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 | 0.1207 | 0.0072 |
298.15 | 0.3506 | 0.0064 |
298.15 | 0.5615 | 0.0058 |
298.15 | 0.7463 | 0.0052 |
298.15 | 0.9227 | 0.0047 |
308.15 | 0.1207 | 0.0052 |
308.15 | 0.3506 | 0.0047 |
308.15 | 0.5615 | 0.0043 |
308.15 | 0.7463 | 0.0039 |
308.15 | 0.9227 | 0.0035 |
318.15 | 0.1207 | 0.0038 |
318.15 | 0.3506 | 0.0035 |
318.15 | 0.5615 | 0.0032 |
318.15 | 0.7463 | 0.0029 |
318.15 | 0.9227 | 0.0027 |
328.15 | 0.1207 | 0.0029 |
328.15 | 0.3506 | 0.0026 |
328.15 | 0.5615 | 0.0024 |
328.15 | 0.7463 | 0.0022 |
328.15 | 0.9227 | 0.0021 |
338.15 | 0.1207 | 0.0022 |
338.15 | 0.3506 | 0.0020 |
338.15 | 0.5615 | 0.0019 |
338.15 | 0.7463 | 0.0018 |
338.15 | 0.9227 | 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 | 0.1207 | 0.0072 |
298.15 | 0.3506 | 0.0064 |
298.15 | 0.5615 | 0.0058 |
298.15 | 0.7463 | 0.0052 |
298.15 | 0.9227 | 0.0047 |
308.15 | 0.1207 | 0.0052 |
308.15 | 0.3506 | 0.0047 |
308.15 | 0.5615 | 0.0043 |
308.15 | 0.7463 | 0.0039 |
308.15 | 0.9227 | 0.0035 |
318.15 | 0.1207 | 0.0038 |
318.15 | 0.3506 | 0.0035 |
318.15 | 0.5615 | 0.0032 |
318.15 | 0.7463 | 0.0029 |
318.15 | 0.9227 | 0.0027 |
328.15 | 0.1207 | 0.0029 |
328.15 | 0.3506 | 0.0026 |
328.15 | 0.5615 | 0.0024 |
328.15 | 0.7463 | 0.0022 |
328.15 | 0.9227 | 0.0021 |
338.15 | 0.1207 | 0.0022 |
338.15 | 0.3506 | 0.0020 |
338.15 | 0.5615 | 0.0019 |
338.15 | 0.7463 | 0.0018 |
338.15 | 0.9227 | 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 | 0.1207 | 821.1 |
298.15 | 0.3506 | 820.0 |
298.15 | 0.5615 | 818.7 |
298.15 | 0.7463 | 817.5 |
298.15 | 0.9227 | 816.5 |
308.15 | 0.1207 | 814.1 |
308.15 | 0.3506 | 812.8 |
308.15 | 0.5615 | 811.5 |
308.15 | 0.7463 | 810.3 |
308.15 | 0.9227 | 809.2 |
318.15 | 0.1207 | 807.0 |
318.15 | 0.3506 | 805.7 |
318.15 | 0.5615 | 804.3 |
318.15 | 0.7463 | 803.1 |
318.15 | 0.9227 | 801.8 |
328.15 | 0.1207 | 799.8 |
328.15 | 0.3506 | 798.4 |
328.15 | 0.5615 | 797.0 |
328.15 | 0.7463 | 795.7 |
328.15 | 0.9227 | 794.4 |
338.15 | 0.1207 | 792.4 |
338.15 | 0.3506 | 791.0 |
338.15 | 0.5615 | 789.5 |
338.15 | 0.7463 | 788.1 |
338.15 | 0.9227 | 786.7 |
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 | 0.1207 | 821.1 |
298.15 | 0.3506 | 820.0 |
298.15 | 0.5615 | 818.7 |
298.15 | 0.7463 | 817.5 |
298.15 | 0.9227 | 816.5 |
308.15 | 0.1207 | 814.1 |
308.15 | 0.3506 | 812.8 |
308.15 | 0.5615 | 811.5 |
308.15 | 0.7463 | 810.3 |
308.15 | 0.9227 | 809.2 |
318.15 | 0.1207 | 807.0 |
318.15 | 0.3506 | 805.7 |
318.15 | 0.5615 | 804.3 |
318.15 | 0.7463 | 803.1 |
318.15 | 0.9227 | 801.8 |
328.15 | 0.1207 | 799.8 |
328.15 | 0.3506 | 798.4 |
328.15 | 0.5615 | 797.0 |
328.15 | 0.7463 | 795.7 |
328.15 | 0.9227 | 794.4 |
338.15 | 0.1207 | 792.4 |
338.15 | 0.3506 | 791.0 |
338.15 | 0.5615 | 789.5 |
338.15 | 0.7463 | 788.1 |
338.15 | 0.9227 | 786.7 |