Datasets
-
Mole fraction (2)
-
η - Viscosity, Pa*s (2)
-
ρl - Mass density, kg/m3 (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of o-Xylene (2)
[ref]
Fixed |
Measured |
Mole fraction of o-Xylene (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of o-Xylene (2) - Gas |
0.0000 |
428.45 |
0.0000 |
0.0625 |
427.45 |
0.0948 |
0.1035 |
426.75 |
0.1540 |
0.1800 |
425.45 |
0.2583 |
0.2597 |
424.15 |
0.3585 |
0.3192 |
423.15 |
0.4279 |
0.3654 |
422.45 |
0.4787 |
0.4279 |
421.45 |
0.5434 |
0.4795 |
420.65 |
0.5934 |
0.5560 |
419.55 |
0.6623 |
0.6500 |
418.35 |
0.7392 |
0.7111 |
417.65 |
0.7854 |
0.8233 |
416.55 |
0.8650 |
0.8858 |
416.05 |
0.9087 |
0.9350 |
415.75 |
0.9449 |
1.0000 |
415.45 |
1.0000 |
Mole fraction of o-Xylene (2)
[ref]
Fixed |
Measured |
Mole fraction of o-Xylene (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of o-Xylene (2) - Gas |
0.0000 |
428.45 |
0.0000 |
0.0625 |
427.45 |
0.0948 |
0.1035 |
426.75 |
0.1540 |
0.1800 |
425.45 |
0.2583 |
0.2597 |
424.15 |
0.3585 |
0.3192 |
423.15 |
0.4279 |
0.3654 |
422.45 |
0.4787 |
0.4279 |
421.45 |
0.5434 |
0.4795 |
420.65 |
0.5934 |
0.5560 |
419.55 |
0.6623 |
0.6500 |
418.35 |
0.7392 |
0.7111 |
417.65 |
0.7854 |
0.8233 |
416.55 |
0.8650 |
0.8858 |
416.05 |
0.9087 |
0.9350 |
415.75 |
0.9449 |
1.0000 |
415.45 |
1.0000 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1-Hexanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
308.15 |
0.0000 |
0.0007 |
308.15 |
0.0999 |
0.0007 |
308.15 |
0.1999 |
0.0008 |
308.15 |
0.2999 |
0.0009 |
308.15 |
0.4001 |
0.0010 |
308.15 |
0.4997 |
0.0012 |
308.15 |
0.6000 |
0.0015 |
308.15 |
0.7000 |
0.0018 |
308.15 |
0.8000 |
0.0022 |
308.15 |
0.8999 |
0.0027 |
308.15 |
1.0000 |
0.0033 |
318.15 |
0.0000 |
0.0006 |
318.15 |
0.0999 |
0.0006 |
318.15 |
0.1999 |
0.0007 |
318.15 |
0.2999 |
0.0008 |
318.15 |
0.4001 |
0.0009 |
318.15 |
0.4997 |
0.0010 |
318.15 |
0.6000 |
0.0012 |
318.15 |
0.7000 |
0.0014 |
318.15 |
0.8000 |
0.0017 |
318.15 |
0.8999 |
0.0021 |
318.15 |
1.0000 |
0.0025 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1-Hexanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
308.15 |
0.0000 |
0.0007 |
308.15 |
0.0999 |
0.0007 |
308.15 |
0.1999 |
0.0008 |
308.15 |
0.2999 |
0.0009 |
308.15 |
0.4001 |
0.0010 |
308.15 |
0.4997 |
0.0012 |
308.15 |
0.6000 |
0.0015 |
308.15 |
0.7000 |
0.0018 |
308.15 |
0.8000 |
0.0022 |
308.15 |
0.8999 |
0.0027 |
308.15 |
1.0000 |
0.0033 |
318.15 |
0.0000 |
0.0006 |
318.15 |
0.0999 |
0.0006 |
318.15 |
0.1999 |
0.0007 |
318.15 |
0.2999 |
0.0008 |
318.15 |
0.4001 |
0.0009 |
318.15 |
0.4997 |
0.0010 |
318.15 |
0.6000 |
0.0012 |
318.15 |
0.7000 |
0.0014 |
318.15 |
0.8000 |
0.0017 |
318.15 |
0.8999 |
0.0021 |
318.15 |
1.0000 |
0.0025 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1-Hexanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
308.15 |
0.0000 |
866.7 |
308.15 |
0.0999 |
860.1 |
308.15 |
0.1999 |
853.9 |
308.15 |
0.2999 |
847.9 |
308.15 |
0.4001 |
842.1 |
308.15 |
0.4997 |
836.4 |
308.15 |
0.6000 |
830.7 |
308.15 |
0.7000 |
825.1 |
308.15 |
0.8000 |
819.5 |
308.15 |
0.8999 |
814.0 |
308.15 |
1.0000 |
808.5 |
318.15 |
0.0000 |
858.4 |
318.15 |
0.0999 |
851.7 |
318.15 |
0.1999 |
845.6 |
318.15 |
0.2999 |
839.7 |
318.15 |
0.4001 |
833.9 |
318.15 |
0.4997 |
828.3 |
318.15 |
0.6000 |
822.7 |
318.15 |
0.7000 |
817.2 |
318.15 |
0.8000 |
811.8 |
318.15 |
0.8999 |
806.4 |
318.15 |
1.0000 |
801.2 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1-Hexanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
308.15 |
0.0000 |
866.7 |
308.15 |
0.0999 |
860.1 |
308.15 |
0.1999 |
853.9 |
308.15 |
0.2999 |
847.9 |
308.15 |
0.4001 |
842.1 |
308.15 |
0.4997 |
836.4 |
308.15 |
0.6000 |
830.7 |
308.15 |
0.7000 |
825.1 |
308.15 |
0.8000 |
819.5 |
308.15 |
0.8999 |
814.0 |
308.15 |
1.0000 |
808.5 |
318.15 |
0.0000 |
858.4 |
318.15 |
0.0999 |
851.7 |
318.15 |
0.1999 |
845.6 |
318.15 |
0.2999 |
839.7 |
318.15 |
0.4001 |
833.9 |
318.15 |
0.4997 |
828.3 |
318.15 |
0.6000 |
822.7 |
318.15 |
0.7000 |
817.2 |
318.15 |
0.8000 |
811.8 |
318.15 |
0.8999 |
806.4 |
318.15 |
1.0000 |
801.2 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
95.6 (Liquid)
Mole fraction of o-Xylene (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
428.45 |
0.0625 |
427.45 |
0.1035 |
426.75 |
0.1800 |
425.45 |
0.2597 |
424.15 |
0.3192 |
423.15 |
0.3654 |
422.45 |
0.4279 |
421.45 |
0.4795 |
420.65 |
0.5560 |
419.55 |
0.6500 |
418.35 |
0.7111 |
417.65 |
0.8233 |
416.55 |
0.8858 |
416.05 |
0.9350 |
415.75 |
1.0000 |
415.45 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
95.6 (Liquid)
Mole fraction of o-Xylene (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
428.45 |
0.0625 |
427.45 |
0.1035 |
426.75 |
0.1800 |
425.45 |
0.2597 |
424.15 |
0.3192 |
423.15 |
0.3654 |
422.45 |
0.4279 |
421.45 |
0.4795 |
420.65 |
0.5560 |
419.55 |
0.6500 |
418.35 |
0.7111 |
417.65 |
0.8233 |
416.55 |
0.8858 |
416.05 |
0.9350 |
415.75 |
1.0000 |
415.45 |
Sources