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 |
---|---|
0.1822 | 303.00 |
0.2007 | 305.10 |
0.2318 | 308.10 |
0.2471 | 309.60 |
0.2708 | 311.30 |
0.2942 | 312.80 |
0.3365 | 314.70 |
0.3617 | 315.30 |
0.3807 | 315.70 |
0.4197 | 316.60 |
0.4466 | 316.60 |
0.4692 | 316.80 |
0.4991 | 317.00 |
0.5145 | 317.00 |
0.5445 | 317.00 |
0.5751 | 316.90 |
0.5940 | 316.70 |
0.6172 | 316.70 |
0.6653 | 316.00 |
0.6660 | 316.20 |
0.6872 | 315.60 |
0.7177 | 314.40 |
0.7433 | 312.60 |
0.7659 | 310.20 |
0.7871 | 306.70 |
0.8020 | 303.80 |
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 |
---|---|
0.1822 | 303.00 |
0.2007 | 305.10 |
0.2318 | 308.10 |
0.2471 | 309.60 |
0.2708 | 311.30 |
0.2942 | 312.80 |
0.3365 | 314.70 |
0.3617 | 315.30 |
0.3807 | 315.70 |
0.4197 | 316.60 |
0.4466 | 316.60 |
0.4692 | 316.80 |
0.4991 | 317.00 |
0.5145 | 317.00 |
0.5445 | 317.00 |
0.5751 | 316.90 |
0.5940 | 316.70 |
0.6172 | 316.70 |
0.6653 | 316.00 |
0.6660 | 316.20 |
0.6872 | 315.60 |
0.7177 | 314.40 |
0.7433 | 312.60 |
0.7659 | 310.20 |
0.7871 | 306.70 |
0.8020 | 303.80 |