1 Reters, C. J., De Roo, J. L., "Measurements and calculations of phase equilibria of binary mixtures of ethane + eicosane. Part I: vapour + liquid equilibria", Fluid Phase Equilib, 34 (2-3), 287-308 (1987).2 Connemann, M., Gaube, J., Karrer, L., Pfennig, A., Reuter, U., "Measurement and representation of ternary vapor-liquid-equilibria", Fluid Phase Equilib, 60 (1-2), 99-118 (1990).3 De Loos, T.W., Van der Kooi, H.J., Ott, P.L., "Vapor-liquid critical curve of the system ethane + 2-methylpropane", J. Chem. Eng. Data, 31 (2), 166-168 (1986).4 Wang, J.H., Zhao, H.F., Luo, L., Luo, L., Song, H.H., Ci, D.J., "Design of high purity cyclohexene oxide by distillation", Chemical Industry and Engineering Progress, 22 (11), 1210-1212 (2003). (in Chinese)5 Wang, Z.X., Zhang, Y.D., Tang, P.G., "Cyclohexene oxide synthesized by epoxidation of cyclohexene and hydrogen peroxide with phase thansfer catalyst", Fine Chemicals, 23(1), 1023-1026 (2006). (in Chinese)6 Ma, P.S., Chemical Engineering Thermodynamics, Chemical Industry Press, Beijing (2005). (in Chinese)7 Van Schilt, M.A., Wering, R.M., Kemmere, M.F., "Measurement and modeling of the high-pressure phase behavior of the binary system carbon dioxide + 1,2-epoxycyclohexane", J. Chem. Eng. Data, 50 (6), 1879-1882 (2005).8 Zhou, C.R., Li, H.P., Du, B., Li, J.J., Jiang, D.G., "Thermodynamic properties of binary system of dimethyl sulfoxide and water", Journal of Chemical Engineering of Chinese Universities, 13 (2), 153-155 (1999). (in Chinese)9 Hu, S.Z., "The modification of ROSE vapor-liquid equilibrium still", Natural Science Journal of Xiangtan University, 12 (1), 76-78 (1990). (in Chinese)10 Chen, Z.X., Hu, W.M., "Isobaric vapor-liquid equilibriums of octane-ethyl acetate and octane-isopropyl acetate systems", Chin. J. Chem. Eng., 3 (3), 180-186 (1995).11 Wang, X.M., Jiang, D.G., Geng, Z.X., "Measurement and correlation of vapor liquid equilibrium data for cyclohexene-1,2-epoxycyclohexane binary system under normal pressure", Journal of Chemical Engineering of Chinese Universities, 23 (3), 366-368 (2009). (in Chinese)12 Okada, I., Ogino, H., Pocket-size Chemical Engineering Handbook, Jiangsu Science and Technology Press, Nanjing (1985).13 Maciel, M.R.W., Franceconi, A.Z., "Vapor-liquid phase equilibrium measurements for the N-hexane-1-butanol system at 323.15, 338.15, and 348.15 K", Fluid Phase Equilib., 50 (1-2), 201-208 (1989).14 Makoto, F., Hiroyuki, M., Kiyofumi, K., Kenji, O., "Equilimetric determination of vapor-liquid equilibria for methanol + ethanol + dimethyl carbonate", J. Chem. Eng. Data, 51 (4), 1458-1463 (2006).15 Wang, X.M., Jiang, D.G., Geng, Z.X., "Isobaric vapor-liquid equilibrium of binary system 2-cyclohexen-1-one and 1,2-epoxycyclohexane", Chin. J. Chem. Eng., 17 (1), 136-139 (2009).16 Sundaram, S., Viswanath, D.S., "Thermodynamic properties of the system toluene-1,2-dichloroethane", J. Chem. Eng. Data, 21 (4), 448-451 (1976).17 Sandler, S.I., Chemical and Engineering Thermodynamics, 3rd edition, Chemical Industry Press, Beijing (2002). |