Abstract
Experimental tie-line data were determined for one ternary system, water + diisopropyl ether + n-heptane and two quaternary systems, water + diisopropyl ether + 2-propanol + n-heptane or toluene at 298.15 K and ambient pressure. The experimental liquid–liquid equilibrium data were successfully correlated using a modified UNIQUAC model with ternary and quaternary mixture parameters, in addition to the binary ones. The calculated results were also compared with those obtained from an extended UNIQUAC model of Nagata [Fluid Phase Equilib. 54, 191 (1990)].
This is a preview of subscription content, log in via an institution to check access.
Similar content being viewed by others
References
K. Tamura, Y. Chen, K. Tada, T. Yamada, and I. Nagata, J. Solution Chem. 29, 463 (2000).
I. Nagata, Fluid Phase Equilib. 54, 191 (1990).
V. V. Udovenko and T. F. Mazanko, Zh. Fiz. Khim. 41, 1615 (1967).
C. R. Chamorro, J. J. Segovia, M. C. MartÍn, and M. A. Villamañán, J. Chem. Thernodyn. 34, 13 (2002).
S. V. Vijayaraghavan, P. K. Deshpande, and N. R. Kuloor, J. Chem. Eng. Data 12, 15 (1967).
J. Wisniak, B. Yardeni, T. Sling, and H. Segura, J. Chem. Eng. Data 46, 223 (2001).
R. Barraza and J. Edwards, Monatsh. Chem. 112, 925 (1981).
S. J. Ashcroft, A. D. Claylon, and R. B. Shearn, J. Chem. Eng. Data 24, 195 (1979).
A. Arce, A. Marchiaro, O. Rodriguez, and A. Soto, J. Chem. Eng. Data 47, 529 (2002).
J. M. Sö rensen and W. Arlt, Liquid–Liquid Equilibrium Data Collection, Vol. V, Part 1 (DECHEMA, Frankfurt am Main, 1979), 470 pp.
F. Ruiz, D. Prats, and V. Gomis, J. Chem. Eng. Data 30, 412 (1985).
A. Arce, A. Arce Jr., J. MartÍnez-Ageitos, E. Rodil, O. RodrÍguez, and A. Soto, Fluid Phase Equilib. 170, 113 (2000).
E. R. Washburn and A. E. Beguin, J. Am. Chem. Soc. 62, 579 (1940).
A. I. Vorobeva and M. K. H. Karapetyants, Zh. Fiz. Khim. 41, 1984 (1967).
Z. J. Pan, Y. Chen, Y. H. Dong, R. Q. Li, and Y. Tang, J. Jinan Univ. Nat. Sci. Med. Ed. 25, 609 (2004).
J. Gmehling, J. Li, and M. Schiller, Ind. Eng. Chem. Res. 32, 178 (1993).
J. M. Prausnitz, T. F. Anderson, E. A. Grens, C. A. Eckert, R. Hsieh, and J. P. O'Connell, Computer Calculations for Multicomponent Vapor–Liquid and Liquid–Liquid Equilibria (Prentice-Hall, Englewood Cliffs, NJ, 1980).
K. Tamura, Y. Chen, and T. Yamada, J. Solution Chem. 30, 291 (2001).
J. A. Riddick, W. B. Bunger, and T. K. Sakano, Organic Solvents, 4th edn. (Wiley-Interscience, New York, 1986).
C. F. Spencer and R. P. Danner, J. Chem. Eng. Data 17, 236 (1972).
J. G. Hayden and J. P. O'Connell, Ind. Eng. Chem. Process. Des. Dev. 14, 209 (1975).
J. A. Nelder and P. Mead, Comput. J. 7, 308 (1965).
E. A. Macedo and P. Rasmussen, Liquid–Liquid Equilibrium Data Collection, Suppl. 1. Vol. V, Part 4 (DECHEMA, Frankfurt am Main, 1987).
Author information
Authors and Affiliations
Corresponding author
Rights and permissions
About this article
Cite this article
Chen, Y., Dong, Y. Liquid–Liquid Equilibria of Oxygenate Fuel Additives with Water at 298.15 K: Ternary and Quaternary Aqueous Systems of Diisopropyl Ether and Hydrocarbons with 2-Propanol. J Solution Chem 34, 1445–1457 (2005). https://doi.org/10.1007/s10953-005-8517-8
Received:
Revised:
Accepted:
Issue Date:
DOI: https://doi.org/10.1007/s10953-005-8517-8