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 |
---|---|
0.2459 | 290.20 |
0.2521 | 290.80 |
0.2903 | 295.30 |
0.3035 | 296.20 |
0.3438 | 299.10 |
0.3533 | 299.80 |
0.3862 | 301.80 |
0.4053 | 302.90 |
0.4257 | 303.60 |
0.4397 | 304.10 |
0.4676 | 305.70 |
0.5174 | 306.40 |
0.5433 | 306.80 |
0.5920 | 307.00 |
0.6483 | 307.00 |
0.6709 | 306.90 |
0.7028 | 306.70 |
0.7288 | 306.50 |
0.7457 | 306.40 |
0.7760 | 306.00 |
0.7991 | 305.30 |
0.8161 | 304.40 |
0.8521 | 302.00 |
0.8714 | 299.30 |
0.8981 | 294.50 |
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 |
---|---|
0.2459 | 290.20 |
0.2521 | 290.80 |
0.2903 | 295.30 |
0.3035 | 296.20 |
0.3438 | 299.10 |
0.3533 | 299.80 |
0.3862 | 301.80 |
0.4053 | 302.90 |
0.4257 | 303.60 |
0.4397 | 304.10 |
0.4676 | 305.70 |
0.5174 | 306.40 |
0.5433 | 306.80 |
0.5920 | 307.00 |
0.6483 | 307.00 |
0.6709 | 306.90 |
0.7028 | 306.70 |
0.7288 | 306.50 |
0.7457 | 306.40 |
0.7760 | 306.00 |
0.7991 | 305.30 |
0.8161 | 304.40 |
0.8521 | 302.00 |
0.8714 | 299.30 |
0.8981 | 294.50 |