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 | 0.1577 | 0.0123 |
298.15 | 0.4196 | 0.0095 |
298.15 | 0.6279 | 0.0075 |
298.15 | 0.7981 | 0.0061 |
298.15 | 0.9389 | 0.0048 |
308.15 | 0.1577 | 0.0085 |
308.15 | 0.4196 | 0.0067 |
308.15 | 0.6279 | 0.0054 |
308.15 | 0.7981 | 0.0044 |
308.15 | 0.9389 | 0.0035 |
318.15 | 0.1577 | 0.0061 |
318.15 | 0.4196 | 0.0049 |
318.15 | 0.6279 | 0.0040 |
318.15 | 0.7981 | 0.0033 |
318.15 | 0.9389 | 0.0027 |
328.15 | 0.1577 | 0.0045 |
328.15 | 0.4196 | 0.0036 |
328.15 | 0.6279 | 0.0030 |
328.15 | 0.7981 | 0.0025 |
328.15 | 0.9389 | 0.0021 |
338.15 | 0.1577 | 0.0034 |
338.15 | 0.4196 | 0.0028 |
338.15 | 0.6279 | 0.0023 |
338.15 | 0.7981 | 0.0020 |
338.15 | 0.9389 | 0.0016 |
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 | 0.1577 | 0.0123 |
298.15 | 0.4196 | 0.0095 |
298.15 | 0.6279 | 0.0075 |
298.15 | 0.7981 | 0.0061 |
298.15 | 0.9389 | 0.0048 |
308.15 | 0.1577 | 0.0085 |
308.15 | 0.4196 | 0.0067 |
308.15 | 0.6279 | 0.0054 |
308.15 | 0.7981 | 0.0044 |
308.15 | 0.9389 | 0.0035 |
318.15 | 0.1577 | 0.0061 |
318.15 | 0.4196 | 0.0049 |
318.15 | 0.6279 | 0.0040 |
318.15 | 0.7981 | 0.0033 |
318.15 | 0.9389 | 0.0027 |
328.15 | 0.1577 | 0.0045 |
328.15 | 0.4196 | 0.0036 |
328.15 | 0.6279 | 0.0030 |
328.15 | 0.7981 | 0.0025 |
328.15 | 0.9389 | 0.0021 |
338.15 | 0.1577 | 0.0034 |
338.15 | 0.4196 | 0.0028 |
338.15 | 0.6279 | 0.0023 |
338.15 | 0.7981 | 0.0020 |
338.15 | 0.9389 | 0.0016 |
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 | 0.1577 | 826.8 |
298.15 | 0.4196 | 824.2 |
298.15 | 0.6279 | 821.8 |
298.15 | 0.7981 | 819.2 |
298.15 | 0.9389 | 817.1 |
308.15 | 0.1577 | 819.8 |
308.15 | 0.4196 | 817.2 |
308.15 | 0.6279 | 814.6 |
308.15 | 0.7981 | 812.2 |
308.15 | 0.9389 | 809.9 |
318.15 | 0.1577 | 812.9 |
318.15 | 0.4196 | 810.2 |
318.15 | 0.6279 | 807.5 |
318.15 | 0.7981 | 805.0 |
318.15 | 0.9389 | 802.6 |
328.15 | 0.1577 | 805.9 |
328.15 | 0.4196 | 803.1 |
328.15 | 0.6279 | 800.3 |
328.15 | 0.7981 | 797.6 |
328.15 | 0.9389 | 795.1 |
338.15 | 0.1577 | 798.8 |
338.15 | 0.4196 | 795.9 |
338.15 | 0.6279 | 792.9 |
338.15 | 0.7981 | 790.2 |
338.15 | 0.9389 | 787.4 |
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 | 0.1577 | 826.8 |
298.15 | 0.4196 | 824.2 |
298.15 | 0.6279 | 821.8 |
298.15 | 0.7981 | 819.2 |
298.15 | 0.9389 | 817.1 |
308.15 | 0.1577 | 819.8 |
308.15 | 0.4196 | 817.2 |
308.15 | 0.6279 | 814.6 |
308.15 | 0.7981 | 812.2 |
308.15 | 0.9389 | 809.9 |
318.15 | 0.1577 | 812.9 |
318.15 | 0.4196 | 810.2 |
318.15 | 0.6279 | 807.5 |
318.15 | 0.7981 | 805.0 |
318.15 | 0.9389 | 802.6 |
328.15 | 0.1577 | 805.9 |
328.15 | 0.4196 | 803.1 |
328.15 | 0.6279 | 800.3 |
328.15 | 0.7981 | 797.6 |
328.15 | 0.9389 | 795.1 |
338.15 | 0.1577 | 798.8 |
338.15 | 0.4196 | 795.9 |
338.15 | 0.6279 | 792.9 |
338.15 | 0.7981 | 790.2 |
338.15 | 0.9389 | 787.4 |