Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Mole fraction of Acetonitrile (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.6058 | 404.00 |
| 0.6297 | 405.57 |
| 0.6507 | 406.74 |
| 0.6806 | 408.79 |
| 0.7001 | 409.71 |
| 0.7291 | 410.22 |
| 0.7432 | 410.46 |
| 0.7597 | 410.57 |
| 0.7716 | 410.68 |
| 0.8004 | 410.98 |
| 0.8206 | 411.12 |
| 0.8299 | 410.98 |
| 0.8486 | 410.89 |
| 0.8704 | 410.48 |
| 0.8844 | 410.29 |
| 0.9018 | 409.69 |
| 0.9198 | 407.59 |
| 0.9334 | 405.27 |
| 0.9481 | 400.72 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Mole fraction of Acetonitrile (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.6058 | 404.00 |
| 0.6297 | 405.57 |
| 0.6507 | 406.74 |
| 0.6806 | 408.79 |
| 0.7001 | 409.71 |
| 0.7291 | 410.22 |
| 0.7432 | 410.46 |
| 0.7597 | 410.57 |
| 0.7716 | 410.68 |
| 0.8004 | 410.98 |
| 0.8206 | 411.12 |
| 0.8299 | 410.98 |
| 0.8486 | 410.89 |
| 0.8704 | 410.48 |
| 0.8844 | 410.29 |
| 0.9018 | 409.69 |
| 0.9198 | 407.59 |
| 0.9334 | 405.27 |
| 0.9481 | 400.72 |