1 Grunberg, L., Nissan, A.H., “Mixture law for viscosity”, Nature, 164, 799—802(1949). 2 Glasstone, S., Laidler, K.J., Eyring, H., The Theory of Rate Processes, McGraw-Hill, New York (1941). 3 Poling, B.E., Prausnitz, J.M., O’Connell, J.P., The Proper-ties of Gases and Liquids, 5th ed., McGraw-Hill, Boston (2001). 4 Teja, A. S., Rice, P., “Generalized corresponding states method for the viscosities of liquid mixtures”, Ind. Eng. Chem. Fundam., 20, 77—81(1981). 5 Liu, H., Wang, W., Chang, C.H., “Model with tempera-ture-independent parameters for the viscosities of liquid mixtures”, Ind. Eng. Chem. Res., 30, 1617—1624(1991). 6 Papaloannou, D., Evangelou, T., Panayiotou, C., “Dy-namic viscosity of multicomponent liquid mixtures”, J. Chem. Eng. Data, 36, 43—46(1991). 7 McAllister, R.A., “The viscosities of liquid mixtures”, AIChE J., 6, 427—431(1960). 8 Wei, I. C., Rowley, R. L., “A local composition model for multicomponent liquid mixture shear viscosity”, Chem. Eng. Sci., 40, 401—408(1985). 9 Wu, D. T., “Prediction of viscosities of liquid mixtures by a group contribution method”, Fluid Phase Equilibria, 30, 149—156(1986). 10 Chevalier, J. L. E., Petrino, P. J., Gaston-Bonhomme, Y., “Estimation method for the kinematic viscosity of a liq-uid-phase mixture”, Chem. Eng. Sci., 43, 1303—1309(1988). 11 Cao, W., Fredenslund, A., Rasmussen, P., “Statistical ther-modynamic model for viscosity of pure liquids and liquid mixtures”, Ind. Eng. Chem. Res., 31, 2603—2619(1992). 12 Cao, W., Knudaen, K., Fredenslund, A., Rasmussen, P., “Simultaneous correlation of viscosity and vapor-liquid equilibrium data”, Ind. Eng. Chem. Res., 32, 2077—2087(1993). 13 Lee, M.J., Chiu, J.Y., Hwang, S.M., Lin, H.M, “Viscosity calculations with the Eyring-Patel-Teja model for liquid mixtures”, Ind. Eng. Chem. Res., 38, 2867—2876(1999). 14 Adachi, Y., Sugie, H., “A new mixing rule—modified conventional mixing rule”, Fluid Phase Equilibria, 28, 103—108(1986). 15 Michelsen, M.L., Kistenmacher, H., “On composi-tion-dependent interaction coefficients”, Fluid Phase Equilibria, 58, 229—230(1990). 16 Stryjek, R., Vera, J.H., “PRSV an improved Peng-Robinson equation of state with new mixing rules for strongly non-ideal mixtures”, Can. J. Chem. Eng., 64, 334—340(1986). 17 Wei, I.C., Rowley, R.L., “Binary liquid viscosities and densities”, J. Chem. Eng. Data, 29, 332—335(1984). 18 Dizechl, M., Marschall, E., “Viscosity of some binary and ternary liquid mixtures”, J. Chem. Eng. Data, 27, 358—363(1982). 19 Chevalier, J. L. E., Pertrino, P. J., Gaston-Bonhomme, Y. H., “Viscosity and density of some aliphatic, cyclic, and aromatic hydrocarbons binary liquid mixtures”, J. Chem. Eng. Data, 35, 206—212(1990). 20 Kouris, S., Panajiotou, C., “Dynamic viscosity of mix-tures of benzene, ethanol, and n-heptane at 298.15K”, J. Chem. Eng. Data, 34, 200—203(1989). 21 Asfour, A.F.A., Siddique, M.H.J., Vavanellos, T.D., “Kinematic viscosity-composition data for eight binary systems containing toluene or ethylbenzene and C8-C16 n-alkanes at 293.15 and 298.15K”, Chem. Eng. Data, 35, 199—201(1990). 22 Fermeglia, M., Lapasin, R., “Excess volumes and vis-cosities of binary mixtures of organics”, J. Chem. Eng. Data, 33, 415—417(1988). 23 Singh, R.P., Sinha, C.P., “Viscosity and thermodynamics of viscous flow of some associated mixtures”, Z. Phys. Chemie, Leipzig, 265, 593—602(1984). 24 Asfour, A.F.A., Dullien, F.A.L., “Viscosities and densi-ties of four binary liquid systems at 25.00℃”, J. Chem. Eng. Data, 26, 312—316(1981). 25 Singh, R.P., Sinha, C.P., Singh, B.N., “Viscosities densi-ties and activation energies of viscous flow of some ter-nary systems and their partially miscible binary subsys-tem n-hexane+benzyl alcohol at 30, 40, 50, and 60℃”, J. Chem. Eng. Data, 31, 107—111(1986). 26 Orge, B., Iglesias, M., Rodrigguez, A., Canosa, J.M., Tojo, J., “Mixing properties of (methanol, ethanol, or 1-propanol) with (n-pentane, n-hexane, n-heptane and n-octane)”, Fluid Phase Equilibria, 133, 213—227(1997). 27 Aminabhavi, V.A., Aminabhavi, T.M., Balundgi, R.H., “Evaluation of excess parameters from densities and viscosities of binary mixtures of ethanol with anisole, N,N-dimethylformamide, carbon tetrachloride, and ace-tophenone from 298.15 to 313,14K”, J. Chem. Eng. Data, 29, 2106—2111(1990). 28 Singh, R.P., Sinha, C.P., “Viscosities and activation en-ergies of viscous flow of the binary mixtures of n-hexane with toluene, chlorobenzene, and 1-hexanol,” J. Chem. Eng. Data, 29, 132—135(1984). 29 Hammond, L.W., Howard, K.S., McAllister, R.A., “Vis-cosities and densities of methanol-toluene solutions up to their normal boiling points”, J. Phys. Chem., 62, 637—639(1958). 30 Katti, P.K., Chaudhri, M.M., Prakash, O., “Viscosities of binary mixtures of carbon tetrachloride with methanol and isopropyl alcohol”, J. Chem. Eng. Data, 11, 593—594(1966). 31 Christensen, C., Gmehling, J., Rasmussen, P., Weidlich, U., Heat of Mixing Data Collection, Binary Systems, DECHEMA Chemistry Data Series, Vol. III, Part 1, Part2, Frankfurt (1984). 32 Ji, W.R., Lempe, D.A., “A systematic study of cubic three-parameter equations for deriving a structurally op-timized PVT relation”, Fluid Phase Equilibria, 147, 85—103(1998). 33 Ji, W.R., Stiebing, E., Lempe, D.A., Strukturooptimierte Dreiparameter-Zustandsgleichung (C3EOS) zur Besch- reibung von Phasengleichgewichts und anderen thermo- physikalischen Eigenschaften. Bericht zum DFG- Vorhaben LE 886/4-1, Merseburg (2004). 34 Wei, I.C., Rowley, R.L., “Ternary liquid mixture viscosi-ties and densities”, J. Chem. Eng. Data, 29, 336—340(1984). 35 Singh, R.P., Sinha, C.P., “Viscosities and activation ener-gies of viscous flow of the ternary mixtures of toluene, chlorobenzene, and 1-hexanol, and benyl alcohol”, J. Chem. Eng. Data, 30, 470—474(1985).
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