Skip to main content
Log in

First and second thermodynamic mixing functions of ethylbenzene+n-nonane, +n-decane, and+n-dodecane at 25 and 45°C

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

Abstract

Isothermal compressibilities κT and isobaric thermal expansion coefficients αp have been determined for mixtures of ethylbenzene+n-nonane, +n-decane, and +n-dodecane at 25 and 45°C in the whole range of composition. The excess functions\((\kappa _\nu ^V )^E = - (\partial V^{\text{E}} /\partial p)_{\text{T}} \) and\((\alpha p{\text{V}})^{\text{E}} = (\partial {\text{V}}^{\text{E}} /\partial T)_p \) have been obtained at each measured mole fraction. The first one\( - (\partial {\text{V}}^{\text{E}} /\partial p)_{\text{T}} )\) is zero for ethylbenzene +n-nonane, positive for ethylbenzene +n-decane, and +n-dodecane and increases with chain length n of the n-alkane. The\((\partial {\text{V}}^{\text{E}} /\partial T)_{\text{P}} \) function is positive for the three studied systems and nearly constant with n. Both mixing functions increase slightly with temperature. From this measurement and supplementary literature data of molar heat capacities at constant pressure C P , the isentropic compressibilities κS, the molar heat capacities at constant volume C V and the corresponding mixing functions have been calculated at 25°C. Furthermore, the pressure dependence of excess enthalpy HB,\((\partial H^{\text{E}} /\partial p)_{\text{T}} \) at zero pressure and at 25°C has been obtained from our experimental results of\((\partial V^{\text{E}} /\partial T)_{\text{P}} \) and experimental literature values for excess volume VE.

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.

Similar content being viewed by others

References

  1. A. D. Matilla, E. Aicart, M. Diaz Peña, and G. Tardajos,J. Solution Chem. 17, 000 (1988) (in press).

  2. M. Costas, H. V. Tra, D. Patterson, M. Caceres G. Tardajos and E. Aicart,J. Chem. Soc. Faraday Trans. I 84, 1603 (1988).

    Google Scholar 

  3. E. Aicart, G. Tardajos, and M. Costas,J. Solution Chem. (submitted).

  4. Selected Values of Physical Thermodynamic Properties of Hydrocarbons and Related Compounds, API Research Project 44. Thermodynamic Research Center (Texas A&M University, College Station, Texas 1977).

  5. M. Diaz Peña and M. L. McGlashan,Trans. Faraday Soc. 57, 1511 (1961);

    Google Scholar 

  6. M. Diaz Peña and G. Tardajos,J. Chem. Thermodynamics 10, 19 (1978).

    Google Scholar 

  7. M. Caceres J. M. Arsuaga, and J. Nuñez,Fluid Phase Equilibria 20, 81 (1985).

    Google Scholar 

  8. J. L. Fortier and G. C. Benson,J. Chem. Eng. Data 25, 47 (1980).

    Google Scholar 

  9. J. F. Messerly, G. B. Guthrie, S. S. Todd, and H. L. Finke,J. Chem. Eng. Data 12, 338 (1967).

    Google Scholar 

  10. J. P. E. Grolier, A. Faradjzadeh, and H. V. Keihaian,Thermochim. Acta 53, 157 (1982).

    Google Scholar 

  11. Y. P. Handa, C. J. Halpin, and G. C. Benson,J. Chem. Thermodynn 13, 875 (1981).

    Google Scholar 

  12. J. J. Christensen, J. B. Ott, and J. F. Moellmer,J. Chem. Thermodynn 9, 249 (1977).

    Google Scholar 

Download references

Author information

Authors and Affiliations

Authors

Rights and permissions

Reprints and permissions

About this article

Cite this article

Matilla, A.D., Tardajos, G., Diaz Peña, M. et al. First and second thermodynamic mixing functions of ethylbenzene+n-nonane, +n-decane, and+n-dodecane at 25 and 45°C. J Solution Chem 18, 893–901 (1989). https://doi.org/10.1007/BF00685064

Download citation

  • Received:

  • Issue Date:

  • DOI: https://doi.org/10.1007/BF00685064

Key words

Navigation