Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (2) - Liquid mixture 1 | Mole fraction of Cyclohexanol (1) - Liquid mixture 1 |
298.15 | 0.0000 | 0.5610 |
298.15 | 0.0550 | 0.5720 |
298.15 | 0.1000 | 0.5680 |
298.15 | 0.1680 | 0.5500 |
298.15 | 0.2170 | 0.5320 |
298.15 | 0.2780 | 0.5010 |
298.15 | 0.3310 | 0.4760 |
298.15 | 0.5400 | 0.3600 |
298.15 | 0.7170 | 0.2250 |
298.15 | 0.8930 | 0.0950 |
323.15 | 0.0000 | 0.5340 |
323.15 | 0.0560 | 0.5550 |
323.15 | 0.1110 | 0.5520 |
323.15 | 0.1620 | 0.5360 |
323.15 | 0.2320 | 0.5110 |
323.15 | 0.2920 | 0.4860 |
323.15 | 0.3430 | 0.4620 |
323.15 | 0.4100 | 0.4310 |
323.15 | 0.6730 | 0.2560 |
323.15 | 0.8330 | 0.1320 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (2) - Liquid mixture 1 | Mole fraction of Cyclohexanol (1) - Liquid mixture 1 |
298.15 | 0.0000 | 0.5610 |
298.15 | 0.0550 | 0.5720 |
298.15 | 0.1000 | 0.5680 |
298.15 | 0.1680 | 0.5500 |
298.15 | 0.2170 | 0.5320 |
298.15 | 0.2780 | 0.5010 |
298.15 | 0.3310 | 0.4760 |
298.15 | 0.5400 | 0.3600 |
298.15 | 0.7170 | 0.2250 |
298.15 | 0.8930 | 0.0950 |
323.15 | 0.0000 | 0.5340 |
323.15 | 0.0560 | 0.5550 |
323.15 | 0.1110 | 0.5520 |
323.15 | 0.1620 | 0.5360 |
323.15 | 0.2320 | 0.5110 |
323.15 | 0.2920 | 0.4860 |
323.15 | 0.3430 | 0.4620 |
323.15 | 0.4100 | 0.4310 |
323.15 | 0.6730 | 0.2560 |
323.15 | 0.8330 | 0.1320 |