Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Benzyl nitrile (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.1402 | 304.40 |
| 0.1511 | 306.60 |
| 0.1785 | 309.10 |
| 0.1933 | 309.50 |
| 0.2343 | 310.20 |
| 0.2506 | 310.50 |
| 0.2840 | 310.60 |
| 0.2934 | 310.60 |
| 0.3049 | 310.60 |
| 0.3155 | 310.60 |
| 0.3516 | 310.50 |
| 0.3778 | 310.40 |
| 0.4061 | 310.30 |
| 0.4276 | 310.20 |
| 0.4529 | 310.10 |
| 0.4788 | 310.00 |
| 0.5009 | 309.70 |
| 0.5477 | 308.70 |
| 0.5747 | 307.90 |
| 0.5944 | 307.10 |
| 0.6143 | 306.00 |
| 0.6454 | 303.90 |
| 0.6678 | 302.70 |
| 0.7315 | 294.90 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Benzyl nitrile (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.1402 | 304.40 |
| 0.1511 | 306.60 |
| 0.1785 | 309.10 |
| 0.1933 | 309.50 |
| 0.2343 | 310.20 |
| 0.2506 | 310.50 |
| 0.2840 | 310.60 |
| 0.2934 | 310.60 |
| 0.3049 | 310.60 |
| 0.3155 | 310.60 |
| 0.3516 | 310.50 |
| 0.3778 | 310.40 |
| 0.4061 | 310.30 |
| 0.4276 | 310.20 |
| 0.4529 | 310.10 |
| 0.4788 | 310.00 |
| 0.5009 | 309.70 |
| 0.5477 | 308.70 |
| 0.5747 | 307.90 |
| 0.5944 | 307.10 |
| 0.6143 | 306.00 |
| 0.6454 | 303.90 |
| 0.6678 | 302.70 |
| 0.7315 | 294.90 |