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• W2065004246 abstract "A new static apparatus was designed and constructed for the measurement of high pressure liquidliquid equilibria up to 450 K and 20 MPa. Binary phase equilibria for the water + 1,1-difluoroethane system at 323.2 K and ternary liquidliquid equilibria for the water + ethanol + 1,1-difluoroethane system at 323.2 K were measured. The liquefied gas 1,1-difluoroethane was found to be an excellent solvent for the extraction of ethanol from low ethanol concentration aqueous solutions. 1,1-Difluoroethane could achieve more than double the ethanol distribution coefficients obtained with carbon dioxide at much lower pressures. The liquidliquid equilibrium data were correlated by the UNIQUAC and NRTL equations. The UNIQUAC and NRTL equations gave comparable correlation of the experimental data, however, the UNIQUAC equation yielded slightly better results." @default.
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• W2065004246 date "1987-01-01" @default.
• W2065004246 modified "2023-10-03" @default.
• W2065004246 title "High pressure liquidliquid equilibria for the system of water, ethanol and 1,1-difluoroethane at 323.2 K" @default.
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• W2065004246 doi "https://doi.org/10.1016/0378-3812(87)90007-0" @default.
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