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 |
---|---|
0.1608 | 310.30 |
0.1800 | 312.90 |
0.2048 | 315.60 |
0.2275 | 317.30 |
0.2609 | 319.00 |
0.2771 | 319.80 |
0.3072 | 320.80 |
0.3137 | 321.00 |
0.3361 | 321.40 |
0.3512 | 321.90 |
0.3771 | 322.10 |
0.4044 | 322.30 |
0.4214 | 322.20 |
0.4532 | 322.40 |
0.4805 | 322.50 |
0.5021 | 322.40 |
0.5298 | 322.20 |
0.5457 | 322.30 |
0.5793 | 322.10 |
0.6009 | 321.60 |
0.6317 | 320.70 |
0.6464 | 320.10 |
0.6742 | 317.70 |
0.7534 | 306.70 |
0.7742 | 302.00 |
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 |
---|---|
0.1608 | 310.30 |
0.1800 | 312.90 |
0.2048 | 315.60 |
0.2275 | 317.30 |
0.2609 | 319.00 |
0.2771 | 319.80 |
0.3072 | 320.80 |
0.3137 | 321.00 |
0.3361 | 321.40 |
0.3512 | 321.90 |
0.3771 | 322.10 |
0.4044 | 322.30 |
0.4214 | 322.20 |
0.4532 | 322.40 |
0.4805 | 322.50 |
0.5021 | 322.40 |
0.5298 | 322.20 |
0.5457 | 322.30 |
0.5793 | 322.10 |
0.6009 | 321.60 |
0.6317 | 320.70 |
0.6464 | 320.10 |
0.6742 | 317.70 |
0.7534 | 306.70 |
0.7742 | 302.00 |