William G. Killian1, Aseel M. Bala2 Lars Peereboom1, Jackson A. Storer1, Renming Liu1, Andrew T. Norfleet1, Cesar Plascencia3, James E. Jackson3, Carl T. Lira1
1Chemical Engineering, Michigan State University, East Lansing, MI; 2Chemial Engineering, Lafayette College, Easton PA; 3Chemistry, Michigan State University, East Lansing, MI
References:
[1] M.S. Wertheim, Fluids with highly directional attractive forces. 4. Equilibrium polymerization, Journal of Statistical Physics. 42 (1986) 477–492. doi:10.1007/bf01127722.
[2] M.S. Wertheim, Fluids with highly directional attractive forces. 3. Multiple attraction sites, Journal of Statistical Physics. 42 (1986) 459–476. doi:10.1007/bf01127721.
[3] H. Renon, J.M. Prausnitz, Local compositions in thermodynamic excess functions for liquid mixtures, Aiche J. 14 (1968) 135-. doi:10.1002/aic.690140124.
[4] J.G. Hayden, J.P. O’Connell, A generalized method for predicting second virial coefficients, Industrial & Engineering Chemistry Process Design and Development. 14 (1975) 209–216. doi:10.1021/i260055a003.
[5] J. Gross, G. Sadowski, Application of the Perturbed-Chain SAFT Equation of State to Associating Systems, Ind. Eng. Chem. Res. 41 (2002) 5510–5515. doi:10.1021/ie010954d.
[6] H. Renon, J.M. Prausnitz, On the thermodynamics of alcohol-hydrocarbon solutions. Errata., Chemical Engineering Science. 22 (1967) 1891. doi:10.1016/0009-2509(67)80223-9.
[7] S.W. Campbell, Chemical theory for mixtures containing any number of alcohols, Fluid Phase Equilibria. 102 (1994) 61–84. doi:10.1016/0378-3812(94)87091-8.
[8] G.M. Kontogeorgis, E.C. Voutsas, I.V. Yakoumis, D.P. Tassios, An Equation of State for Associating Fluids, Industrial & Engineering Chemistry Research. 35 (1996) 4310–4318. doi:10.1021/ie9600203.
[9] L.S. Budantseva, T.M. Lesteva, M.S. Nemtsov, Liquid-vapor equilibriums in methanol-C6 hydrocarbons of different classes, Zh. Fiz. Khim. 49 (1975) 260–1.
[10] H. Katayama, Liquid–liquid equilibria of two ternary systems: methanol–cyclohexane including 1,3-dioxolane or 1,4-dioxane in the range of 277.79–308.64 K, Fluid Phase Equilibria. 164 (1999) 83–95. doi:10.1016/S0378-3812(99)00241-1.
[11] A.N. Marinichev, M.P. Susarev, Zh. Prikl. Khim. (Leningrad). 38 (1965) 1619.
[12] K. Strubl, V. Svoboda, R. Holub, J. Pick, Liquid Vapor Equilibrium XIV. Isothermal Equilibriuim and Calculation of Excess Functions in the Systems Methanol-Cyclohexane and Cyclohexane-Propanol, Collect. Czech. Chem. Commun. 35 (1970) 3004.
[13] J. Gmehling, B. Krentscher, Excess enthalpies of 12 binary liquid mixtures containing cyclohexane at elevated temperatures and pressures (up to 416 K and 1.9 MPa), ELDATA Int. Electron. J. Phys.-Chem. Data. 1 (1995) 181–190.
[14] M.J. Lazzaroni, D. Bush, C.A. Eckert, T.C. Frank, S. Gupta, J.D. Olson, Revision of MOSCED parameters and extension to solid solubility calculations, Industrial & Engineering Chemistry Research. 44 (2005) 4075–4083. doi:10.1021/ie049122g.
[15] N.A. Smirnova, L.M. Kurtynina, Thermodynamic functions of mixing for a number of binary alcohol-hydrocarbon solutions., Zh. Fiz. Khim. 43 (1969) 1883.