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Received March 25, 2022
Accepted June 2, 2022
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Liquid-liquid equilibrium (LLE) data of ternary mixtures of [water+acetic acid+1-nonanol] and [water+acetic acid+1-decanol] at 298.2-318.2 K and 101.3 kPa
Department of Chemical and Biomolecular Engineering, Sogang University, C.P.O. Box, 1142, Seoul 04107, Korea 1Department of Chemical and Biomolecular Engineering, University of Maryland, College Park, MD 20742, USA
limjs@sogang.ac.kr
Korean Journal of Chemical Engineering, December 2022, 39(12), 3422-3433(12), 10.1007/s11814-022-1196-y
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Abstract
The addition of alcohols to acetic acid and water mixture is effective for extracting acetic acid from the mixture. This work presents the liquid-liquid phase equilibrium (LLE) data of the ternary systems of 1-nonanol/acetic acid/water and 1-decanol/acetic acid/water measured at 298.2, 303.2, 308.2, and 318.2 K at 101.3 kPa. The effectiveness of the extraction process was quantified by the distribution coefficient (D) and selectivity (S). It was found that the extraction capability of 1-nonanol was superior to that of 1-decanol. We also used the Hand plot and the Othmer?Tobias plot to assess the reliability of the experimental LLE data, and the linear coefficient was greater than 0.99. The non-random two-liquid (NRTL) and the universal quasichemical (UNIQUAC) model were also used to correlate the experimental data. The Gibbs energy minimization method was used to evaluate the reliability of the regression parameters of the statistical model. The calculated root mean square deviation (RMSD) values were less than 0.023, indicating that both models were adequate for these systems.
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Fahim MA, Al-Muhtaseb SA, Al-Nashef IM, J. Chem. Eng. Data, 42, 183 (1997)
Tan TC, Aravinth S, Fluid Phase Equilib., 163, 243 (1999)
Al-Muhtaseb SA, Fahim MA, Fluid Phase Equilib., 123, 189 (1996)
Esquível MM, Bernardo-Gil MG, Fluid Phase Equilib., 57, 307 (1990)
Aljimaz AS, Fandary MSH, Alkandary JA, Fahim MA, J. Chem. Eng. Data, 45, 301 (2000)
Jia K, Zhing T, Feng L, Zhang C, Xu X, J. Chem. Thermodyn., 153, 106305 (2021)
Feng L, Zhang W, Ge M, Yi Y, J. Chem. Eng. Data,, 65, 1531 (2020)
Ebrahimkhani MJ, Azadian M, J. Chem. Eng. Data, 67, 404 (2022)
Jeong AY, Cho JA, Kim Y, Cho HK, Choi KY, Lim JS, Korean J. Chem. Eng., 35, 1328 (2018)
Yim JH, Park KW, Lim JS, Choi KY, J. Chem. Eng. Data, 64, 3882 (2019)
Taylor BN, Kuyatt CE, NIST Technical Note 1297 1994 Edition, Guidelines for Evaluating and Expressing the Uncertainty of NIST Measurement Results, Natl. Inst. Stand. Technol., 1 (1994).
Othmer D, Tobias P, Ind. Eng. Chem., 34, 693 (1942)
Hand DB, J. Phys. Chem., 34, 1961 (1930)
Renon H, Prausnitz JM, AIChE J., 4, 135 (1968)
Abrams DS, Prausnitz JM, AIChE J., 21, 116 (1975)
Marcilla A, Reyes-Labarta JA, Olaya MM, Fluid Phase Equilib., 433, 243 (2017)
Reyes-Labarta, J. A. Graphical User Interface (GUI) for the Representation of GM Surfaces (Using the NRTL Model) and Curves, Including Tie-Lines and Hessian Matrix. Universidad de Alicante (2015).