Thermodynamic Model Used to Predict Supercritical Carbon Dioxide Separation of an Ethanol-Octane Mixture: Feasibility Studies

R. Davarnejad; K. Kassim; A. Zainal; Suhairi Sata

Thermodynamic Model Used to Predict Supercritical Carbon Dioxide Separation of an Ethanol-Octane Mixture: Feasibility Studies

Year 2009, Volume: 12 Issue: 1, 51 - 59, 01.03.2009

R. Davarnejad K. Kassim A. Zainal Suhairi Sata

Abstract

Mutual solubilities of a mixture containing 80.52% ethanol and 19.48% octane were measured in a carbon dioxide solvent using a high-pressure type phase equilibrium apparatus at pressures up to 100 bar and at a temperature of 75°C. Experimental results showed that a considerable separation was not achieved in the ethanol-octane ratio investigated in this work. The experimental data were then compared with the theoretical data which were obtained from the regular solution equations. Regular solution theory was employed for each phase by applying activity coefficient expressions. The regular solution theory approach has been found to be encouraging for the prediction of solubility data (vapor phase data) and also showed that the interaction parameters were dependent on pressure.

Keywords

supercritical extraction , regular solution theory , ethanol-octane mixture , carbon dioxide solvent , miscibility

Year 2009, Volume: 12 Issue: 1, 51 - 59, 01.03.2009

R. Davarnejad K. Kassim A. Zainal Suhairi Sata

Abstract

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Details

Primary Language	English
Authors	R. Davarnejad This is me K. Kassim This is me A. Zainal This is me Suhairi Sata This is me
Publication Date	March 1, 2009
Published in Issue	Year 2009 Volume: 12 Issue: 1

Cite

APA	Davarnejad, R., Kassim, K., Zainal, A., Sata, S. (2009). Thermodynamic Model Used to Predict Supercritical Carbon Dioxide Separation of an Ethanol-Octane Mixture: Feasibility Studies. International Journal of Thermodynamics, 12(1), 51-59.
AMA	Davarnejad R, Kassim K, Zainal A, Sata S. Thermodynamic Model Used to Predict Supercritical Carbon Dioxide Separation of an Ethanol-Octane Mixture: Feasibility Studies. International Journal of Thermodynamics. March 2009;12(1):51-59.
Chicago	Davarnejad, R., K. Kassim, A. Zainal, and Suhairi Sata. “Thermodynamic Model Used to Predict Supercritical Carbon Dioxide Separation of an Ethanol-Octane Mixture: Feasibility Studies”. International Journal of Thermodynamics 12, no. 1 (March 2009): 51-59.
EndNote	Davarnejad R, Kassim K, Zainal A, Sata S (March 1, 2009) Thermodynamic Model Used to Predict Supercritical Carbon Dioxide Separation of an Ethanol-Octane Mixture: Feasibility Studies. International Journal of Thermodynamics 12 1 51–59.
IEEE	R. Davarnejad, K. Kassim, A. Zainal, and S. Sata, “Thermodynamic Model Used to Predict Supercritical Carbon Dioxide Separation of an Ethanol-Octane Mixture: Feasibility Studies”, International Journal of Thermodynamics, vol. 12, no. 1, pp. 51–59, 2009.
ISNAD	Davarnejad, R. et al. “Thermodynamic Model Used to Predict Supercritical Carbon Dioxide Separation of an Ethanol-Octane Mixture: Feasibility Studies”. International Journal of Thermodynamics 12/1 (March2009), 51-59.
JAMA	Davarnejad R, Kassim K, Zainal A, Sata S. Thermodynamic Model Used to Predict Supercritical Carbon Dioxide Separation of an Ethanol-Octane Mixture: Feasibility Studies. International Journal of Thermodynamics. 2009;12:51–59.
MLA	Davarnejad, R. et al. “Thermodynamic Model Used to Predict Supercritical Carbon Dioxide Separation of an Ethanol-Octane Mixture: Feasibility Studies”. International Journal of Thermodynamics, vol. 12, no. 1, 2009, pp. 51-59.
Vancouver	Davarnejad R, Kassim K, Zainal A, Sata S. Thermodynamic Model Used to Predict Supercritical Carbon Dioxide Separation of an Ethanol-Octane Mixture: Feasibility Studies. International Journal of Thermodynamics. 2009;12(1):51-9.