Datasets
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Mole fraction (2)
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Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of 1-Hexanol (2)
[ref]
| Fixed |
Measured |
| Mole fraction of 1-Hexanol (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of 1-Hexanol (2) - Gas |
| 0.0000 |
455.25 |
0.0000 |
| 0.0746 |
451.95 |
0.1534 |
| 0.1950 |
447.25 |
0.3537 |
| 0.2574 |
445.05 |
0.4402 |
| 0.3264 |
442.75 |
0.5247 |
| 0.3889 |
440.85 |
0.5928 |
| 0.4468 |
439.25 |
0.6496 |
| 0.5093 |
437.55 |
0.7050 |
| 0.5655 |
436.15 |
0.7499 |
| 0.6280 |
434.65 |
0.7951 |
| 0.6845 |
433.65 |
0.8320 |
| 0.7470 |
432.25 |
0.8690 |
| 0.8668 |
430.15 |
0.9309 |
| 0.9293 |
429.35 |
0.9610 |
| 1.0000 |
428.45 |
1.0000 |
Mole fraction of 1-Hexanol (2)
[ref]
| Fixed |
Measured |
| Mole fraction of 1-Hexanol (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of 1-Hexanol (2) - Gas |
| 0.0000 |
455.25 |
0.0000 |
| 0.0746 |
451.95 |
0.1534 |
| 0.1950 |
447.25 |
0.3537 |
| 0.2574 |
445.05 |
0.4402 |
| 0.3264 |
442.75 |
0.5247 |
| 0.3889 |
440.85 |
0.5928 |
| 0.4468 |
439.25 |
0.6496 |
| 0.5093 |
437.55 |
0.7050 |
| 0.5655 |
436.15 |
0.7499 |
| 0.6280 |
434.65 |
0.7951 |
| 0.6845 |
433.65 |
0.8320 |
| 0.7470 |
432.25 |
0.8690 |
| 0.8668 |
430.15 |
0.9309 |
| 0.9293 |
429.35 |
0.9610 |
| 1.0000 |
428.45 |
1.0000 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
95.6 (Liquid)
| Mole fraction of 1-Hexanol (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
455.25 |
| 0.0746 |
451.95 |
| 0.1950 |
447.25 |
| 0.2574 |
445.05 |
| 0.3264 |
442.75 |
| 0.3889 |
440.85 |
| 0.4468 |
439.25 |
| 0.5093 |
437.55 |
| 0.5655 |
436.15 |
| 0.6280 |
434.65 |
| 0.6845 |
433.65 |
| 0.7470 |
432.25 |
| 0.8668 |
430.15 |
| 0.9293 |
429.35 |
| 1.0000 |
428.45 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
95.6 (Liquid)
| Mole fraction of 1-Hexanol (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
455.25 |
| 0.0746 |
451.95 |
| 0.1950 |
447.25 |
| 0.2574 |
445.05 |
| 0.3264 |
442.75 |
| 0.3889 |
440.85 |
| 0.4468 |
439.25 |
| 0.5093 |
437.55 |
| 0.5655 |
436.15 |
| 0.6280 |
434.65 |
| 0.6845 |
433.65 |
| 0.7470 |
432.25 |
| 0.8668 |
430.15 |
| 0.9293 |
429.35 |
| 1.0000 |
428.45 |
Sources