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 |
---|---|
0.2232 | 279.30 |
0.2653 | 285.20 |
0.2833 | 286.40 |
0.2929 | 287.10 |
0.3250 | 288.90 |
0.3431 | 289.60 |
0.3688 | 290.60 |
0.4059 | 291.40 |
0.4605 | 292.30 |
0.4775 | 292.40 |
0.4844 | 292.50 |
0.4853 | 292.50 |
0.5528 | 292.40 |
0.5673 | 292.40 |
0.5993 | 292.30 |
0.6316 | 292.20 |
0.6521 | 292.20 |
0.6695 | 291.90 |
0.6939 | 291.60 |
0.7211 | 291.00 |
0.7534 | 289.90 |
0.7684 | 289.10 |
0.7997 | 286.80 |
0.8176 | 285.50 |
0.8341 | 283.20 |
0.8683 | 278.30 |
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 |
---|---|
0.2232 | 279.30 |
0.2653 | 285.20 |
0.2833 | 286.40 |
0.2929 | 287.10 |
0.3250 | 288.90 |
0.3431 | 289.60 |
0.3688 | 290.60 |
0.4059 | 291.40 |
0.4605 | 292.30 |
0.4775 | 292.40 |
0.4844 | 292.50 |
0.4853 | 292.50 |
0.5528 | 292.40 |
0.5673 | 292.40 |
0.5993 | 292.30 |
0.6316 | 292.20 |
0.6521 | 292.20 |
0.6695 | 291.90 |
0.6939 | 291.60 |
0.7211 | 291.00 |
0.7534 | 289.90 |
0.7684 | 289.10 |
0.7997 | 286.80 |
0.8176 | 285.50 |
0.8341 | 283.20 |
0.8683 | 278.30 |