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 |
---|---|
0.1908 | 309.40 |
0.2483 | 314.80 |
0.2676 | 316.40 |
0.2923 | 318.30 |
0.3352 | 321.10 |
0.3570 | 322.30 |
0.3960 | 323.70 |
0.4303 | 324.90 |
0.4524 | 325.10 |
0.4779 | 325.40 |
0.5052 | 325.70 |
0.5271 | 325.80 |
0.5573 | 325.90 |
0.5840 | 325.90 |
0.5996 | 326.00 |
0.6247 | 326.00 |
0.6405 | 325.80 |
0.6733 | 325.70 |
0.7062 | 325.40 |
0.7251 | 325.10 |
0.7486 | 324.20 |
0.7728 | 322.70 |
0.7970 | 320.70 |
0.8277 | 317.50 |
0.8463 | 314.20 |
0.8657 | 310.20 |
0.8968 | 303.10 |
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 |
---|---|
0.1908 | 309.40 |
0.2483 | 314.80 |
0.2676 | 316.40 |
0.2923 | 318.30 |
0.3352 | 321.10 |
0.3570 | 322.30 |
0.3960 | 323.70 |
0.4303 | 324.90 |
0.4524 | 325.10 |
0.4779 | 325.40 |
0.5052 | 325.70 |
0.5271 | 325.80 |
0.5573 | 325.90 |
0.5840 | 325.90 |
0.5996 | 326.00 |
0.6247 | 326.00 |
0.6405 | 325.80 |
0.6733 | 325.70 |
0.7062 | 325.40 |
0.7251 | 325.10 |
0.7486 | 324.20 |
0.7728 | 322.70 |
0.7970 | 320.70 |
0.8277 | 317.50 |
0.8463 | 314.20 |
0.8657 | 310.20 |
0.8968 | 303.10 |