[1] Hawkins, J.E., Armstrong, G.T., "Physical and thermodynamic properties of terpenes", J. Am. Chem. Soc., 76,3756-3758 (1954). [2] Farelo, F., Santos, F., Serrano, L., "Isobaric vapor-liquid equilibria in binary mixtures of α-pinene, limonene and 1,8-cineole", Can. J. Chem. Eng., 69,794-799 (1991). [3] Tucker, W. C., Hawkins, J. E., "Vapor-liquid equilibria of alpha-pinene-beta-pinene system", Ind. Eng. Chem., 46,2387-2390 (1954). [4] Reich, R., Sanhueza, V., "Vapor-liquid equilibria for α-pinene and β-pinene and for these pinenes with heptane,cyclohexane, 1-octene and cyclohexene", Fluid Phase Equilib., 77, 313-325 (1992). [5] Reich, R., Sanhueza, V., "Vapor-liquid equilibria for α-pinene and β-pinene with 1- butanol and 1-pentanol", Fluid Phase Equilib., 78, 239-248 (1992). [6] Wang, C., Li, H., Ma, L., Han, S., "(Vapor + liquid) equilibria for the binary mixtures (cis-pinane +α-pinene) and (cispinane + 1-butanol)", J. Chem. Thermodyn., 35, 131-136 (2003). [7] Wang, C., Li, H., Tai, J., Han, S., "Vapor-liquid equilibria for the binary systems α -pinene + alkanols", Fluid Phase Equilib., 209, 147-154 (2003). [8] Robert, C.W., Melvin, J.A., Willian, H.B., The CRC Handbook of Chemisty and Physics, 66th edition, CRC Press,Inc. Boca Raton, Florida (1986). [9] Li, H., Han, S., Teng, Y., "Bubble points measurement for system chloroform-ethanol- benzene by inclined ebulliometer", Fluid Phase Equilib., 113, 185-195 (1995). [10] Li, H., Han, S., "Isothermal and isobaric (vapor+liquid)equilibria of (ethanol + benzene + hexane)", J. Chem.Thermodyn., 29, 921-927 (1997). [11] Wang, C., Li, H., Zhu, L., Han, S., "Isothermal and isobaric vapor + liquid equilibria of N,N-dimethylformamide + npropanol + n-butanol", Fluid Phase Equilib., 189, 119-127 (2001). [12] Hayden, J. G., O’Connell, J. P., "A generalized method for predicting second virial coefficients", Ind. Eng. Chem.,Process. Des. Dev., 14, 209-216 (1975). [13] Spencer, C.F., Danner, R.P., "Improved equation for prediction of saturated liquid density", J. Chem. Eng. Data.,17, 236-241 (1972). [14] Gmehling, J. G., Onken, U., "Vapour-liquid equilibrium data collection", DECHEMA Chemistry Data Series:DECHEMA Frankfurt, Vol. 1, Germany (1977). [15] Anderson, T. F., Prausnitz, J. M., "Application of the UNIQUAC equation to calculation of multi-component phase equilibria", Ind. Eng. Chem., Process. Des. Dev., 17,552-561 (1978). [16] Powell, M.J.D., "An efficient method for finding the minimum of a function of several variables without calculating derivatives", Computer J., 7, 155-162 (1964). |