Skip to main content
Log in

Liquid–Liquid Equilibria of the Methanol + Hexane + Methylcyclohexane + Toluene Quaternary System at T = 303.15 K

  • Published:
Journal of Solution Chemistry Aims and scope Submit manuscript

Abstract

Tie line data of the {methanol + methylcyclohexane + hexane} and {methanol + toluene + hexane} ternary systems were obtained at T = 303.15 K, while data for {methanol + toluene + methylcyclohexane} were taken from the literature. A quaternary system {methanol + methylcyclohexane + hexane + toluene} was also studied at the same temperature. In order to obtain the binodal surface of the quaternary system, four quaternary sectional planes with several hexane/methylcyclohexane ratios were studied. Experimental results show that the binodal surface in the solid diagram is small and that the highest toluene mass fraction values, beyond which only one phase is present for the methanol-rich phase and hydrocarbon-rich one, respectively, are: 0.052 and 0.064 for P1, 0.068 and 0.052 for P2, 0.047 and 0.107 for P3, 0.029 and 0.030 for P4. So, if this quaternary system contains the correct methanol and hydrocarbon concentrations, this blend can be used as a reformulated gasoline, because no phase separation should be observed. Ternary experimental results were correlated with the UNIQUAC and NRTL equations. The equilibrium data for the three ternary systems were used to determine interaction parameters for the UNIQUAC equation. The NRTL equation is more accurate than the UNIQUAC for the ternary systems studied here. The UNIQUAC equation fitted to the experimental data is more accurate than the UNIFAC method for this quaternary system.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Institutional subscriptions

Fig. 1
Fig. 2
Fig. 3
Fig. 4

Similar content being viewed by others

References

  1. García-Flores, B.E., Galicia-Aguilar, G., Eustaquio-Rincón, R., Trejo, A.: Liquid–liquid phase diagrams of ternary systems as a function of temperature: isooctane + aromatic + methanol with and without water. Fluid Phase Equilib. 185, 275–293 (2001)

    Article  Google Scholar 

  2. Gramajo de Doz, M.B., Bonatti, C.M., Barnes, N., Sólimo, H.N.: Liquid–liquid equilibria of ternary and quaternary systems including 2,2,4-trimethylpentane, benzene, ethanol, and water at 303.15 K. Sep. Sci. Technol. 37, 245–260 (2002)

    Article  Google Scholar 

  3. Arce, A., Blanco, M., Soto, A.: Determination and correlation of liquid–liquid equilibrium data for the quaternary system 1-octanol + 2-methoxy-2-methylbutane + water + methanol at 25 °C. Fluid Phase Equilib. 158–160, 949–960 (1999)

    Article  Google Scholar 

  4. Chen, J., Duan, L.-P., Mi, J.-G., Fei, W.-Y., Li, Z.-C.: Liquid–liquid equilibria of multi-component systems including n-hexane, n-octane, benzene, toluene, xylene and sulfolane at 298.15 K and atmospheric pressure. Fluid Phase Equilib. 173, 109–119 (2000)

    Article  CAS  Google Scholar 

  5. Gramajo de Doz, M.B., Bonatti, C.M., Sólimo, H.N.: Liquid–liquid equilibria of ternary and quaternary systems with two hydrocarbons, an alcohol, and water at T = 303.15 K. Systems containing cyclohexane, benzene, ethanol, and water. J. Chem. Thermodyn. 35, 2055–2065 (2003)

    Article  CAS  Google Scholar 

  6. Gramajo de Doz, M.B., Bonatti, C.M., Sólimo, H.N.: (Liquid + liquid) equilibria for methyl tert-butyl ether + benzene + cyclohexane + water at 303.15 K. Energy Fuels 19, 1977–1983 (2005)

    Article  CAS  Google Scholar 

  7. Gramajo, M.B., Veliz, J.H., Lucena, M.C., Gonzalez, D.A.: Liquid–liquid equilibria of methanol + toluene + methylcyclohexane at 278.15, 283.15, 288.15, 293.15, 298.15 and 303.15 K. J. Solution Chem. 42, 2025–2033 (2013)

    Article  CAS  Google Scholar 

  8. Treybal, R.E.: Liquid extraction, vol. 2. McGraw-Hill, New York (1963)

    Google Scholar 

  9. Abrams, D.S., Prausnitz, J.M.: A new expression for the excess Gibbs energy of partly or completely miscible systems. AIChE J. 21, 116–128 (1975)

    Article  CAS  Google Scholar 

  10. Renon, H., Prausnitz, J.M.: Local compositions in thermodynamic excess functions for liquid mixtures. AIChE J. 14, 135–144 (1968)

    Article  CAS  Google Scholar 

  11. Fredenslund, A., Gmehling, J., Rasmussen, P.: Vapour-liquid equilibria using UNIFAC. Elsevier, Amsterdam (1977)

    Google Scholar 

  12. Magnussen, T., Rasmusen, P., Fredenslund, A.: UNIFAC parameter table prediction of liquid–liquid equilibrium. Ing. Eng. Chem. Process Des. Dev. 20, 331–339 (1981)

    Article  CAS  Google Scholar 

  13. Gomis, V., Ruíz, F., Asensi, J.C., Saquete, M.D.: Procedure for checking and fitting experimental liquid–liquid equilibrium data. Fluid Phase Equilib. 129, 15–19 (1997)

    Article  CAS  Google Scholar 

  14. Sørensen, J.M.: ESTM. Phase equilibria and separation processes. MAN 8106. ESTM: estimation of UNIQUAC and NRTL parameters from ternary LLE data. Instituttet for Kemiteknik, Lyngby, Denmark (1980)

  15. Sørensen, J. M., Arlt, W.: Liquid–liquid equilibrium data collection. Ternary and quaternary systems, vol. V, part 3. Dechema Chemistry Data Series, Frankfurt (1980)

Download references

Acknowledgments

Financial support from the Consejo de Investigaciones de la Universidad Nacional de Tucumán, Argentina (CIUNT, Grant 26/E518) and Secretaria de Políticas Universitarias de la Nación Argentina “Proyecto Ing. Mosconi” Res. No. 3270 SPU, 20/11/2013 are gratefully acknowledged.

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to Mónica B. Gramajo.

Rights and permissions

Reprints and permissions

About this article

Check for updates. Verify currency and authenticity via CrossMark

Cite this article

Gramajo, M.B., Cases, A.M. Liquid–Liquid Equilibria of the Methanol + Hexane + Methylcyclohexane + Toluene Quaternary System at T = 303.15 K. J Solution Chem 44, 171–180 (2015). https://doi.org/10.1007/s10953-015-0301-9

Download citation

  • Received:

  • Accepted:

  • Published:

  • Issue Date:

  • DOI: https://doi.org/10.1007/s10953-015-0301-9

Keywords

Navigation