Abstract
In this work, liquid–liquid equilibria data for the methyl tert-butyl ketone (MTBK) + phenol + water ternary system at 298.15, 313.15 and 323.15 K, under atmospheric pressure, were measured. The experimental tie-line data’s reliability was verified by the Hand and Bachman equations. The distribution coefficient, together with the selectivity, was used to assess the extraction performance of MTBK. The experimental data were correlated with the nonrandom two-liquid and universal quasi-chemical activity coefficient models to yield binary interaction parameters for relevant process simulations.
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Financial support from Project of the Science & Technology New Star of Pearl River in Guangzhou (2011J2200056), the Fundamental Research Funds for the Central Universities, SCUT (2014ZZ0057), the Guangdong Science Foundation (2014A030310260) and National Science Foundation of China (20906028) are gratefully acknowledged.
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Liu, D., Luo, L., Li, L. et al. Liquid–Liquid Equilibria for the Methyl Tert-Butyl Ketone + Phenol + Water Ternary System at 298.15, 313.15 and 323.15 K. J Solution Chem 44, 1891–1899 (2015). https://doi.org/10.1007/s10953-015-0382-5
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DOI: https://doi.org/10.1007/s10953-015-0382-5