Skip to main content
Log in

Modeling of the Interfacial Behavior of Carbon Dioxide + Methyl Myristate, Carbon Dioxide + Palmitate, and Carbon Dioxide + Methyl Myristate + Methyl Palmitate Mixtures Using CPA-EOS and Gradient Theory

  • Published:
International Journal of Thermophysics Aims and scope Submit manuscript

Abstract

This work presents the vapor–liquid equilibrium and the interfacial behavior modeling of binary and ternary CO\(_2\) + ester mixtures, with the cubic plus association equation of state (CPA-EOS) combined with the density gradient theory. The binary mixtures, CO\(_2\) + methyl myristate and CO\(_2\) + methyl palmitate, were studied at temperatures from 313.15 K to 333.15 K, considering the ester molecules as non-associating and the carbon dioxide as non-associating or self-associating (2B scheme) molecule. Phase behavior was predicted with binary interaction parameters adjusted from binary mixture phase equilibrium experimental data. Results show than there are some points better represented by the associating scheme, but the overall trend shows that the CPA-EOS with the non-associating scheme for all the molecules is the best option for describing the phase equilibrium and calculating the interfacial tension for the CO\(_2\) + ester binary mixtures. For this reason, the CO\(_2\) + methyl myristate + methyl palmitate mixture at 313.15 K was modeled only with non-associating fluids. The AAD% for the calculated interfacial tensions, considering non-associating molecules in the mixture is 9.7 % for the CO\(_2\) + methyl myristate mixture, 15.1 % for the CO\(_2\) + methyl palmitate mixture, and 7.9 % for the CO\(_2\) + methyl myristate + methyl palmitate mixture.

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.

Fig. 1
Fig. 2
Fig. 3
Fig. 4
Fig. 5
Fig. 6
Fig. 7
Fig. 8
Fig. 9
Fig. 10
Fig. 11
Fig. 12
Fig. 13
Fig. 14
Fig. 15
Fig. 16
Fig. 17
Fig. 18
Fig. 19
Fig. 20

Similar content being viewed by others

Abbreviations

\(\kappa\) :

Influence parameter

A :

Adjustable parameter of the influence parameter

a :

Attractive parameter in CPA-EOS

\(a_0\) :

Adjustable parameter of the CPA-EOS

AAD :

Statistical deviation

B :

Adjustable parameter of the influence parameter

b :

Covolume parameter in the CPA-EOS

\(c_1\) :

Adjustable parameter of the CPA-EOS

\(f_0\) :

Helmholtz energy density

g :

The radial distribution function

\(k_{ij}\) :

Interaction parameter in the CPA-EOS

n :

Number of points

\(n_c\) :

Number of components

P :

Absolute pressure

R :

Universal gas constant

T :

Absolute temperature

x :

Liquid mole fraction

\(X_{A_i}\) :

The mole fraction of the molecule i not bonded at site A

y :

Vapor mole fraction

z :

Position in the interface

\(\beta ^{A_i B_i}\) :

Association volume

\(\beta ^{A_i B_j}\) :

Cross-association volume

\(\Delta ^{A_i B_j}\) :

The association strength

\(\epsilon ^{A_i B_i}\) :

Association energy

\(\epsilon ^{A_i B_j}\) :

Cross-association energy

\(\eta\) :

Reduced density

\(\gamma\) :

Interfacial tension

\(\kappa _{ij}\) :

Cross-influence parameter

\(\mu\) :

Chemical potential

\(\Omega\) :

Grand thermodynamic potential

\(\rho\) :

Mole density

c :

Critical condition

ijs :

Species

0:

Equilibrium condition

exp :

Experimental

L :

Liquid phase

theo :

Theoretical

V :

Vapor phase

References

  1. G.M. Kontogeorgis, E.C. Voutsas, I.V. Yakoumis, D.P. Tassios, Ind. Eng. Chem. Res. 35, 4310–4318 (1996)

    Article  Google Scholar 

  2. I.V. Yakoumis, G.M. Kontogeorgis, E.C. Voutsas, D.P. Tassios, Fluid Phase Equilib. 130, 31–47 (1997)

    Article  Google Scholar 

  3. M.B. Oliveira, A.J. Queimada, G.M. Kontogeorgis, J.A.P. Coutinho, J. Supercrit. Fluids 55, 876–892 (2011)

    Article  Google Scholar 

  4. G.M. Kontogeorgis, I.V. Yakoumis, H. Meijer, E. Hendriks, T. Moorwood, Fluid Phase Equilib. 158, 201–209 (1999)

    Article  Google Scholar 

  5. T.Y. Kwak, G.A. Mansoori, Chem. Eng. Sci. 41, 1303–1309 (1986)

    Article  Google Scholar 

  6. G.K. Folas, G.M. Kontogeorgis, M.L. Michelsen, E.H. Stenby, Ind. Eng. Chem. Res. 45, 1527–1538 (2006)

    Article  Google Scholar 

  7. A. Hernández, M. Cartes, A. Mejía, Fuel 229, 105–115 (2018)

    Article  Google Scholar 

  8. A. Hernández, Chem. Phys. 534, 110747 (2020)

  9. A. Hernández, Int. J. Thermophys. 41, 1–18 (2020)

    Article  Google Scholar 

  10. A. Hernández, S. Khosharay, Int. J. Thermophys. 41, 1–22 (2020)

    Article  Google Scholar 

  11. A. Hernández, Int. J. Thermophys. 42, 1–27 (2020)

    Google Scholar 

  12. B.S. Carey, PhD thesis, University of Minnesota (1979)

  13. J. Wisniak, A. Apelblat, H. Segura, Chem. Eng. Sci. 53, 743–751 (1998)

    Article  Google Scholar 

  14. A. Hartono, I. Kim, Calculation of Vapor-liquid Equilibria for Methanol-water Mixture using Cubic-plus-association Equation of State (NTNU, 2004). http://folk.ntnu.no/haugwarb/KP8108/Essays/ardi_hartono_and_inna_kim.pdf. Accessed 09 Nov 2020

  15. J.M. Prausnitz, R.N. Lichtenthaler, E. Gomes, Molecular Thermodynamics of Fluid-phase Equilibria, 3rd edn. (Prentice Hall, 1999), pp 16

  16. L.M.C. Pereira, A. Chapoy, R. Burgass, M.B. Oliveira, J.A.P. Coutinho, B. Tohidi, J. Chem. Thermodyn. 93, 404–415 (2015)

    Article  Google Scholar 

  17. C.A. Lockemann, Chem. Eng. Process. 33, 171–187 (1994)

    Article  Google Scholar 

  18. C.A. Lockemann, Chem. Eng. Process. 33, 193–198 (1994)

    Article  Google Scholar 

  19. P.M.W. Cornelisse, C.J. Peters, J. de Swaan Arons, Mol. Phys. 80, 941–955 (1993)

    Article  ADS  Google Scholar 

  20. A. Mejía, H. Segura, J. Wisniak, I. Polishuk, J. Phase Equilib. Diffus. 26, 215–224 (2005)

    Article  Google Scholar 

  21. D. Zabala, A. Wender, Revista INGENIERÍA UC 23, 237–246 (2016)

    Google Scholar 

  22. P. Saxena, J.C. Patel, M.H. Joshipura, Procedia Eng. 51, 403–408 (2013)

    Article  Google Scholar 

  23. M.J. Pratas, M.B. Oliveira, M.J. Pastoriza-Gallego, A.J. Queimada, M. Pineiro, J.A.P. Coutinho, Energy Fuels 25, 3806–3814 (2011)

    Article  Google Scholar 

  24. T.E. Daubert, R.P. Danner, Taylor & Francis: Bristol, PA. (1989)

  25. C.S. Nevin, P.M. Althouse, H.O. Triebold, J. Am. Oil Chem. Soc. 28, 325–327 (1951)

    Article  Google Scholar 

Download references

Acknowledgements

A.H acknowledges the economic support given by the UCSC.

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to Ariel Hernández.

Additional information

Publisher's Note

Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.

Rights and permissions

Reprints and permissions

About this article

Check for updates. Verify currency and authenticity via CrossMark

Cite this article

Hernández, A., Zabala, D. Modeling of the Interfacial Behavior of Carbon Dioxide + Methyl Myristate, Carbon Dioxide + Palmitate, and Carbon Dioxide + Methyl Myristate + Methyl Palmitate Mixtures Using CPA-EOS and Gradient Theory. Int J Thermophys 42, 31 (2021). https://doi.org/10.1007/s10765-020-02788-4

Download citation

  • Received:

  • Accepted:

  • Published:

  • DOI: https://doi.org/10.1007/s10765-020-02788-4

Keywords

Navigation