Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Mole fraction of Ethanol, 2-phenoxy- (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.1990 | 327.34 |
| 0.2106 | 327.79 |
| 0.2246 | 328.36 |
| 0.2499 | 329.09 |
| 0.2748 | 329.63 |
| 0.2971 | 329.97 |
| 0.3252 | 330.20 |
| 0.3493 | 330.28 |
| 0.3746 | 330.35 |
| 0.4027 | 330.36 |
| 0.4255 | 330.37 |
| 0.4491 | 330.31 |
| 0.4756 | 330.32 |
| 0.4994 | 330.19 |
| 0.5238 | 330.05 |
| 0.5497 | 329.70 |
| 0.5710 | 329.36 |
| 0.6005 | 328.57 |
| 0.6233 | 327.79 |
| 0.6350 | 327.19 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Mole fraction of Ethanol, 2-phenoxy- (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.1990 | 327.34 |
| 0.2106 | 327.79 |
| 0.2246 | 328.36 |
| 0.2499 | 329.09 |
| 0.2748 | 329.63 |
| 0.2971 | 329.97 |
| 0.3252 | 330.20 |
| 0.3493 | 330.28 |
| 0.3746 | 330.35 |
| 0.4027 | 330.36 |
| 0.4255 | 330.37 |
| 0.4491 | 330.31 |
| 0.4756 | 330.32 |
| 0.4994 | 330.19 |
| 0.5238 | 330.05 |
| 0.5497 | 329.70 |
| 0.5710 | 329.36 |
| 0.6005 | 328.57 |
| 0.6233 | 327.79 |
| 0.6350 | 327.19 |