Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Phenylethyl Alcohol (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.1544 | 295.70 |
| 0.1730 | 298.50 |
| 0.1918 | 300.30 |
| 0.2248 | 303.20 |
| 0.2407 | 304.00 |
| 0.2745 | 305.90 |
| 0.3044 | 306.90 |
| 0.3355 | 307.70 |
| 0.3626 | 308.10 |
| 0.3956 | 308.40 |
| 0.4240 | 308.50 |
| 0.4362 | 308.50 |
| 0.4595 | 308.50 |
| 0.4835 | 308.50 |
| 0.5223 | 308.50 |
| 0.5485 | 308.40 |
| 0.5742 | 308.30 |
| 0.6019 | 307.90 |
| 0.6281 | 307.70 |
| 0.6487 | 306.90 |
| 0.6684 | 306.30 |
| 0.6943 | 304.30 |
| 0.7165 | 301.60 |
| 0.7502 | 293.90 |
| 0.7730 | 285.00 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Phenylethyl Alcohol (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.1544 | 295.70 |
| 0.1730 | 298.50 |
| 0.1918 | 300.30 |
| 0.2248 | 303.20 |
| 0.2407 | 304.00 |
| 0.2745 | 305.90 |
| 0.3044 | 306.90 |
| 0.3355 | 307.70 |
| 0.3626 | 308.10 |
| 0.3956 | 308.40 |
| 0.4240 | 308.50 |
| 0.4362 | 308.50 |
| 0.4595 | 308.50 |
| 0.4835 | 308.50 |
| 0.5223 | 308.50 |
| 0.5485 | 308.40 |
| 0.5742 | 308.30 |
| 0.6019 | 307.90 |
| 0.6281 | 307.70 |
| 0.6487 | 306.90 |
| 0.6684 | 306.30 |
| 0.6943 | 304.30 |
| 0.7165 | 301.60 |
| 0.7502 | 293.90 |
| 0.7730 | 285.00 |