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• W2767842575 abstract "To separate isopropanol from its aqueous solution, isobutyl acetate, butyl acetate and butyl propionate were adopted as the extractive solvents, and the liquid-liquid equilibrium (LLE) data for the ternary systems (isobutyl acetate / butyl acetate / butyl propionate) + isopropanol + water were determined at 298.15 K and 308.15 K under atmospheric pressure. The experimental LLE data were correlated by the NRTL and UNIQUAC models, and the values of the root mean square deviations (RMSD) were less than 1%. And the binary interaction parameters of the NRTL and UNIQUAC models were optimized. Meantime, the distribution coefficient and selectivity were calculated to evaluate the extraction capacity of the solvents. As a result, butyl propionate is a desirable extractive solvent compared with the other two solvents." @default.
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• W2767842575 date "2018-02-01" @default.
• W2767842575 modified "2023-10-10" @default.
• W2767842575 title "Liquid-liquid equilibrium determination and thermodynamics modeling for extraction of isopropanol from its aqueous solution" @default.
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• W2767842575 doi "https://doi.org/10.1016/j.fluid.2017.11.010" @default.
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