Datasets
-
Mole fraction (4)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of 1-Hexanol (1)
[ref]
Operational condition: Temperature, K =
413.15 (Liquid)
Mole fraction of 1-Hexanol (1) - Liquid |
Mole fraction of 1-Hexanol (1) - Gas |
0.0254 |
0.0406 |
0.0368 |
0.0580 |
0.0655 |
0.1013 |
0.0913 |
0.1397 |
0.1175 |
0.1754 |
0.2188 |
0.3022 |
0.3225 |
0.4160 |
0.4139 |
0.5054 |
0.6003 |
0.6646 |
0.9125 |
0.9211 |
0.9343 |
0.9401 |
0.9566 |
0.9601 |
0.9797 |
0.9812 |
0.9894 |
0.9901 |
Mole fraction of 1-Hexanol (1)
[ref]
Fixed |
Measured |
Mole fraction of 1-Hexanol (1) - Liquid |
Pressure, kPa - Gas |
Mole fraction of 1-Hexanol (1) - Gas |
0.0160 |
90.00 |
0.0246 |
0.0210 |
60.00 |
0.0327 |
0.0263 |
30.00 |
0.0396 |
0.0315 |
90.00 |
0.0480 |
0.0365 |
60.00 |
0.0560 |
0.0490 |
30.00 |
0.0732 |
0.0554 |
90.00 |
0.0843 |
0.0664 |
60.00 |
0.1005 |
0.0853 |
90.00 |
0.1287 |
0.0902 |
30.00 |
0.1318 |
0.1101 |
60.00 |
0.1646 |
0.1212 |
90.00 |
0.1797 |
0.1268 |
30.00 |
0.1815 |
0.1513 |
60.00 |
0.2209 |
0.1634 |
90.00 |
0.2329 |
0.1721 |
30.00 |
0.2398 |
0.2131 |
90.00 |
0.2965 |
0.2254 |
90.00 |
0.3092 |
0.2359 |
60.00 |
0.3236 |
0.2369 |
30.00 |
0.3186 |
0.2384 |
30.00 |
0.3179 |
0.2657 |
90.00 |
0.3561 |
0.2983 |
60.00 |
0.3897 |
0.3052 |
60.00 |
0.3991 |
0.3062 |
90.00 |
0.4024 |
0.3523 |
30.00 |
0.4353 |
0.3657 |
60.00 |
0.4537 |
0.3970 |
90.00 |
0.4964 |
0.3998 |
90.00 |
0.4948 |
0.4018 |
60.00 |
0.4891 |
0.4034 |
60.00 |
0.4933 |
0.4365 |
90.00 |
0.5350 |
0.4798 |
90.00 |
0.5722 |
0.4852 |
30.00 |
0.5543 |
0.4927 |
60.00 |
0.5687 |
0.5234 |
60.00 |
0.6006 |
0.5557 |
90.00 |
0.6393 |
0.5746 |
90.00 |
0.6568 |
0.5819 |
60.00 |
0.6549 |
0.5959 |
30.00 |
0.6437 |
0.6269 |
60.00 |
0.6876 |
0.6434 |
30.00 |
0.6828 |
0.6494 |
90.00 |
0.7180 |
0.7008 |
90.00 |
0.7581 |
0.7158 |
90.00 |
0.7670 |
0.7221 |
60.00 |
0.7659 |
0.7371 |
30.00 |
0.7587 |
0.7384 |
90.00 |
0.7874 |
0.7783 |
30.00 |
0.7928 |
0.7839 |
60.00 |
0.8131 |
0.7898 |
90.00 |
0.8282 |
0.8168 |
30.00 |
0.8248 |
0.8405 |
90.00 |
0.8685 |
0.8574 |
30.00 |
0.8603 |
0.8608 |
60.00 |
0.8779 |
0.8782 |
30.00 |
0.8795 |
0.8796 |
90.00 |
0.9005 |
0.8825 |
60.00 |
0.8967 |
0.8851 |
90.00 |
0.9041 |
0.8871 |
30.00 |
0.8876 |
0.8966 |
60.00 |
0.9083 |
0.9091 |
30.00 |
0.9082 |
0.9150 |
90.00 |
0.9285 |
0.9245 |
60.00 |
0.9320 |
0.9319 |
30.00 |
0.9302 |
0.9438 |
60.00 |
0.9489 |
0.9450 |
90.00 |
0.9533 |
0.9563 |
30.00 |
0.9545 |
0.9603 |
60.00 |
0.9637 |
0.9727 |
60.00 |
0.9749 |
0.9766 |
90.00 |
0.9800 |
0.9811 |
30.00 |
0.9800 |
0.9906 |
30.00 |
0.9899 |
Mole fraction of 1-Hexanol (1)
[ref]
Operational condition: Temperature, K =
413.15 (Liquid)
Mole fraction of 1-Hexanol (1) - Liquid |
Mole fraction of 1-Hexanol (1) - Gas |
0.0254 |
0.0406 |
0.0368 |
0.0580 |
0.0655 |
0.1013 |
0.0913 |
0.1397 |
0.1175 |
0.1754 |
0.2188 |
0.3022 |
0.3225 |
0.4160 |
0.4139 |
0.5054 |
0.6003 |
0.6646 |
0.9125 |
0.9211 |
0.9343 |
0.9401 |
0.9566 |
0.9601 |
0.9797 |
0.9812 |
0.9894 |
0.9901 |
Mole fraction of 1-Hexanol (1)
[ref]
Fixed |
Measured |
Mole fraction of 1-Hexanol (1) - Liquid |
Pressure, kPa - Gas |
Mole fraction of 1-Hexanol (1) - Gas |
0.0160 |
90.00 |
0.0246 |
0.0210 |
60.00 |
0.0327 |
0.0263 |
30.00 |
0.0396 |
0.0315 |
90.00 |
0.0480 |
0.0365 |
60.00 |
0.0560 |
0.0490 |
30.00 |
0.0732 |
0.0554 |
90.00 |
0.0843 |
0.0664 |
60.00 |
0.1005 |
0.0853 |
90.00 |
0.1287 |
0.0902 |
30.00 |
0.1318 |
0.1101 |
60.00 |
0.1646 |
0.1212 |
90.00 |
0.1797 |
0.1268 |
30.00 |
0.1815 |
0.1513 |
60.00 |
0.2209 |
0.1634 |
90.00 |
0.2329 |
0.1721 |
30.00 |
0.2398 |
0.2131 |
90.00 |
0.2965 |
0.2254 |
90.00 |
0.3092 |
0.2359 |
60.00 |
0.3236 |
0.2369 |
30.00 |
0.3186 |
0.2384 |
30.00 |
0.3179 |
0.2657 |
90.00 |
0.3561 |
0.2983 |
60.00 |
0.3897 |
0.3052 |
60.00 |
0.3991 |
0.3062 |
90.00 |
0.4024 |
0.3523 |
30.00 |
0.4353 |
0.3657 |
60.00 |
0.4537 |
0.3970 |
90.00 |
0.4964 |
0.3998 |
90.00 |
0.4948 |
0.4018 |
60.00 |
0.4891 |
0.4034 |
60.00 |
0.4933 |
0.4365 |
90.00 |
0.5350 |
0.4798 |
90.00 |
0.5722 |
0.4852 |
30.00 |
0.5543 |
0.4927 |
60.00 |
0.5687 |
0.5234 |
60.00 |
0.6006 |
0.5557 |
90.00 |
0.6393 |
0.5746 |
90.00 |
0.6568 |
0.5819 |
60.00 |
0.6549 |
0.5959 |
30.00 |
0.6437 |
0.6269 |
60.00 |
0.6876 |
0.6434 |
30.00 |
0.6828 |
0.6494 |
90.00 |
0.7180 |
0.7008 |
90.00 |
0.7581 |
0.7158 |
90.00 |
0.7670 |
0.7221 |
60.00 |
0.7659 |
0.7371 |
30.00 |
0.7587 |
0.7384 |
90.00 |
0.7874 |
0.7783 |
30.00 |
0.7928 |
0.7839 |
60.00 |
0.8131 |
0.7898 |
90.00 |
0.8282 |
0.8168 |
30.00 |
0.8248 |
0.8405 |
90.00 |
0.8685 |
0.8574 |
30.00 |
0.8603 |
0.8608 |
60.00 |
0.8779 |
0.8782 |
30.00 |
0.8795 |
0.8796 |
90.00 |
0.9005 |
0.8825 |
60.00 |
0.8967 |
0.8851 |
90.00 |
0.9041 |
0.8871 |
30.00 |
0.8876 |
0.8966 |
60.00 |
0.9083 |
0.9091 |
30.00 |
0.9082 |
0.9150 |
90.00 |
0.9285 |
0.9245 |
60.00 |
0.9320 |
0.9319 |
30.00 |
0.9302 |
0.9438 |
60.00 |
0.9489 |
0.9450 |
90.00 |
0.9533 |
0.9563 |
30.00 |
0.9545 |
0.9603 |
60.00 |
0.9637 |
0.9727 |
60.00 |
0.9749 |
0.9766 |
90.00 |
0.9800 |
0.9811 |
30.00 |
0.9800 |
0.9906 |
30.00 |
0.9899 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
413.15 (Liquid)
Mole fraction of 1-Hexanol (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0254 |
41.89 |
0.0368 |
42.22 |
0.0655 |
43.08 |
0.0913 |
43.90 |
0.1175 |
44.70 |
0.2188 |
47.25 |
0.3225 |
49.67 |
0.4139 |
51.19 |
0.6003 |
54.71 |
0.9125 |
57.23 |
0.9343 |
57.40 |
0.9566 |
57.45 |
0.9797 |
57.32 |
0.9894 |
57.18 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
413.15 (Liquid)
Mole fraction of 1-Hexanol (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0254 |
41.89 |
0.0368 |
42.22 |
0.0655 |
43.08 |
0.0913 |
43.90 |
0.1175 |
44.70 |
0.2188 |
47.25 |
0.3225 |
49.67 |
0.4139 |
51.19 |
0.6003 |
54.71 |
0.9125 |
57.23 |
0.9343 |
57.40 |
0.9566 |
57.45 |
0.9797 |
57.32 |
0.9894 |
57.18 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 1-Hexanol (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0160 |
90.00 |
439.63 |
0.0210 |
60.00 |
425.05 |
0.0263 |
30.00 |
402.87 |
0.0315 |
90.00 |
439.27 |
0.0365 |
60.00 |
424.73 |
0.0490 |
30.00 |
402.43 |
0.0554 |
90.00 |
438.70 |
0.0664 |
60.00 |
424.08 |
0.0853 |
90.00 |
438.01 |
0.0902 |
30.00 |
401.69 |
0.1101 |
60.00 |
423.14 |
0.1212 |
90.00 |
437.16 |
0.1268 |
30.00 |
401.07 |
0.1513 |
60.00 |
422.34 |
0.1634 |
90.00 |
436.31 |
0.1721 |
30.00 |
400.30 |
0.2131 |
90.00 |
435.34 |
0.2254 |
90.00 |
435.10 |
0.2359 |
60.00 |
420.83 |
0.2369 |
30.00 |
399.38 |
0.2384 |
30.00 |
399.31 |
0.2657 |
90.00 |
434.44 |
0.2983 |
60.00 |
419.75 |
0.3052 |
60.00 |
419.69 |
0.3062 |
90.00 |
433.63 |
0.3523 |
30.00 |
398.07 |
0.3657 |
60.00 |
418.96 |
0.3970 |
90.00 |
432.18 |
0.3998 |
90.00 |
432.01 |
0.4018 |
60.00 |
418.43 |
0.4034 |
60.00 |
418.41 |
0.4365 |
90.00 |
431.46 |
0.4798 |
90.00 |
430.85 |
0.4852 |
30.00 |
396.99 |
0.4927 |
60.00 |
417.38 |
0.5234 |
60.00 |
417.09 |
0.5557 |
90.00 |
429.89 |
0.5746 |
90.00 |
429.67 |
0.5819 |
60.00 |
416.39 |
0.5959 |
30.00 |
396.33 |
0.6269 |
60.00 |
416.06 |
0.6434 |
30.00 |
396.01 |
0.6494 |
90.00 |
428.96 |
0.7008 |
90.00 |
428.54 |
0.7158 |
90.00 |
428.49 |
0.7221 |
60.00 |
415.48 |
0.7371 |
30.00 |
395.68 |
0.7384 |
90.00 |
428.19 |
0.7783 |
30.00 |
395.66 |
0.7839 |
60.00 |
415.10 |
0.7898 |
90.00 |
427.71 |
0.8168 |
30.00 |
395.54 |
0.8405 |
90.00 |
427.38 |
0.8574 |
30.00 |
395.53 |
0.8608 |
60.00 |
414.69 |
0.8782 |
30.00 |
395.54 |
0.8796 |
90.00 |
427.38 |
0.8825 |
60.00 |
414.87 |
0.8851 |
90.00 |
427.17 |
0.8871 |
30.00 |
395.63 |
0.8966 |
60.00 |
414.56 |
0.9091 |
30.00 |
395.56 |
0.9150 |
90.00 |
427.05 |
0.9245 |
60.00 |
414.48 |
0.9319 |
30.00 |
395.51 |
0.9438 |
60.00 |
414.45 |
0.9450 |
90.00 |
426.90 |
0.9563 |
30.00 |
395.59 |
0.9603 |
60.00 |
414.42 |
0.9727 |
60.00 |
414.33 |
0.9766 |
90.00 |
426.77 |
0.9811 |
30.00 |
395.66 |
0.9906 |
30.00 |
395.70 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 1-Hexanol (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0160 |
90.00 |
439.63 |
0.0210 |
60.00 |
425.05 |
0.0263 |
30.00 |
402.87 |
0.0315 |
90.00 |
439.27 |
0.0365 |
60.00 |
424.73 |
0.0490 |
30.00 |
402.43 |
0.0554 |
90.00 |
438.70 |
0.0664 |
60.00 |
424.08 |
0.0853 |
90.00 |
438.01 |
0.0902 |
30.00 |
401.69 |
0.1101 |
60.00 |
423.14 |
0.1212 |
90.00 |
437.16 |
0.1268 |
30.00 |
401.07 |
0.1513 |
60.00 |
422.34 |
0.1634 |
90.00 |
436.31 |
0.1721 |
30.00 |
400.30 |
0.2131 |
90.00 |
435.34 |
0.2254 |
90.00 |
435.10 |
0.2359 |
60.00 |
420.83 |
0.2369 |
30.00 |
399.38 |
0.2384 |
30.00 |
399.31 |
0.2657 |
90.00 |
434.44 |
0.2983 |
60.00 |
419.75 |
0.3052 |
60.00 |
419.69 |
0.3062 |
90.00 |
433.63 |
0.3523 |
30.00 |
398.07 |
0.3657 |
60.00 |
418.96 |
0.3970 |
90.00 |
432.18 |
0.3998 |
90.00 |
432.01 |
0.4018 |
60.00 |
418.43 |
0.4034 |
60.00 |
418.41 |
0.4365 |
90.00 |
431.46 |
0.4798 |
90.00 |
430.85 |
0.4852 |
30.00 |
396.99 |
0.4927 |
60.00 |
417.38 |
0.5234 |
60.00 |
417.09 |
0.5557 |
90.00 |
429.89 |
0.5746 |
90.00 |
429.67 |
0.5819 |
60.00 |
416.39 |
0.5959 |
30.00 |
396.33 |
0.6269 |
60.00 |
416.06 |
0.6434 |
30.00 |
396.01 |
0.6494 |
90.00 |
428.96 |
0.7008 |
90.00 |
428.54 |
0.7158 |
90.00 |
428.49 |
0.7221 |
60.00 |
415.48 |
0.7371 |
30.00 |
395.68 |
0.7384 |
90.00 |
428.19 |
0.7783 |
30.00 |
395.66 |
0.7839 |
60.00 |
415.10 |
0.7898 |
90.00 |
427.71 |
0.8168 |
30.00 |
395.54 |
0.8405 |
90.00 |
427.38 |
0.8574 |
30.00 |
395.53 |
0.8608 |
60.00 |
414.69 |
0.8782 |
30.00 |
395.54 |
0.8796 |
90.00 |
427.38 |
0.8825 |
60.00 |
414.87 |
0.8851 |
90.00 |
427.17 |
0.8871 |
30.00 |
395.63 |
0.8966 |
60.00 |
414.56 |
0.9091 |
30.00 |
395.56 |
0.9150 |
90.00 |
427.05 |
0.9245 |
60.00 |
414.48 |
0.9319 |
30.00 |
395.51 |
0.9438 |
60.00 |
414.45 |
0.9450 |
90.00 |
426.90 |
0.9563 |
30.00 |
395.59 |
0.9603 |
60.00 |
414.42 |
0.9727 |
60.00 |
414.33 |
0.9766 |
90.00 |
426.77 |
0.9811 |
30.00 |
395.66 |
0.9906 |
30.00 |
395.70 |
Sources