Prediction of the Solubility of Benzoic Acid in Supercritical CO2 Using the PC-SAFT EoS
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Prediction of the Solubility of Benzoic Acid in Supercritical CO2 Using the PC-SAFT EoS

Authors: Hamidreza Bagheri, Alireza Shariati

Abstract:

There are many difficulties in the purification of raw components and products. However, researchers are seeking better ways for purification. One of the recent methods is extraction using supercritical fluids. In this study, the phase equilibria of benzoic acid -supercritical carbon dioxide system were investigated. Regarding the phase equilibria of this system, the modeling of solid-supercritical fluid behavior was performed using the Perturbed-Chain Statistical Association Fluid Theory (PC-SAFT) and Peng-Robinson equations of state (PR EoS). For this purpose, five PC-SAFT EoS parameters for pure benzoic acid were obtained using its experimental vapor pressure. Benzoic acid has association sites and the behavior of the benzoic acid-supercritical fluid system was well predicted using both equations of state, while the binary interaction parameter values for PR EoS were negative. Genetic algorithm, which is one of the most accurate global optimization algorithms, was also used to optimize the pure benzoic acid parameters and the binary interaction parameters. The AAD% value for the PC-SAFT EoS, were 0.22 for the carbon dioxide-benzoic acid system.

Keywords: Supercritical fluids, Solubility, Solid, PC-SAFT EoS, Genetic algorithm.

Digital Object Identifier (DOI): doi.org/10.5281/zenodo.1336957

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[1] Y. Tanaka and O. Takeshi, "Extraction of Phospholipids from Salmon Roe with Supercritical Carbon Dioxide and an Entrainer”, J. Oleo Sci., Japan Oil Chemists Society, 53(9): 417–424 (2004).
[2] M. Ollanketo, K. Hartonen, M. Riekkola, Y. Holm, R. Hiltunen, "Supercritical carbon dioxide extraction of lycopene in tomato skins” (2001), Eur. Food Res. Technol. 212 561–565.
[3] N.L. Rozzi, R.K. Singh, R.A. Vierling, B.A. Watkins, "Supercritical fluid extraction of lycopene from tomato processing byproducts” J. Agric. Food Chem. 50 (2002) 2638–2643.
[4] CL. Phelps, NG. Smart, CM. Wai, Past, "Present and possible future applications of supercritical fluid extraction technology”, J. Chem. Educ., 1163: 73 (1996).
[5] U. Nguyen, D. A. Evans, D. J. Berger, and Calderon, "Process for the Supercritical Extraction and Fractionation of Spices”, US Patent 5,120,558 (1992).
[6] M. Gehrig, "Extraction of Natural Material with Carbon Dioxide”: Current Applications in Handouts, NATO ASI on Supercritical Fluids IIÐ Fundamentals and Applications, Kemer, Turkey (1998).
[7] LiF. and Hsieh, Y. "Supercritical fluid chromatography-mass spectrometry for chemical analysis", J. Sep. Sci., 31, 1231-1237 (2008).
[8] M. Saito, "History of supercritical fluid chromatography: Instrumental development”. J. Bioengineering, 590-599, (2013).
[9] G. Xu, A. M. Scurto, M. Castier, J. F. Brennecke and M. A. Stadtherr, "Reliable computation of high-pressure solid- fluid equilibrium”, Ind. Eng. Chem. Res.1624-1636, (2000).
[10] G. B. Solórzano, "Supercritical fluid technology: computational and experimental equilibrium studies and design of supercritical extraction processes”, Ph.D. Thesis, Graduate School, University of Notre Dame, USA, (2004).
[11] M. N. Ponte, "The thermodynamics of supercritical fluids, Science and Technology Faculty”, Nova de Lisbon University, Portugal.40-42, (2001).
[12] B. Francesca, D. V. Sara, and G. Fausto, "Supercritical extraction column for separation of limonene and citral”, Paper no. 782, University of Roma, Italy, (2000).
[13] Q. Li, Z. Zhang, C. Zhong, Y. Liu, Q. Zhou, "Solubility of solid solutes in supercritical carbon dioxide with and without co-solvents”, Fluid Phase Equilibrium. 207 (2003) 183–192.
[14] M.J. Periago, F. Rincon, M.D. Aguera, G. Ros, "Mixture approach for optimizing lycopene extraction from tomato and tomato products”, J. Agric. Food Chem. 52 (2004) 5796–5802.
[15] R. Prasad, and H. J. Grubbs, "Process and Apparatus forthe Semi continuous Extraction of Nicotine from Tobacco”, US Patent 5,497,792(1996).
[16] C.S. Yeh, T. Yu, and A. Berthod, "Separation of steroidsby countercurrent chromatography using supercritical fluidcarbon dioxide”, J. Liq. Chrom. And Rel. Technol. 22, 345-356(1999).
[17] X. Xu, T. D. Veenstra, S. D. Fox, J. M. Roman, H. J., Issaq, R. Falk, J. E. Saavedra, L. K. Keefer, and R. G. Ziegler, "Measuring fifteen endogenous estrogens simultaneously in human urine by high-performance liquid chromatography- mass spectrometry”, Anal. Chem., 77, 6646-6654 (2005).
[18] Z. Yu, B. Singh, S.S.H. Rizvi, J.A. Zollewg, "Solubilities of fatty acids, fatty acid esters, and fats and oils in supercritical carbon dioxide”, J. Supercrit. Fluids 7 (1994) 51.
[19] R. Murga, M. T. Sanaz, S. Beltran, and J. L. Cabezas, "Solubility of three Hydroxycinnamic Acids in Supercritical Carbon Dioxide”, J. Supercrit. Fluids 27 (2003) 239-245.
[20] S. X. Yang, H. Li, and J. Shi, "Modeling of supercritical fluid extraction by neural networks”, Intelligent Automation and Soft Computing,3-12, (2003).
[21] T. Wang, M. Barber, I. Hardt, and D. B. Kassel, "Mass-directed fractionation and isolation of pharmaceutical compounds by packed-column supercritical fluid chromatography/mass spectrometry”, Rapid Commun. Mass Spectrum, 15, 2067-2075 (2001).
[22] C. H. Harris, "Product review: the SFC comeback”, Anal. Chem., 74, 87A-91A (2002).
[23] H. Yang, C. Zhong, "Modeling of the solubility of organic compounds in supercritical carbon dioxide – cosolvent system using SAFT equation of state”,J. Supercrit. Fluids 33 (2005) 99–106.
[24] D. M. Kassim, D. Al-Sammerrai, and F. Paulus, "Near critical carbon dioxide extraction of oxidation products from base stock mineral oils”, Sep. Sci. Tech.157-164, (1987).
[25] J.M. Smith, H.C. Van Ness, M.M. Abbott, "Introduction to Chemical Engineering Thermodynamics”, McGraw-Hill, 7th edition, New York, (2005).
[26] P. Coimbra, M. H. Gil, C. M. M. Duarte, B. M. Heron, and H. C. de Sousa, "Solubility of a Spiroindolinonaphthoxazine photo chromic dye in Supercritical carbon dioxide: Experimental determination and correlation”, Fluid Phase Equilibrium, 120-128 (2005).
[27] A. Danesh, "PVT and phase behaviour of petroleum reservoir fluids” Elsevier Science, 1th, Amsterdam,(1998).
[28] Huang, S. H., Radosz, M., "Equation of state for small, large, polydisperse, and associating molecules” Ind. Eng. Chem. Res. (1990), 29, 2284-2294.
[29] J. Gross, G. Sadowski, "Perturbed-Chain SAFT: An Equation of State Based on a Perturbation Theory for Chain Molecules”, Ind. Eng. Chem. Res., 2001, 40, 1244-1260.