Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Viscosity, Pa*s - Liquid |
293.15 | 0.0000 | 0.0021 |
293.15 | 0.0610 | 0.0024 |
293.15 | 0.1205 | 0.0026 |
293.15 | 0.2357 | 0.0028 |
293.15 | 0.3458 | 0.0030 |
293.15 | 0.4513 | 0.0032 |
293.15 | 0.5523 | 0.0034 |
293.15 | 0.6492 | 0.0035 |
293.15 | 0.7421 | 0.0035 |
293.15 | 0.8315 | 0.0036 |
293.15 | 0.9174 | 0.0037 |
293.15 | 1.0000 | 0.0040 |
298.15 | 0.0000 | 0.0019 |
298.15 | 0.0610 | 0.0021 |
298.15 | 0.1205 | 0.0023 |
298.15 | 0.2357 | 0.0025 |
298.15 | 0.3458 | 0.0026 |
298.15 | 0.4513 | 0.0028 |
298.15 | 0.5523 | 0.0029 |
298.15 | 0.6492 | 0.0030 |
298.15 | 0.7421 | 0.0030 |
298.15 | 0.8315 | 0.0031 |
298.15 | 0.9174 | 0.0031 |
298.15 | 1.0000 | 0.0034 |
303.15 | 0.0000 | 0.0018 |
303.15 | 0.0610 | 0.0019 |
303.15 | 0.1205 | 0.0021 |
303.15 | 0.2357 | 0.0022 |
303.15 | 0.3458 | 0.0023 |
303.15 | 0.4513 | 0.0025 |
303.15 | 0.5523 | 0.0026 |
303.15 | 0.6492 | 0.0026 |
303.15 | 0.7421 | 0.0026 |
303.15 | 0.8315 | 0.0026 |
303.15 | 0.9174 | 0.0027 |
303.15 | 1.0000 | 0.0029 |
308.15 | 0.0000 | 0.0016 |
308.15 | 0.0610 | 0.0017 |
308.15 | 0.1205 | 0.0018 |
308.15 | 0.2357 | 0.0019 |
308.15 | 0.3458 | 0.0020 |
308.15 | 0.4513 | 0.0021 |
308.15 | 0.5523 | 0.0022 |
308.15 | 0.6492 | 0.0023 |
308.15 | 0.7421 | 0.0023 |
308.15 | 0.8315 | 0.0023 |
308.15 | 0.9174 | 0.0023 |
308.15 | 1.0000 | 0.0025 |
313.15 | 0.0000 | 0.0014 |
313.15 | 0.0610 | 0.0015 |
313.15 | 0.1205 | 0.0016 |
313.15 | 0.2357 | 0.0017 |
313.15 | 0.3458 | 0.0018 |
313.15 | 0.4513 | 0.0018 |
313.15 | 0.5523 | 0.0019 |
313.15 | 0.6492 | 0.0020 |
313.15 | 0.7421 | 0.0020 |
313.15 | 0.8315 | 0.0020 |
313.15 | 0.9174 | 0.0020 |
313.15 | 1.0000 | 0.0021 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Viscosity, Pa*s - Liquid |
293.15 | 0.0000 | 0.0021 |
293.15 | 0.0610 | 0.0024 |
293.15 | 0.1205 | 0.0026 |
293.15 | 0.2357 | 0.0028 |
293.15 | 0.3458 | 0.0030 |
293.15 | 0.4513 | 0.0032 |
293.15 | 0.5523 | 0.0034 |
293.15 | 0.6492 | 0.0035 |
293.15 | 0.7421 | 0.0035 |
293.15 | 0.8315 | 0.0036 |
293.15 | 0.9174 | 0.0037 |
293.15 | 1.0000 | 0.0040 |
298.15 | 0.0000 | 0.0019 |
298.15 | 0.0610 | 0.0021 |
298.15 | 0.1205 | 0.0023 |
298.15 | 0.2357 | 0.0025 |
298.15 | 0.3458 | 0.0026 |
298.15 | 0.4513 | 0.0028 |
298.15 | 0.5523 | 0.0029 |
298.15 | 0.6492 | 0.0030 |
298.15 | 0.7421 | 0.0030 |
298.15 | 0.8315 | 0.0031 |
298.15 | 0.9174 | 0.0031 |
298.15 | 1.0000 | 0.0034 |
303.15 | 0.0000 | 0.0018 |
303.15 | 0.0610 | 0.0019 |
303.15 | 0.1205 | 0.0021 |
303.15 | 0.2357 | 0.0022 |
303.15 | 0.3458 | 0.0023 |
303.15 | 0.4513 | 0.0025 |
303.15 | 0.5523 | 0.0026 |
303.15 | 0.6492 | 0.0026 |
303.15 | 0.7421 | 0.0026 |
303.15 | 0.8315 | 0.0026 |
303.15 | 0.9174 | 0.0027 |
303.15 | 1.0000 | 0.0029 |
308.15 | 0.0000 | 0.0016 |
308.15 | 0.0610 | 0.0017 |
308.15 | 0.1205 | 0.0018 |
308.15 | 0.2357 | 0.0019 |
308.15 | 0.3458 | 0.0020 |
308.15 | 0.4513 | 0.0021 |
308.15 | 0.5523 | 0.0022 |
308.15 | 0.6492 | 0.0023 |
308.15 | 0.7421 | 0.0023 |
308.15 | 0.8315 | 0.0023 |
308.15 | 0.9174 | 0.0023 |
308.15 | 1.0000 | 0.0025 |
313.15 | 0.0000 | 0.0014 |
313.15 | 0.0610 | 0.0015 |
313.15 | 0.1205 | 0.0016 |
313.15 | 0.2357 | 0.0017 |
313.15 | 0.3458 | 0.0018 |
313.15 | 0.4513 | 0.0018 |
313.15 | 0.5523 | 0.0019 |
313.15 | 0.6492 | 0.0020 |
313.15 | 0.7421 | 0.0020 |
313.15 | 0.8315 | 0.0020 |
313.15 | 0.9174 | 0.0020 |
313.15 | 1.0000 | 0.0021 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0000 | 866.85 |
293.15 | 0.0610 | 865.7 |
293.15 | 0.1205 | 865.02 |
293.15 | 0.2357 | 861.79 |
293.15 | 0.3458 | 856.98 |
293.15 | 0.4513 | 850.89 |
293.15 | 0.5523 | 847.01 |
293.15 | 0.6492 | 839.36 |
293.15 | 0.7421 | 830.79 |
293.15 | 0.8315 | 820.81 |
293.15 | 0.9174 | 814.12 |
293.15 | 1.0000 | 801.96 |
298.15 | 0.0000 | 862.31 |
298.15 | 0.0610 | 861.18 |
298.15 | 0.1205 | 860.59 |
298.15 | 0.2357 | 857.37 |
298.15 | 0.3458 | 852.62 |
298.15 | 0.4513 | 846.55 |
298.15 | 0.5523 | 842.76 |
298.15 | 0.6492 | 835.13 |
298.15 | 0.7421 | 826.7 |
298.15 | 0.8315 | 816.78 |
298.15 | 0.9174 | 810.19 |
298.15 | 1.0000 | 798.12 |
303.15 | 0.0000 | 857.79 |
303.15 | 0.0610 | 856.68 |
303.15 | 0.1205 | 856.11 |
303.15 | 0.2357 | 852.93 |
303.15 | 0.3458 | 848.23 |
303.15 | 0.4513 | 842.2 |
303.15 | 0.5523 | 838.46 |
303.15 | 0.6492 | 830.89 |
303.15 | 0.7421 | 822.55 |
303.15 | 0.8315 | 812.73 |
303.15 | 0.9174 | 806.19 |
303.15 | 1.0000 | 794.22 |
308.15 | 0.0000 | 853.24 |
308.15 | 0.0610 | 852.18 |
308.15 | 0.1205 | 851.64 |
308.15 | 0.2357 | 848.49 |
308.15 | 0.3458 | 843.79 |
308.15 | 0.4513 | 837.83 |
308.15 | 0.5523 | 834.13 |
308.15 | 0.6492 | 826.62 |
308.15 | 0.7421 | 818.36 |
308.15 | 0.8315 | 808.63 |
308.15 | 0.9174 | 802.09 |
308.15 | 1.0000 | 790.27 |
313.15 | 0.0000 | 848.71 |
313.15 | 0.0610 | 847.71 |
313.15 | 0.1205 | 847.15 |
313.15 | 0.2357 | 844.09 |
313.15 | 0.3458 | 839.39 |
313.15 | 0.4513 | 833.46 |
313.15 | 0.5523 | 829.78 |
313.15 | 0.6492 | 822.37 |
313.15 | 0.7421 | 814.15 |
313.15 | 0.8315 | 804.54 |
313.15 | 0.9174 | 798.0 |
313.15 | 1.0000 | 786.27 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0000 | 866.85 |
293.15 | 0.0610 | 865.7 |
293.15 | 0.1205 | 865.02 |
293.15 | 0.2357 | 861.79 |
293.15 | 0.3458 | 856.98 |
293.15 | 0.4513 | 850.89 |
293.15 | 0.5523 | 847.01 |
293.15 | 0.6492 | 839.36 |
293.15 | 0.7421 | 830.79 |
293.15 | 0.8315 | 820.81 |
293.15 | 0.9174 | 814.12 |
293.15 | 1.0000 | 801.96 |
298.15 | 0.0000 | 862.31 |
298.15 | 0.0610 | 861.18 |
298.15 | 0.1205 | 860.59 |
298.15 | 0.2357 | 857.37 |
298.15 | 0.3458 | 852.62 |
298.15 | 0.4513 | 846.55 |
298.15 | 0.5523 | 842.76 |
298.15 | 0.6492 | 835.13 |
298.15 | 0.7421 | 826.7 |
298.15 | 0.8315 | 816.78 |
298.15 | 0.9174 | 810.19 |
298.15 | 1.0000 | 798.12 |
303.15 | 0.0000 | 857.79 |
303.15 | 0.0610 | 856.68 |
303.15 | 0.1205 | 856.11 |
303.15 | 0.2357 | 852.93 |
303.15 | 0.3458 | 848.23 |
303.15 | 0.4513 | 842.2 |
303.15 | 0.5523 | 838.46 |
303.15 | 0.6492 | 830.89 |
303.15 | 0.7421 | 822.55 |
303.15 | 0.8315 | 812.73 |
303.15 | 0.9174 | 806.19 |
303.15 | 1.0000 | 794.22 |
308.15 | 0.0000 | 853.24 |
308.15 | 0.0610 | 852.18 |
308.15 | 0.1205 | 851.64 |
308.15 | 0.2357 | 848.49 |
308.15 | 0.3458 | 843.79 |
308.15 | 0.4513 | 837.83 |
308.15 | 0.5523 | 834.13 |
308.15 | 0.6492 | 826.62 |
308.15 | 0.7421 | 818.36 |
308.15 | 0.8315 | 808.63 |
308.15 | 0.9174 | 802.09 |
308.15 | 1.0000 | 790.27 |
313.15 | 0.0000 | 848.71 |
313.15 | 0.0610 | 847.71 |
313.15 | 0.1205 | 847.15 |
313.15 | 0.2357 | 844.09 |
313.15 | 0.3458 | 839.39 |
313.15 | 0.4513 | 833.46 |
313.15 | 0.5523 | 829.78 |
313.15 | 0.6492 | 822.37 |
313.15 | 0.7421 | 814.15 |
313.15 | 0.8315 | 804.54 |
313.15 | 0.9174 | 798.0 |
313.15 | 1.0000 | 786.27 |