Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Mole fraction of Acetonitrile (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.6010 | 400.89 |
| 0.6496 | 402.99 |
| 0.6992 | 404.59 |
| 0.7224 | 404.95 |
| 0.7527 | 405.21 |
| 0.7740 | 405.37 |
| 0.7898 | 405.39 |
| 0.7993 | 405.39 |
| 0.8137 | 405.41 |
| 0.8262 | 405.37 |
| 0.8375 | 405.37 |
| 0.8489 | 405.31 |
| 0.8618 | 405.18 |
| 0.8745 | 405.03 |
| 0.8854 | 404.76 |
| 0.8984 | 404.23 |
| 0.9085 | 402.76 |
| 0.9222 | 401.08 |
| 0.9495 | 392.46 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Mole fraction of Acetonitrile (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.6010 | 400.89 |
| 0.6496 | 402.99 |
| 0.6992 | 404.59 |
| 0.7224 | 404.95 |
| 0.7527 | 405.21 |
| 0.7740 | 405.37 |
| 0.7898 | 405.39 |
| 0.7993 | 405.39 |
| 0.8137 | 405.41 |
| 0.8262 | 405.37 |
| 0.8375 | 405.37 |
| 0.8489 | 405.31 |
| 0.8618 | 405.18 |
| 0.8745 | 405.03 |
| 0.8854 | 404.76 |
| 0.8984 | 404.23 |
| 0.9085 | 402.76 |
| 0.9222 | 401.08 |
| 0.9495 | 392.46 |