Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Benzyl nitrile (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.2247 | 349.40 |
| 0.2648 | 354.00 |
| 0.2720 | 354.90 |
| 0.3023 | 355.90 |
| 0.3033 | 356.00 |
| 0.3369 | 356.00 |
| 0.3558 | 356.20 |
| 0.3797 | 356.20 |
| 0.4011 | 356.20 |
| 0.4321 | 356.20 |
| 0.4471 | 356.10 |
| 0.4780 | 356.00 |
| 0.5058 | 355.80 |
| 0.5298 | 355.60 |
| 0.5575 | 355.40 |
| 0.5745 | 355.30 |
| 0.5944 | 355.10 |
| 0.6250 | 354.70 |
| 0.7246 | 348.10 |
| 0.7531 | 344.80 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Benzyl nitrile (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.2247 | 349.40 |
| 0.2648 | 354.00 |
| 0.2720 | 354.90 |
| 0.3023 | 355.90 |
| 0.3033 | 356.00 |
| 0.3369 | 356.00 |
| 0.3558 | 356.20 |
| 0.3797 | 356.20 |
| 0.4011 | 356.20 |
| 0.4321 | 356.20 |
| 0.4471 | 356.10 |
| 0.4780 | 356.00 |
| 0.5058 | 355.80 |
| 0.5298 | 355.60 |
| 0.5575 | 355.40 |
| 0.5745 | 355.30 |
| 0.5944 | 355.10 |
| 0.6250 | 354.70 |
| 0.7246 | 348.10 |
| 0.7531 | 344.80 |