Operational condition: Pressure, kPa = 101.325 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mass fraction of Ethanol (1) - Liquid mixture 2 | Mass fraction of Water (3) - Liquid mixture 2 | Mass fraction of Water (3) - Liquid mixture 1 | Mass fraction of Ethanol (1) - Liquid mixture 1 |
303.15 | 0.0509 | 0.0438 | 0.8224 | 0.1448 |
303.15 | 0.0891 | 0.0710 | 0.7490 | 0.2023 |
303.15 | 0.1440 | 0.0981 | 0.6925 | 0.2361 |
303.15 | 0.1607 | 0.1339 | 0.6412 | 0.2603 |
303.15 | 0.1966 | 0.1569 | 0.5870 | 0.2805 |
303.15 | 0.2123 | 0.1713 | 0.5803 | 0.2796 |
313.15 | 0.0208 | 0.0319 | 0.9504 | 0.0306 |
313.15 | 0.0513 | 0.0493 | 0.8944 | 0.0600 |
313.15 | 0.0961 | 0.0762 | 0.8372 | 0.1276 |
313.15 | 0.1193 | 0.1041 | 0.7574 | 0.1843 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mass fraction of Ethanol (1) - Liquid mixture 2 | Mass fraction of Water (3) - Liquid mixture 2 | Mass fraction of Water (3) - Liquid mixture 1 | Mass fraction of Ethanol (1) - Liquid mixture 1 |
303.15 | 0.0509 | 0.0438 | 0.8224 | 0.1448 |
303.15 | 0.0891 | 0.0710 | 0.7490 | 0.2023 |
303.15 | 0.1440 | 0.0981 | 0.6925 | 0.2361 |
303.15 | 0.1607 | 0.1339 | 0.6412 | 0.2603 |
303.15 | 0.1966 | 0.1569 | 0.5870 | 0.2805 |
303.15 | 0.2123 | 0.1713 | 0.5803 | 0.2796 |
313.15 | 0.0208 | 0.0319 | 0.9504 | 0.0306 |
313.15 | 0.0513 | 0.0493 | 0.8944 | 0.0600 |
313.15 | 0.0961 | 0.0762 | 0.8372 | 0.1276 |
313.15 | 0.1193 | 0.1041 | 0.7574 | 0.1843 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |
---|---|---|
Mass fraction of Ethanol (1) - Liquid mixture 1 | Mass fraction of Water (3) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
0.0000 | 0.9789 | 313.15 |
0.0445 | 0.9341 | 303.15 |
0.0467 | 0.9305 | 313.15 |
0.0513 | 0.9259 | 303.15 |
0.0805 | 0.0494 | 303.15 |
0.1401 | 0.8333 | 303.15 |
0.1454 | 0.0895 | 313.15 |
0.1560 | 0.0958 | 303.15 |
0.1676 | 0.7916 | 313.15 |
0.1936 | 0.1347 | 313.15 |
0.2033 | 0.7580 | 303.15 |
0.2037 | 0.1454 | 303.15 |
0.2104 | 0.1586 | 313.15 |
0.2179 | 0.7391 | 303.15 |
0.2203 | 0.7399 | 303.15 |
0.2226 | 0.7067 | 313.15 |
0.2280 | 0.7180 | 303.15 |
0.2342 | 0.1963 | 303.15 |
0.2373 | 0.7118 | 303.15 |
0.2415 | 0.2292 | 313.15 |
0.2563 | 0.6388 | 313.15 |
0.2571 | 0.2448 | 303.15 |
0.2612 | 0.2943 | 313.15 |
0.2724 | 0.6430 | 303.15 |
0.2743 | 0.3635 | 313.15 |
0.2781 | 0.5704 | 313.15 |
0.2888 | 0.5787 | 303.15 |
0.2946 | 0.4353 | 303.15 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |
---|---|---|
Mass fraction of Ethanol (1) - Liquid mixture 1 | Mass fraction of Water (3) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
0.0000 | 0.9789 | 313.15 |
0.0445 | 0.9341 | 303.15 |
0.0467 | 0.9305 | 313.15 |
0.0513 | 0.9259 | 303.15 |
0.0805 | 0.0494 | 303.15 |
0.1401 | 0.8333 | 303.15 |
0.1454 | 0.0895 | 313.15 |
0.1560 | 0.0958 | 303.15 |
0.1676 | 0.7916 | 313.15 |
0.1936 | 0.1347 | 313.15 |
0.2033 | 0.7580 | 303.15 |
0.2037 | 0.1454 | 303.15 |
0.2104 | 0.1586 | 313.15 |
0.2179 | 0.7391 | 303.15 |
0.2203 | 0.7399 | 303.15 |
0.2226 | 0.7067 | 313.15 |
0.2280 | 0.7180 | 303.15 |
0.2342 | 0.1963 | 303.15 |
0.2373 | 0.7118 | 303.15 |
0.2415 | 0.2292 | 313.15 |
0.2563 | 0.6388 | 313.15 |
0.2571 | 0.2448 | 303.15 |
0.2612 | 0.2943 | 313.15 |
0.2724 | 0.6430 | 303.15 |
0.2743 | 0.3635 | 313.15 |
0.2781 | 0.5704 | 313.15 |
0.2888 | 0.5787 | 303.15 |
0.2946 | 0.4353 | 303.15 |