Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Mole fraction of Ethanol, 2-phenoxy- (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.2774 | 365.92 |
| 0.2914 | 366.52 |
| 0.2992 | 366.86 |
| 0.3196 | 367.62 |
| 0.3382 | 368.19 |
| 0.3561 | 368.46 |
| 0.3719 | 368.84 |
| 0.3958 | 368.95 |
| 0.4208 | 369.12 |
| 0.4448 | 369.18 |
| 0.4740 | 369.25 |
| 0.4998 | 369.25 |
| 0.5221 | 369.16 |
| 0.5446 | 369.17 |
| 0.5700 | 368.98 |
| 0.5914 | 368.80 |
| 0.6195 | 368.26 |
| 0.6406 | 367.64 |
| 0.6687 | 366.74 |
| 0.6894 | 365.69 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Mole fraction of Ethanol, 2-phenoxy- (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.2774 | 365.92 |
| 0.2914 | 366.52 |
| 0.2992 | 366.86 |
| 0.3196 | 367.62 |
| 0.3382 | 368.19 |
| 0.3561 | 368.46 |
| 0.3719 | 368.84 |
| 0.3958 | 368.95 |
| 0.4208 | 369.12 |
| 0.4448 | 369.18 |
| 0.4740 | 369.25 |
| 0.4998 | 369.25 |
| 0.5221 | 369.16 |
| 0.5446 | 369.17 |
| 0.5700 | 368.98 |
| 0.5914 | 368.80 |
| 0.6195 | 368.26 |
| 0.6406 | 367.64 |
| 0.6687 | 366.74 |
| 0.6894 | 365.69 |