PHASE BEHAVIOUR CALCULATIONS FOR THE CARBON DIOXIDE + 1,2-DIMETHOXYETHANE BINARY SYSTEM WITH A CUBIC EQUATION OF STATE

Authors

  • Sergiu SIMA Department of Inorganic Chemistry, Physical Chemistry and Electrochemistry, Faculty of Applied Chemistry and Materials Science, Politehnica University, Bucharest, Romania. Email: sergiu.sima@upb.ro. https://orcid.org/0000-0002-4789-7287
  • Radu C. RACOVIŢĂ Department of Inorganic Chemistry, Physical Chemistry and Electrochemistry, Faculty of Applied Chemistry and Materials Science, Politehnica University, Bucharest, Romania. Email: radu.racovita@upb.ro. https://orcid.org/0000-0002-6396-9869
  • Aurel CHIRILĂ Department of Electrical Machines, Drives, and Materials, Faculty of Electrical Engineering, Politehnica University, Bucharest, Romania. Email: aurel.chirila@upb.ro.
  • Dragoș DEACONU Department of Electrical Machines, Drives, and Materials, Faculty of Electrical Engineering, Politehnica University, Bucharest, Romania. Email: dragos.deaconu@upb.ro.
  • Viorel FEROIU Department of Inorganic Chemistry, Physical Chemistry and Electrochemistry, Faculty of Applied Chemistry and Materials Science, Politehnica University, Bucharest, Romania. Email: v_feroiu@chim.upb.ro. https://orcid.org/0000-0002-1653-3376
  • Catinca SECUIANU Department of Inorganic Chemistry, Physical Chemistry and Electrochemistry, Faculty of Applied Chemistry and Materials Science, Politehnica University, Bucharest, Romania; Department of Chemical Engineering, Imperial College London, United Kingdom. Email: catinca.secuianu@upb.ro. https://orcid.org/0000-0001-5779-6415

DOI:

https://doi.org/10.24193/subbchem.2019.3.11

Keywords:

carbon dioxide, 1,2-dimethoxyethane, high-pressures, vapour-liquid equilibrium, equations of state, GEOS, GEOS3C

Abstract

The ability of different thermodynamic models to predict the phase behaviour of carbon dioxide (1) + 1,2-dimethoxyethane (2) binary system is tested. The model chosen is the General Equation of State (GEOS) coupled with classical van der Waals mixing rules (two-parameter conventional mixing rule, 2PCMR). Comparisons were made with the GEOS3C, Soave-Redlich-Kwong (SRK), and Peng-Robinson (PR) cubic equations of state (EoS) too. A single set of binary parameters for each model was used to predict correctly the global phase behaviour of the system. 

 

References

https://www.epa.gov/ghgemissions/overview-greenhouse-gases, accessed July 2019

IPCC, Climate Change 2014: Mitigation of Climate Change: Contribution of Working Group III to the Fifth Assessment Report of the Intergovernmental Panel on, Cambridge University Press, 2014

M.T. Mota-Martinez; J.P. Hallett; N. Mac Dowell, Sustain. Energ. Fuels, 2017, 1, 2078-2090

https://www.iea.org/geco/emissions/, accessed July 2019

M. Bui; M. Fajardy; N. Mac Dowell; Fuel, 2018, 213, 164-175

C. Secuianu; V. Feroiu; D. Geană; J. Chem. Eng. Data, 2010, 55 (10), 4255–4259

S. Sima; J.M. Milanesio; J.I. Ramello; M. Cismondi; C. Secuianu; V. Feroiu; D. Geană; J. Chem. Thermodyn., 2016, 93, 374-385

A.V. Crişciu; S. Sima; A.-S. Deaconu; A. Chirilă; D. Deaconu; C. Secuianu; V. Feroiu; Rev. Chim.-Bucharest, 2016, 67 (10), 1984-1989

S. Sima; S. Ionită; C. Secuianu; V. Feroiu; D. Geană; J. Chem. Eng. Data, 2018, 63 (4), 1109-1122

S. Sima; R.C. Racoviţă; C. Dincă; V. Feroiu; C. Secuianu; Univ. Politeh. Buchar. Sci. Bull.-Ser. B-Chem. Mat. Sci., 2017, 79 (4), 11-24

C. Secuianu; V. Feroiu; D. Geană; Fluid Phase Equilib., 2016, 428, 62-75

S. Secuianu; S. Ioniţă; V. Feroiu; D. Geană; J. Chem. Thermodyn., 2016, 93, 360-373

S. Ioniţă; C. Secuianu; V. Feroiu; D. Geană; Univ. Politeh. Buchar. Sci. Bull.-Ser. B-Chem. Mat. Sci., 2015, 77 (1), 31-40

S. Sima; C. Secuianu; V. Feroiu; D. Geană; Cent. Eur. J. Chem., 2014, 12 (9), 953-961

S. Sima; C. Secuianu; V. Feroiu; D. Geană; Cent. Eur. J. Chem., 2014, 12 (9), 893-900

S. Sima; C. Secuianu; V. Feroiu; Fluid Phase Equilib., 2018, 458, 47-57

C. Secuianu; J. Qian; R. Privat; J.-N. Jaubert; Ind. Eng. Chem. Res., 2012, 51, 11284-11293

J. Gujt, H. Dominguez; S. Sokolowski; O. Pizio; Cond. Matt. Phys., 2017, 20, 1–14

A. Jänes; J. Eskusson; T. Thomberg; T. Romann; E. Lust; J. Energy Chem., 2016, 25, 609–614.

D. Geană; Rev. Chim. (Bucharest), 1986, 37, 303-309

D. Geană; Rev. Chim. (Bucharest), 1986, 37, 951-959

D. Geană; Rev. Chim. (Bucharest), 1987, 38, 975-979

D. Geană; V. Feroiu; Fluid Phase Equilib., 2000, 174, 51–68

D. Geană; V. Feroiu; Ecuaţii de stare. Aplicaţii la echilibre de faze, Ed. Tehnică: Bucharest, Romania, 2000

C. Secuianu; V. Feroiu; D. Geană; J. Supercrit. Fluid., 2008, 47 (2), 109-116

D. Geană; L. Rus; Phase equilibria database and calculation program for pure components systems and mixtures, in Proc. Romanian Int. Conf. Chem. Chem. Eng. (RICCCE XIV), Bucharest, Romania, 2005; Volume 2, pp.170–178

R.A. Heidemann; A. M. Khalil; AIChE J., 1980, 26, 769–779

R. Stockfleth; R. Dohrn; Fluid Phase Equilib., 1998, 145, 43–52

Evaluated Standard Thermophysical Property Values, DIPPR Project 801 full version, Brigham Young University, Provo Utah, 2005

P.H. van Konynenburg; R.L. Scott; Philos. Trans. R. Soc. Lond.-Ser. A, 1980, 298, 495–540

R. Privat; J.-N. Jaubert; Chem. Eng. Res. Des., 2013, 91, 1807–1839.

STUDIA UBB CHEMIA, Volume 64 (LXIV), No. 3, September 2019

Downloads

Published

2019-09-30

How to Cite

SIMA, S. ., RACOVIŢĂ, R. C. ., CHIRILĂ, A. ., DEACONU, D. ., FEROIU, V. ., & SECUIANU, C. . (2019). PHASE BEHAVIOUR CALCULATIONS FOR THE CARBON DIOXIDE + 1,2-DIMETHOXYETHANE BINARY SYSTEM WITH A CUBIC EQUATION OF STATE. Studia Universitatis Babeș-Bolyai Chemia, 64(3), 129–142. https://doi.org/10.24193/subbchem.2019.3.11

Issue

Volume 64, No. 3, 2019

Section

Articles

License

Copyright (c) 2019 Studia Universitatis Babeș-Bolyai Chemia

Creative Commons License

This work is licensed under a Creative Commons Attribution-NonCommercial-NoDerivatives 4.0 International License.

Similar Articles

<< < 24 25 26 27 28 29 30 31 32 > >> 

You may also start an advanced similarity search for this article.