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• W3139181105 endingPage "1838" @default.
• W3139181105 startingPage "1831" @default.
• W3139181105 abstract "For separating 2-butanone and water from the azeotropic system, the liquid–liquid equilibria (LLE) data for the ternary mixture of solvents (p-xylene, mesityl oxide) + 2-butanone + water at 298.2, 303.2, and 313.2 K were obtained under 101.3 kPa. The distribution coefficient (D) and selectivity coefficient (S) were used to evaluate the effect of extracting 2-butanone from water, it is found that p-xylene is better than mesityl oxide. The Bachman and Othmer–Tobias equations were used to verify the reliability of the LLE data with the linear coefficient being greater than 0.98%. The NRTL and UNIQUAC models successfully correlated the experimental data with the root mean square deviation values less than 0.87 and 0.50%, respectively. It shows that the UNIQUAC is more suitable for this system than the NRTL model." @default.
• W3139181105 created "2021-03-29" @default.
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• W3139181105 date "2021-03-24" @default.
• W3139181105 modified "2023-09-27" @default.
• W3139181105 title "Ternary (Liquid + Liquid) Equilibrium Experiment and Thermodynamic Modeling for Solvents (<i>p</i>-Xylene, Mesityl Oxide) + 2-Butanone + Water at 298.2, 303.2, and 313.2 K under 101.3 kPa" @default.
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• W3139181105 doi "https://doi.org/10.1021/acs.jced.1c00158" @default.
• W3139181105 hasPublicationYear "2021" @default.
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