Gas-Liquid Equilibrium Prediction of Co2-Ethanol System at Moderate Pressures and Different Temperatures

https://doi.org/10.24237/djes.2010.03107

Authors

  • Arkan Jasim Hadi College of Engineering, University of Tikrit

Keywords:

Gas-liquid equilibrium, Carbon dioxide, Ethanol, Moderate pressure, Mixing rules, SRK-EOS, PR-EOS, HYSYS program

Abstract

In this work, a thermodynamic model for the prediction of gas-liquid equilibrium at moderate pressures (up to 19 bar) and different temperatures (288-323 K) for the binary system of carbon dioxide (1)-ethanol (2) is established using Soave-Redlich-Kwong equation of state (SRK-EOS), Peng-Robenson equation of state (PR-EOS), and HYSYS program with same equations of state. Three different mixing rules were used to show the effect of the type of mixing rule. A comparison of experimental phase equilibrium data in the literature with the predicted results showed very good representation for some mixing rules and good for the others, also the comparison with the results obtained using simulation on HYSYS program exhibits  good agreement up to 11 bar with a deviation of  4*10-4 - 2*10-4 %.

Downloads

Download data is not yet available.

References

E. Wilhelm, R. Battino, and R.J. Wilcock, Chem. Rev. 1977, vol. 77, pp:219–262.

I. Dalmolin, E. Skovroinski, A. Biasi, M.L. Corazza, C. Dariva, and J. Vladimir Oliveira; 2006, "Solubility of carbon dioxide in binary and ternary mixtures with ethanol and water". Fluid phase Equilibria, vol.245, pp:193-200.

Octavio Elizalde-Solis, Luis A. Galicia-Luna, and Luis E. Camacho-Camacho; 2007 "High-pressure vapor–liquid equilibria for CO2 + alkanol systems and densities of n-dodecane and n-tridecane" Fluid phase Equilibria, vol.259, pp:23-32.

Minqiang Hou, Shuguang Liang, Zhaofu Zhang, Jiyuan Song, and Tao Jiang, Buxing Han.;2007, "Determination and modeling of solubility of CO2 in PEG200 + 1-pentanol and PEG200 + 1-octanol mixtures" Fluid phase Equilibria, vol.258, pp:108-114.

O. Elizalde-Solis, and L.A. Galicia-Luna.; 2005, "Solubility of thiophene in carbon dioxide and carbon dioxide + 1-propanol mixtures at temperatures from 313 to 363K" Fluid phase Equilibria, vol.230, pp:51-57.

Hyprotech Ltd.; 2002. Dynamic Modeling, HYSYS 3. pp:1-3.

Hyprotech Ltd.; 2002. Operations Guids, HYSYS 3.pp:1-3.

J. M. Smith, H. C.,Van Ness, and M. M. Abbott; 2005. Introduction to Chemical Engineering Thermodynamics, 7th Edn., McGraw. Hill Book Company, Cha.3, pp:90

Soave, G, 1972; "Equilibrium constants from a modified Redlich-Kwong equation of state" Chem.Eng.Science, vol.27, pp:1197-1203.

Peng, D.-Y., and Robinson, D.B; 1976, "A new two-constant equation of state" Ind. Eng. Chem. Fundamen., vol.15, pp:59-64.

Walas, S. M., 1985. Phase Equilibria in Chemical Engineering. Butterworth Publishers, USA.

Adachi, Y., and Sugie, H. A; 1986. New Mixing Rule - Modified Conventional Mixing Rule. Fluid Phase Eq., vol.28, pp:103.

Published

2010-06-01

How to Cite

[1]
Arkan Jasim Hadi, “Gas-Liquid Equilibrium Prediction of Co2-Ethanol System at Moderate Pressures and Different Temperatures”, DJES, vol. 3, no. 1, pp. 90–105, Jun. 2010.