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 |
|---|---|
| 0.2064 | 355.60 |
| 0.2317 | 358.00 |
| 0.2613 | 359.30 |
| 0.2791 | 359.70 |
| 0.3077 | 359.90 |
| 0.3321 | 360.30 |
| 0.3503 | 360.30 |
| 0.3660 | 360.40 |
| 0.4156 | 360.20 |
| 0.4448 | 360.10 |
| 0.4771 | 359.90 |
| 0.5123 | 359.50 |
| 0.5536 | 359.30 |
| 0.5695 | 358.90 |
| 0.6123 | 358.20 |
| 0.6221 | 357.90 |
| 0.6428 | 356.80 |
| 0.6711 | 355.50 |
| 0.6995 | 353.40 |
| 0.7126 | 352.10 |
| 0.7443 | 348.00 |
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 |
|---|---|
| 0.2064 | 355.60 |
| 0.2317 | 358.00 |
| 0.2613 | 359.30 |
| 0.2791 | 359.70 |
| 0.3077 | 359.90 |
| 0.3321 | 360.30 |
| 0.3503 | 360.30 |
| 0.3660 | 360.40 |
| 0.4156 | 360.20 |
| 0.4448 | 360.10 |
| 0.4771 | 359.90 |
| 0.5123 | 359.50 |
| 0.5536 | 359.30 |
| 0.5695 | 358.90 |
| 0.6123 | 358.20 |
| 0.6221 | 357.90 |
| 0.6428 | 356.80 |
| 0.6711 | 355.50 |
| 0.6995 | 353.40 |
| 0.7126 | 352.10 |
| 0.7443 | 348.00 |