Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Mole fraction of Acetonitrile (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.3743 | 372.70 |
| 0.3965 | 374.53 |
| 0.4519 | 378.84 |
| 0.4699 | 380.33 |
| 0.4873 | 381.09 |
| 0.5179 | 382.61 |
| 0.5549 | 384.09 |
| 0.5895 | 385.24 |
| 0.6111 | 385.93 |
| 0.6503 | 386.71 |
| 0.6779 | 387.04 |
| 0.7005 | 387.26 |
| 0.7101 | 387.32 |
| 0.7525 | 387.46 |
| 0.7557 | 387.57 |
| 0.7787 | 387.47 |
| 0.7998 | 387.24 |
| 0.8160 | 387.06 |
| 0.8160 | 387.06 |
| 0.8385 | 386.66 |
| 0.8507 | 386.47 |
| 0.8694 | 385.17 |
| 0.8802 | 384.15 |
| 0.9016 | 381.38 |
| 0.9186 | 377.69 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Mole fraction of Acetonitrile (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.3743 | 372.70 |
| 0.3965 | 374.53 |
| 0.4519 | 378.84 |
| 0.4699 | 380.33 |
| 0.4873 | 381.09 |
| 0.5179 | 382.61 |
| 0.5549 | 384.09 |
| 0.5895 | 385.24 |
| 0.6111 | 385.93 |
| 0.6503 | 386.71 |
| 0.6779 | 387.04 |
| 0.7005 | 387.26 |
| 0.7101 | 387.32 |
| 0.7525 | 387.46 |
| 0.7557 | 387.57 |
| 0.7787 | 387.47 |
| 0.7998 | 387.24 |
| 0.8160 | 387.06 |
| 0.8160 | 387.06 |
| 0.8385 | 386.66 |
| 0.8507 | 386.47 |
| 0.8694 | 385.17 |
| 0.8802 | 384.15 |
| 0.9016 | 381.38 |
| 0.9186 | 377.69 |