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 |
|---|---|
| 0.1987 | 348.50 |
| 0.2424 | 350.90 |
| 0.2866 | 352.50 |
| 0.3005 | 352.60 |
| 0.3203 | 352.70 |
| 0.3568 | 352.80 |
| 0.3723 | 352.80 |
| 0.4115 | 352.70 |
| 0.4587 | 352.50 |
| 0.4883 | 352.40 |
| 0.5039 | 352.20 |
| 0.5293 | 352.30 |
| 0.5447 | 352.10 |
| 0.5923 | 351.10 |
| 0.6240 | 350.60 |
| 0.6711 | 348.70 |
| 0.7021 | 346.10 |
| 0.7430 | 340.00 |
| 0.7646 | 336.20 |
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 |
|---|---|
| 0.1987 | 348.50 |
| 0.2424 | 350.90 |
| 0.2866 | 352.50 |
| 0.3005 | 352.60 |
| 0.3203 | 352.70 |
| 0.3568 | 352.80 |
| 0.3723 | 352.80 |
| 0.4115 | 352.70 |
| 0.4587 | 352.50 |
| 0.4883 | 352.40 |
| 0.5039 | 352.20 |
| 0.5293 | 352.30 |
| 0.5447 | 352.10 |
| 0.5923 | 351.10 |
| 0.6240 | 350.60 |
| 0.6711 | 348.70 |
| 0.7021 | 346.10 |
| 0.7430 | 340.00 |
| 0.7646 | 336.20 |