Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Benzenepropanenitrile (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.1993 | 347.60 |
| 0.2167 | 349.20 |
| 0.2279 | 350.50 |
| 0.2598 | 352.60 |
| 0.2829 | 353.90 |
| 0.2834 | 353.90 |
| 0.3128 | 354.90 |
| 0.3415 | 355.60 |
| 0.3772 | 356.10 |
| 0.4105 | 356.40 |
| 0.4283 | 356.30 |
| 0.4524 | 356.40 |
| 0.4737 | 356.50 |
| 0.5177 | 356.40 |
| 0.5478 | 356.30 |
| 0.5891 | 355.60 |
| 0.6038 | 355.10 |
| 0.6762 | 351.90 |
| 0.7010 | 349.50 |
| 0.7278 | 346.00 |
| 0.7336 | 344.50 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Benzenepropanenitrile (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.1993 | 347.60 |
| 0.2167 | 349.20 |
| 0.2279 | 350.50 |
| 0.2598 | 352.60 |
| 0.2829 | 353.90 |
| 0.2834 | 353.90 |
| 0.3128 | 354.90 |
| 0.3415 | 355.60 |
| 0.3772 | 356.10 |
| 0.4105 | 356.40 |
| 0.4283 | 356.30 |
| 0.4524 | 356.40 |
| 0.4737 | 356.50 |
| 0.5177 | 356.40 |
| 0.5478 | 356.30 |
| 0.5891 | 355.60 |
| 0.6038 | 355.10 |
| 0.6762 | 351.90 |
| 0.7010 | 349.50 |
| 0.7278 | 346.00 |
| 0.7336 | 344.50 |