Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Acetophenone (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.4141 | 287.75 |
| 0.4430 | 289.39 |
| 0.4642 | 290.63 |
| 0.4749 | 291.10 |
| 0.4853 | 291.51 |
| 0.4856 | 291.54 |
| 0.4998 | 292.04 |
| 0.5192 | 292.90 |
| 0.5429 | 293.63 |
| 0.5581 | 294.13 |
| 0.5752 | 294.47 |
| 0.6040 | 294.90 |
| 0.6223 | 295.15 |
| 0.6347 | 295.23 |
| 0.6562 | 295.39 |
| 0.6674 | 295.38 |
| 0.6990 | 295.51 |
| 0.7166 | 295.49 |
| 0.7223 | 295.49 |
| 0.7401 | 295.39 |
| 0.7667 | 295.29 |
| 0.7916 | 294.93 |
| 0.8017 | 294.71 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Acetophenone (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.4141 | 287.75 |
| 0.4430 | 289.39 |
| 0.4642 | 290.63 |
| 0.4749 | 291.10 |
| 0.4853 | 291.51 |
| 0.4856 | 291.54 |
| 0.4998 | 292.04 |
| 0.5192 | 292.90 |
| 0.5429 | 293.63 |
| 0.5581 | 294.13 |
| 0.5752 | 294.47 |
| 0.6040 | 294.90 |
| 0.6223 | 295.15 |
| 0.6347 | 295.23 |
| 0.6562 | 295.39 |
| 0.6674 | 295.38 |
| 0.6990 | 295.51 |
| 0.7166 | 295.49 |
| 0.7223 | 295.49 |
| 0.7401 | 295.39 |
| 0.7667 | 295.29 |
| 0.7916 | 294.93 |
| 0.8017 | 294.71 |