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T/K ρ /kg. m-3 n D η /mPa. s Exp Lit Exp Lit Exp Lit Chloroform             288.15 1497.7 1498.45a     0.62630 0.5960a 293.15 1488.0 1489.11a 1.44572 1.44590a 0.59989 0.573d     1487.58b         298.15 1478.4 1479.70a     0.57632 0.5357a     1477.3c         303.15 1469.2 1470.60a     0.55239 0.5140a     1469.4d       0.516d DIPE             288.15 728.6         0.32748 293.15 723.4 723.9a 1.36808 1.3680a 0.31545 0.3347a 298.15 718.2 718.5a     0.30424 0.3790a     718.32e 1.36523e       303.15 712.9 713.5a     0.28817 0.3010a

a Riddick, J. A.; Bunger, W. B.; Sakano, T. K. Organic Solvents. Physical Properties and Methods of Purification. 4th ed.; John Wiley: New York, 1986.

b Kozłowska, M. K.; Domańska, U.; Lempert, M.; Rogalski, M. Determination of Thermodynamic Properties of Isotactic Poly (1-Butene) at Infinite Dilution Using Density and Inverse Gas Chromatography. J. Chromatog. A 1068, 297-305 (2005)

c Atik, Z. Study of Vapor−Liquid Equilibrium for Binary Mixtures (Chloroform + 2,2,2-Trifluoroethanol) and (α,α,α-Trifluorotoluene + 2,2,2-Trifluoroethanol) at Pressure 102 kPa. J. Chem. Eng. Data52, 1128-1130 (2007)

d Clará, R. A.; Gómez Marigliano, A. C.; Sólimo, H. N. Density, Viscosity, Vapor-Liquid Equilibrium, Excess Molar Volume, Viscosity Deviation, and Their Correlations for the Chloroform + 2-Butanone Binary System. J. Chem. Eng. Data51, 1473–1478 (2006)

e Gómez Marigliano, A. C.; Arce, A., Rodil, E., Soto, A. N. Isobaric Vapor-Liquid Equilibriaat 101.32 kPaand Densities, Speeds of Sound, and Refractive Indices at 298.15 K for MTBE or DIPE or TAME + 1-Propanol Binary Systems. J. Chem. Eng. Data55, 92-97 (2010)

Table 1: Density ρ, viscosity η and refractive index nD of pure compounds at several temperatures