Abstract
Liquid–liquid equilibria (LLE) data for {water + 1-butanol + isophorone} and {water + 1-butanol + mesityl oxide} ternary systems were investigated systematically at different temperatures under atmospheric pressure. The Othmer–Tobias and Bachman equations were applied to analyze the dependability of the experimental LLE data. Selectivities and distribution coefficients were used to evaluate the extractive efficiency of the extractants. The Non-Random Two Liquid (NRTL) and Universal Quasi-Chemical (UNIQUAC) models were applied to correlate the studied systems and were well represented with all root mean square deviations (RMSD) less than 0.2%. Meanwhile, binary interaction parameters among these compounds were acquired during the correlation process.
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Zhu, Z., Liu, Y., Wang, Y.: Liquid–liquid equilibrium for the ternary system of 1-butanol + 3-methyl-1-butanol + water at different temperatures. Fluid Phase Equilib. 335, 14–19 (2012)
Othmer, D.F., White, R.E., Trueger, E.: Liquid–liquid extraction data. Ind. Eng. Chem. 33, 1240–1248 (1941)
Kadir, S., Decloux, M., Giampaoli, P., Joulia, X.: Liquid–liquid equilibria of the ternary systems 3-methyl-1-butanol + ethanol + water and 2-methyl-1-propanol + ethanol + water at 293.15 K. J. Chem. Eng. Data 53, 910–912 (2008)
Fandary, M.S., Aljimaz, A.S., Alkandary, J.A., Fahim, M.A.: Liquid−liquid equilibria of water + ethanol + reformate at different temperatures. J. Chem. Eng. Data 47, 487–491 (2002)
Ghanadzadeh, H., Ghanadzadeh, A.: Liquid−liquid equilibria of water + 1-butanol + 2-ethyl-1-hexanol System. J. Chem. Eng. Data 49, 783–786 (2004)
De Oliveira, L., Aznar, M.: (Liquid + liquid) equilibrium of {water + phenol + (1-butanol, or 2-butanol, or tert-butanol) systems. J. Chem. Thermodyn. 42, 1379–1385 (2010)
Stoicescu, C., Iulian, O., Isopescu, R.: Liquid–liquid phase equilibria of 1-propanol + water + n-alcohol ternary systems at 298.15 K and atmospheric pressure. J. Chem. Eng. Data 56, 3214–3221 (2011)
Gilani, H.G., Golpour, M., Souraki, B.A.: Ternary equilibrium data of mixtures consisting of 2-butanol, water, and heavy alcohols at T = 298.2 K. J. Chem. Thermodyn. 49, 39–45 (2012)
Wang, Y., Ying, L., Cui, P.: Measurement and correlation of liquid–liquid equilibrium data for 2-methyl-1-propanol + 2-propanol + water at several temperatures. Fluid Phase Equilib. 340, 37–41 (2013)
Ghanadzadeh, H., Ghanadzadeh, A., Bahrpaima, K.: Measurement and prediction of tie-line data for mixtures of (water + 1-propanol + diisopropyl ether): LLE diagrams as a function of temperature. Fluid Phase Equilib. 277, 126–130 (2009)
Aznar, M., Araújo, R.N., Romanato, J.F., Santos, G.R., D’Ávila, S.G.: Salt effects on liquid−liquid equilibrium in water + ethanol + alcohol + salt systems. J. Chem. Eng. Data 45, 1055–1059 (2013)
Ghizellaoui, S., Coquelet, C., Richon, D., Meniai, A.H.: Liquid–liquid equilibrium of (water + 1-propanol + 1-pentanol) system at 298.15 and 323.15 K. Fluid Phase Equilib. 296, 4245 (2011)
Domańska, U., Wlazło, M., Paduszyski, K.: Extraction of butan-1-ol from aqueous solution using ionic liquids: an effect of cation revealed by experiments and thermodynamic models. Sep. Purif. Technol. 196, 71–81 (2018)
Domańska, U., Wlazło, M., Dąbrowski, Z., Wiśniewska, A.: Ammonium ionic liquids in separation of water/butan-1-ol using liquid–liquid equilibrium diagrams in ternary systems. Fluid Phase Equilib. 485, 23–31 (2019)
Nann, A., Held, C., Sadowski, G.: Liquid–liquid equilibria of 1-butanol/water/IL Systems. Ind. Eng. Chem. Res. 52, 18472–18481 (2013)
Othmer, D.F., Tobias, P.E.: Tie line correlation. Ind. Eng. Chem. 34, 693–700 (1942)
Bachman, I.: Tie lines in ternary liquid systems. Ind. Eng. Chem. 12, 38–39 (1940)
Renon, H., Prausnitz, J.M.: Local compositions in thermodynamic excess functions for liquid mixtures. AIChE J. 14, 135–144 (1968)
Abrams, D.S., Prausnitz, J.M.: Statistical thermodynamics of liquid mixtures: a new expression for the excess Gibbs energy of partly or completely miscible systems. AIChE J. 21, 116–128 (1975)
Dai, F.F., Xin, K., Song, Y.H., Shi, M.D., Yu, Y.M., Li, Q.S.: Liquid–liquid equilibria for the extraction of phenols from alkane using ethylene glycol. Fluid Phase Equilib. 409, 466–471 (2016)
Ginting, R.R., Mustain, A., Wibawa, G.: Determination of ternary liquid–liquid equilibria for dimethyl carbonate + 2-methyl-1-propanol or 2-methyl-2-propanol + water systems at T = 303.15 and 313.15 K. J. Chem. Eng. Data 62, 463–468 (2016)
Luo, L., Liu, D., Li, L., Chen, Y.: Experimental determination and correlation of liquid–liquid equilibria for the ternary system 2-methoxy-2-methylpropane + o-cresol + water at 298.15 K and 313.15 K. J. Chem. Eng. Data 60, 1396–1400 (2015)
IUPAC: Evaluation of measurement data-Guide to the expression of uncertainty in measurement. JCGM (2008)
Liu, D., Li, L., Lv, R., Chen, Y.: Liquid–liquid equilibria for the ternary system mesityl oxide + phenol + water at 298.15, 313.15, and 323.15 K. J. Chem. Eng. Data 61, 2493–2498 (2016)
Montoya, I.C.A., González, J.M., Villa, A.L.: Liquid–liquid equilibrium for the water + diethyl carbonate + ethanol system at different temperatures. J. Chem. Eng. Data 57, 1708–1712 (2012)
Chen, Y., Wang, H., Lv, R., Li, L.: Liquid–liquid equilibria for methyl isobutyl ketone + cresols + water at 333.15 K, 343.15 K and 353.15 K: experimental results and data correlation. Fluid Phase Equilib. 427, 291–296 (2016)
Cháfer, A., Lladosa, E., Montón, J.B., Torre, J.D.L.: Measurements and correlation of liquid–liquid equilibria of 4-methyl-2-pentanone + ethanol + water and 4-methyl-2-pentanone + n-butanol + water ternary systems between 283.2 and 323.2 K. Fluid Phase Equilib. 317, 89–95 (2012)
Li, Y.X., Xu, Q., Liu, S.L.: Liquid–liquid equilibrium for the ternary system of isopropyl acetate + 2-propanol + glycerol at different temperatures under atmospheric pressure. Fluid Phase Equilib. 412, 199–204 (2016)
Doulabi, F.S.M., Mohsennia, M., Rasa, H.: Ternary liquid–liquid equilibria for the (methanol + methylbenzene + decane) system at different temperatures. J. Chem. Eng. Data 56, 1366–1370 (2011)
Hong, G.B., Lee, M.J., Lin, H.: Liquid–liquid equilibria of ternary mixtures of water + 2-propanol with ethyl acetate, isopropyl acetate, or ethyl caproate. Fluid Phase Equilib. 202, 239–252 (2002)
Sun, C., Cao, W., Wu, J., Hu, X.: Liquid–liquid equilibrium of the ternary system water + propargyl alcohol + n-propyl acetate. Fluid Phase Equilib. 432, 85–89 (2017)
Chen, J.T., Lin, Y.M.: Liquid–liquid equilibria of water + 1-butanol + methyl methacrylate or butyl methacrylate or isobutyl methacrylate at 288.15 K and 318.15 K. Fluid Phase Equilib. 259, 189–194 (2007)
Colombo, A., Battilana, P., Ragaini, V., Bianchi, C.L., Carvoli, G.: Liquid–liquid equilibria of the ternary systems water + acetic acid + ethyl acetate and water + acetic acid + isophorone (3,5,5-trimethyl-2-cyclohexen-1-one). J. Chem. Eng. Data 44, 287–290 (1999)
Cháfer, A., Lladosa, E., Montón, J.B., Burguet, M.C.: Liquid–liquid equilibria for the system 1-methyl propyl ethanoate (1) + acetic acid (2) + water (3) at (283.15 and 323.15) K. J. Chem. Eng. Data 55, 523–525 (2010)
Ghanadzadeh, H., Ghanadzadeh, A., Bahrpaima, K.: Liquid phase equilibria of (water + phosphoric acid + 1-butanol or butyl acetate) ternary systems at T = 308.2 K. J. Chem. Thermodyn. 40, 1666–1670 (2008)
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Yu, Y., Zhang, L., Zhu, C. et al. Experimental Determination and Correlation of Liquid–Liquid Equilibria Data for the Ternary Systems of Water + 1-Butanol + Solvents (Isophorone and Mesityl Oxide) at Different Temperatures. J Solution Chem 49, 1–15 (2020). https://doi.org/10.1007/s10953-019-00939-2
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DOI: https://doi.org/10.1007/s10953-019-00939-2