Operational condition: Pressure, kPa = 101.8 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1-Hexanol (2) - Liquid | Viscosity, Pa*s - Liquid |
298.15 | 0.1493 | 0.0104 |
298.15 | 0.3989 | 0.0085 |
298.15 | 0.6071 | 0.0070 |
298.15 | 0.7831 | 0.0058 |
298.15 | 0.9346 | 0.0049 |
308.15 | 0.1493 | 0.0073 |
308.15 | 0.3989 | 0.0060 |
308.15 | 0.6071 | 0.0051 |
308.15 | 0.7831 | 0.0043 |
308.15 | 0.9346 | 0.0036 |
318.15 | 0.1493 | 0.0053 |
318.15 | 0.3989 | 0.0044 |
318.15 | 0.6071 | 0.0037 |
318.15 | 0.7831 | 0.0032 |
318.15 | 0.9346 | 0.0027 |
328.15 | 0.1493 | 0.0039 |
328.15 | 0.3989 | 0.0033 |
328.15 | 0.6071 | 0.0028 |
328.15 | 0.7831 | 0.0024 |
328.15 | 0.9346 | 0.0021 |
338.15 | 0.1493 | 0.0029 |
338.15 | 0.3989 | 0.0025 |
338.15 | 0.6071 | 0.0022 |
338.15 | 0.7831 | 0.0019 |
338.15 | 0.9346 | 0.0017 |
Operational condition: Pressure, kPa = 101.8 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1-Hexanol (2) - Liquid | Viscosity, Pa*s - Liquid |
298.15 | 0.1493 | 0.0104 |
298.15 | 0.3989 | 0.0085 |
298.15 | 0.6071 | 0.0070 |
298.15 | 0.7831 | 0.0058 |
298.15 | 0.9346 | 0.0049 |
308.15 | 0.1493 | 0.0073 |
308.15 | 0.3989 | 0.0060 |
308.15 | 0.6071 | 0.0051 |
308.15 | 0.7831 | 0.0043 |
308.15 | 0.9346 | 0.0036 |
318.15 | 0.1493 | 0.0053 |
318.15 | 0.3989 | 0.0044 |
318.15 | 0.6071 | 0.0037 |
318.15 | 0.7831 | 0.0032 |
318.15 | 0.9346 | 0.0027 |
328.15 | 0.1493 | 0.0039 |
328.15 | 0.3989 | 0.0033 |
328.15 | 0.6071 | 0.0028 |
328.15 | 0.7831 | 0.0024 |
328.15 | 0.9346 | 0.0021 |
338.15 | 0.1493 | 0.0029 |
338.15 | 0.3989 | 0.0025 |
338.15 | 0.6071 | 0.0022 |
338.15 | 0.7831 | 0.0019 |
338.15 | 0.9346 | 0.0017 |
Operational condition: Pressure, kPa = 101.8 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1-Hexanol (2) - Liquid | Mass density, kg/m3 - Liquid |
298.15 | 0.1493 | 825.8 |
298.15 | 0.3989 | 823.5 |
298.15 | 0.6071 | 821.2 |
298.15 | 0.7831 | 818.9 |
298.15 | 0.9346 | 816.9 |
308.15 | 0.1493 | 818.8 |
308.15 | 0.3989 | 816.5 |
308.15 | 0.6071 | 814.1 |
308.15 | 0.7831 | 811.8 |
308.15 | 0.9346 | 809.6 |
318.15 | 0.1493 | 811.8 |
318.15 | 0.3989 | 809.4 |
318.15 | 0.6071 | 807.0 |
318.15 | 0.7831 | 804.6 |
318.15 | 0.9346 | 802.3 |
328.15 | 0.1493 | 804.8 |
328.15 | 0.3989 | 802.2 |
328.15 | 0.6071 | 799.7 |
328.15 | 0.7831 | 797.2 |
328.15 | 0.9346 | 794.8 |
338.15 | 0.1493 | 797.6 |
338.15 | 0.3989 | 795.0 |
338.15 | 0.6071 | 792.3 |
338.15 | 0.7831 | 789.7 |
338.15 | 0.9346 | 787.2 |
Operational condition: Pressure, kPa = 101.8 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1-Hexanol (2) - Liquid | Mass density, kg/m3 - Liquid |
298.15 | 0.1493 | 825.8 |
298.15 | 0.3989 | 823.5 |
298.15 | 0.6071 | 821.2 |
298.15 | 0.7831 | 818.9 |
298.15 | 0.9346 | 816.9 |
308.15 | 0.1493 | 818.8 |
308.15 | 0.3989 | 816.5 |
308.15 | 0.6071 | 814.1 |
308.15 | 0.7831 | 811.8 |
308.15 | 0.9346 | 809.6 |
318.15 | 0.1493 | 811.8 |
318.15 | 0.3989 | 809.4 |
318.15 | 0.6071 | 807.0 |
318.15 | 0.7831 | 804.6 |
318.15 | 0.9346 | 802.3 |
328.15 | 0.1493 | 804.8 |
328.15 | 0.3989 | 802.2 |
328.15 | 0.6071 | 799.7 |
328.15 | 0.7831 | 797.2 |
328.15 | 0.9346 | 794.8 |
338.15 | 0.1493 | 797.6 |
338.15 | 0.3989 | 795.0 |
338.15 | 0.6071 | 792.3 |
338.15 | 0.7831 | 789.7 |
338.15 | 0.9346 | 787.2 |