Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Mole fraction of 2-Butanone, 4-phenyl- (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.2055 | 275.75 |
0.2331 | 278.10 |
0.2540 | 279.62 |
0.2709 | 280.56 |
0.2936 | 281.66 |
0.3005 | 281.83 |
0.3134 | 282.48 |
0.3495 | 283.48 |
0.3509 | 283.56 |
0.3639 | 283.81 |
0.3971 | 284.34 |
0.4294 | 284.54 |
0.4428 | 284.50 |
0.4695 | 284.49 |
0.4952 | 284.54 |
0.5145 | 284.49 |
0.5413 | 284.44 |
0.5681 | 284.35 |
0.5966 | 284.20 |
0.6195 | 284.02 |
0.6357 | 283.87 |
0.6652 | 283.26 |
0.6860 | 282.69 |
0.7026 | 282.11 |
0.7407 | 280.28 |
0.7773 | 277.57 |
0.7950 | 275.91 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Mole fraction of 2-Butanone, 4-phenyl- (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.2055 | 275.75 |
0.2331 | 278.10 |
0.2540 | 279.62 |
0.2709 | 280.56 |
0.2936 | 281.66 |
0.3005 | 281.83 |
0.3134 | 282.48 |
0.3495 | 283.48 |
0.3509 | 283.56 |
0.3639 | 283.81 |
0.3971 | 284.34 |
0.4294 | 284.54 |
0.4428 | 284.50 |
0.4695 | 284.49 |
0.4952 | 284.54 |
0.5145 | 284.49 |
0.5413 | 284.44 |
0.5681 | 284.35 |
0.5966 | 284.20 |
0.6195 | 284.02 |
0.6357 | 283.87 |
0.6652 | 283.26 |
0.6860 | 282.69 |
0.7026 | 282.11 |
0.7407 | 280.28 |
0.7773 | 277.57 |
0.7950 | 275.91 |