Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Mole fraction of Aniline (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.1240 | 290.35 |
0.1440 | 292.74 |
0.1650 | 294.70 |
0.1860 | 296.35 |
0.2060 | 297.91 |
0.2270 | 299.43 |
0.2470 | 300.42 |
0.2670 | 301.44 |
0.2870 | 302.32 |
0.3070 | 302.97 |
0.3260 | 303.51 |
0.3470 | 303.92 |
0.3660 | 304.13 |
0.3870 | 304.30 |
0.4080 | 304.42 |
0.4270 | 304.45 |
0.4470 | 304.44 |
0.4660 | 304.43 |
0.4840 | 304.44 |
0.5040 | 304.44 |
0.5240 | 304.45 |
0.5440 | 304.37 |
0.5640 | 304.35 |
0.5850 | 304.26 |
0.6060 | 304.04 |
0.6260 | 303.76 |
0.6440 | 303.27 |
0.6670 | 302.36 |
0.6860 | 301.38 |
0.7050 | 300.01 |
0.7210 | 298.41 |
0.7420 | 296.42 |
0.7610 | 293.80 |
0.7830 | 290.07 |
0.7970 | 286.46 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Mole fraction of Aniline (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.1240 | 290.35 |
0.1440 | 292.74 |
0.1650 | 294.70 |
0.1860 | 296.35 |
0.2060 | 297.91 |
0.2270 | 299.43 |
0.2470 | 300.42 |
0.2670 | 301.44 |
0.2870 | 302.32 |
0.3070 | 302.97 |
0.3260 | 303.51 |
0.3470 | 303.92 |
0.3660 | 304.13 |
0.3870 | 304.30 |
0.4080 | 304.42 |
0.4270 | 304.45 |
0.4470 | 304.44 |
0.4660 | 304.43 |
0.4840 | 304.44 |
0.5040 | 304.44 |
0.5240 | 304.45 |
0.5440 | 304.37 |
0.5640 | 304.35 |
0.5850 | 304.26 |
0.6060 | 304.04 |
0.6260 | 303.76 |
0.6440 | 303.27 |
0.6670 | 302.36 |
0.6860 | 301.38 |
0.7050 | 300.01 |
0.7210 | 298.41 |
0.7420 | 296.42 |
0.7610 | 293.80 |
0.7830 | 290.07 |
0.7970 | 286.46 |