Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Benzylamine (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.3783 | 285.88 |
| 0.3895 | 286.23 |
| 0.3924 | 286.52 |
| 0.4311 | 288.14 |
| 0.4656 | 289.30 |
| 0.4835 | 289.89 |
| 0.5201 | 290.68 |
| 0.5373 | 290.94 |
| 0.5619 | 291.40 |
| 0.6025 | 291.98 |
| 0.6424 | 291.98 |
| 0.6614 | 291.97 |
| 0.6797 | 291.92 |
| 0.7009 | 291.93 |
| 0.7203 | 292.01 |
| 0.7372 | 291.97 |
| 0.7588 | 291.86 |
| 0.8037 | 291.56 |
| 0.8151 | 291.42 |
| 0.8401 | 290.63 |
| 0.8565 | 289.96 |
| 0.8743 | 288.53 |
| 0.8843 | 287.87 |
| 0.8987 | 286.12 |
| 0.9320 | 279.35 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Benzylamine (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.3783 | 285.88 |
| 0.3895 | 286.23 |
| 0.3924 | 286.52 |
| 0.4311 | 288.14 |
| 0.4656 | 289.30 |
| 0.4835 | 289.89 |
| 0.5201 | 290.68 |
| 0.5373 | 290.94 |
| 0.5619 | 291.40 |
| 0.6025 | 291.98 |
| 0.6424 | 291.98 |
| 0.6614 | 291.97 |
| 0.6797 | 291.92 |
| 0.7009 | 291.93 |
| 0.7203 | 292.01 |
| 0.7372 | 291.97 |
| 0.7588 | 291.86 |
| 0.8037 | 291.56 |
| 0.8151 | 291.42 |
| 0.8401 | 290.63 |
| 0.8565 | 289.96 |
| 0.8743 | 288.53 |
| 0.8843 | 287.87 |
| 0.8987 | 286.12 |
| 0.9320 | 279.35 |