Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Benzylamine (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.3037 | 276.69 |
| 0.3147 | 277.04 |
| 0.3185 | 277.13 |
| 0.3476 | 278.03 |
| 0.3595 | 278.38 |
| 0.3728 | 278.69 |
| 0.4042 | 279.19 |
| 0.4341 | 279.69 |
| 0.4436 | 279.82 |
| 0.4576 | 279.92 |
| 0.4595 | 279.88 |
| 0.4792 | 280.06 |
| 0.4987 | 280.07 |
| 0.5305 | 280.11 |
| 0.5661 | 280.06 |
| 0.5755 | 280.02 |
| 0.5913 | 280.07 |
| 0.6011 | 280.03 |
| 0.6263 | 280.05 |
| 0.6354 | 280.03 |
| 0.6497 | 279.99 |
| 0.6813 | 279.79 |
| 0.7061 | 279.53 |
| 0.7330 | 279.20 |
| 0.7436 | 279.02 |
| 0.7614 | 278.63 |
| 0.7691 | 278.41 |
| 0.7742 | 278.31 |
| 0.8024 | 277.34 |
| 0.8152 | 276.86 |
| 0.8374 | 275.83 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Benzylamine (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.3037 | 276.69 |
| 0.3147 | 277.04 |
| 0.3185 | 277.13 |
| 0.3476 | 278.03 |
| 0.3595 | 278.38 |
| 0.3728 | 278.69 |
| 0.4042 | 279.19 |
| 0.4341 | 279.69 |
| 0.4436 | 279.82 |
| 0.4576 | 279.92 |
| 0.4595 | 279.88 |
| 0.4792 | 280.06 |
| 0.4987 | 280.07 |
| 0.5305 | 280.11 |
| 0.5661 | 280.06 |
| 0.5755 | 280.02 |
| 0.5913 | 280.07 |
| 0.6011 | 280.03 |
| 0.6263 | 280.05 |
| 0.6354 | 280.03 |
| 0.6497 | 279.99 |
| 0.6813 | 279.79 |
| 0.7061 | 279.53 |
| 0.7330 | 279.20 |
| 0.7436 | 279.02 |
| 0.7614 | 278.63 |
| 0.7691 | 278.41 |
| 0.7742 | 278.31 |
| 0.8024 | 277.34 |
| 0.8152 | 276.86 |
| 0.8374 | 275.83 |