilibria of water+acetic acid+p-xylene mixture at 101.32 kPa”, Ms.D. Thesis, National Central University, Taiwan (2007).13 Korovina, T.V., Pisarenko, Y.A., Balashov, M.I., “Mathematical modelling of the phase relations of binary components of the system methyl formate-methyl acetate-propyl formate-propyl acetate at 760 mm Hg”, Deposited Doc. VINITI (Russia), 3634-3677, 1-10 (1977).14 Prausnitz, J.M., Anderson, F.F., Grens, E.A., Eckert, C.A., Hsieh, R., O’connell, J.P., Computer calculations for multicomponent vapor-liquid and liquid-liquid equilibria, Prentice-Hall, Englewood Cliffs, N.J. (1980).15 Poling, B.E., Prausnitz, J.M., John Paul, O.C., The properties of gases and liquids, 5th edition, McGraw-Hill, New York (2001).16 Aspen Technology, I., Aspen Plus User’s Manual 11.1, In Aspen Technology, Inc., Cambridge, MA (2001).17 Herington, E.F.G., “Tests for the consistency of experimental isobaric vapour-liquid equilibrium data”, J. Inst. Petrol., 37, 457-470 (1951). |