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 |
|---|---|
| 0.1573 | 338.70 |
| 0.1941 | 344.30 |
| 0.2051 | 346.00 |
| 0.2103 | 346.70 |
| 0.2372 | 348.40 |
| 0.2547 | 349.40 |
| 0.2709 | 349.70 |
| 0.2942 | 350.10 |
| 0.3206 | 350.20 |
| 0.3454 | 350.30 |
| 0.3791 | 350.20 |
| 0.3979 | 350.20 |
| 0.4251 | 350.10 |
| 0.4704 | 350.20 |
| 0.5025 | 349.90 |
| 0.5502 | 349.20 |
| 0.5996 | 347.70 |
| 0.6478 | 345.30 |
| 0.6702 | 343.70 |
| 0.7169 | 338.20 |
| 0.7365 | 336.20 |
| 0.7517 | 333.40 |
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 |
|---|---|
| 0.1573 | 338.70 |
| 0.1941 | 344.30 |
| 0.2051 | 346.00 |
| 0.2103 | 346.70 |
| 0.2372 | 348.40 |
| 0.2547 | 349.40 |
| 0.2709 | 349.70 |
| 0.2942 | 350.10 |
| 0.3206 | 350.20 |
| 0.3454 | 350.30 |
| 0.3791 | 350.20 |
| 0.3979 | 350.20 |
| 0.4251 | 350.10 |
| 0.4704 | 350.20 |
| 0.5025 | 349.90 |
| 0.5502 | 349.20 |
| 0.5996 | 347.70 |
| 0.6478 | 345.30 |
| 0.6702 | 343.70 |
| 0.7169 | 338.20 |
| 0.7365 | 336.20 |
| 0.7517 | 333.40 |