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 | 0.1701 | 0.0144 |
298.15 | 0.4377 | 0.0107 |
298.15 | 0.6449 | 0.0082 |
298.15 | 0.8097 | 0.0063 |
298.15 | 0.9429 | 0.0051 |
308.15 | 0.1701 | 0.0099 |
308.15 | 0.4377 | 0.0075 |
308.15 | 0.6449 | 0.0058 |
308.15 | 0.8097 | 0.0046 |
308.15 | 0.9429 | 0.0038 |
318.15 | 0.1701 | 0.0070 |
318.15 | 0.4377 | 0.0054 |
318.15 | 0.6449 | 0.0043 |
318.15 | 0.8097 | 0.0035 |
318.15 | 0.9429 | 0.0028 |
328.15 | 0.1701 | 0.0051 |
328.15 | 0.4377 | 0.0040 |
328.15 | 0.6449 | 0.0032 |
328.15 | 0.8097 | 0.0026 |
328.15 | 0.9429 | 0.0022 |
338.15 | 0.1701 | 0.0038 |
338.15 | 0.4377 | 0.0030 |
338.15 | 0.6449 | 0.0025 |
338.15 | 0.8097 | 0.0020 |
338.15 | 0.9429 | 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 | 0.1701 | 0.0144 |
298.15 | 0.4377 | 0.0107 |
298.15 | 0.6449 | 0.0082 |
298.15 | 0.8097 | 0.0063 |
298.15 | 0.9429 | 0.0051 |
308.15 | 0.1701 | 0.0099 |
308.15 | 0.4377 | 0.0075 |
308.15 | 0.6449 | 0.0058 |
308.15 | 0.8097 | 0.0046 |
308.15 | 0.9429 | 0.0038 |
318.15 | 0.1701 | 0.0070 |
318.15 | 0.4377 | 0.0054 |
318.15 | 0.6449 | 0.0043 |
318.15 | 0.8097 | 0.0035 |
318.15 | 0.9429 | 0.0028 |
328.15 | 0.1701 | 0.0051 |
328.15 | 0.4377 | 0.0040 |
328.15 | 0.6449 | 0.0032 |
328.15 | 0.8097 | 0.0026 |
328.15 | 0.9429 | 0.0022 |
338.15 | 0.1701 | 0.0038 |
338.15 | 0.4377 | 0.0030 |
338.15 | 0.6449 | 0.0025 |
338.15 | 0.8097 | 0.0020 |
338.15 | 0.9429 | 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 | 0.1701 | 828.0 |
298.15 | 0.4377 | 825.0 |
298.15 | 0.6449 | 822.2 |
298.15 | 0.8097 | 819.6 |
298.15 | 0.9429 | 816.9 |
308.15 | 0.1701 | 821.2 |
308.15 | 0.4377 | 818.1 |
308.15 | 0.6449 | 815.2 |
308.15 | 0.8097 | 812.5 |
308.15 | 0.9429 | 809.8 |
318.15 | 0.1701 | 814.3 |
318.15 | 0.4377 | 811.1 |
318.15 | 0.6449 | 808.2 |
318.15 | 0.8097 | 805.3 |
318.15 | 0.9429 | 802.5 |
328.15 | 0.1701 | 807.4 |
328.15 | 0.4377 | 804.1 |
328.15 | 0.6449 | 801.0 |
328.15 | 0.8097 | 798.0 |
328.15 | 0.9429 | 795.1 |
338.15 | 0.1701 | 800.3 |
338.15 | 0.4377 | 796.9 |
338.15 | 0.6449 | 793.7 |
338.15 | 0.8097 | 790.5 |
338.15 | 0.9429 | 787.5 |
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 | 0.1701 | 828.0 |
298.15 | 0.4377 | 825.0 |
298.15 | 0.6449 | 822.2 |
298.15 | 0.8097 | 819.6 |
298.15 | 0.9429 | 816.9 |
308.15 | 0.1701 | 821.2 |
308.15 | 0.4377 | 818.1 |
308.15 | 0.6449 | 815.2 |
308.15 | 0.8097 | 812.5 |
308.15 | 0.9429 | 809.8 |
318.15 | 0.1701 | 814.3 |
318.15 | 0.4377 | 811.1 |
318.15 | 0.6449 | 808.2 |
318.15 | 0.8097 | 805.3 |
318.15 | 0.9429 | 802.5 |
328.15 | 0.1701 | 807.4 |
328.15 | 0.4377 | 804.1 |
328.15 | 0.6449 | 801.0 |
328.15 | 0.8097 | 798.0 |
328.15 | 0.9429 | 795.1 |
338.15 | 0.1701 | 800.3 |
338.15 | 0.4377 | 796.9 |
338.15 | 0.6449 | 793.7 |
338.15 | 0.8097 | 790.5 |
338.15 | 0.9429 | 787.5 |