Operational condition: Pressure, kPa = 101.325 (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 | 0.0515 | 0.0022 |
293.15 | 0.0983 | 0.0024 |
293.15 | 0.1506 | 0.0025 |
293.15 | 0.2011 | 0.0027 |
293.15 | 0.2971 | 0.0031 |
293.15 | 0.4020 | 0.0035 |
293.15 | 0.4982 | 0.0038 |
293.15 | 0.6001 | 0.0041 |
293.15 | 0.6995 | 0.0044 |
293.15 | 0.7978 | 0.0045 |
293.15 | 0.8995 | 0.0044 |
293.15 | 1.0000 | 0.0040 |
298.15 | 0.0000 | 0.0018 |
298.15 | 0.0515 | 0.0019 |
298.15 | 0.0983 | 0.0020 |
298.15 | 0.1506 | 0.0022 |
298.15 | 0.2011 | 0.0024 |
298.15 | 0.2971 | 0.0026 |
298.15 | 0.4020 | 0.0030 |
298.15 | 0.4982 | 0.0032 |
298.15 | 0.6001 | 0.0035 |
298.15 | 0.6995 | 0.0037 |
298.15 | 0.7978 | 0.0038 |
298.15 | 0.8995 | 0.0037 |
298.15 | 1.0000 | 0.0033 |
303.15 | 0.0000 | 0.0016 |
303.15 | 0.0515 | 0.0017 |
303.15 | 0.0983 | 0.0018 |
303.15 | 0.1506 | 0.0019 |
303.15 | 0.2011 | 0.0020 |
303.15 | 0.2971 | 0.0023 |
303.15 | 0.4020 | 0.0025 |
303.15 | 0.4982 | 0.0028 |
303.15 | 0.6001 | 0.0030 |
303.15 | 0.6995 | 0.0032 |
303.15 | 0.7978 | 0.0032 |
303.15 | 0.8995 | 0.0031 |
303.15 | 1.0000 | 0.0028 |
Operational condition: Pressure, kPa = 101.325 (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 | 0.0515 | 0.0022 |
293.15 | 0.0983 | 0.0024 |
293.15 | 0.1506 | 0.0025 |
293.15 | 0.2011 | 0.0027 |
293.15 | 0.2971 | 0.0031 |
293.15 | 0.4020 | 0.0035 |
293.15 | 0.4982 | 0.0038 |
293.15 | 0.6001 | 0.0041 |
293.15 | 0.6995 | 0.0044 |
293.15 | 0.7978 | 0.0045 |
293.15 | 0.8995 | 0.0044 |
293.15 | 1.0000 | 0.0040 |
298.15 | 0.0000 | 0.0018 |
298.15 | 0.0515 | 0.0019 |
298.15 | 0.0983 | 0.0020 |
298.15 | 0.1506 | 0.0022 |
298.15 | 0.2011 | 0.0024 |
298.15 | 0.2971 | 0.0026 |
298.15 | 0.4020 | 0.0030 |
298.15 | 0.4982 | 0.0032 |
298.15 | 0.6001 | 0.0035 |
298.15 | 0.6995 | 0.0037 |
298.15 | 0.7978 | 0.0038 |
298.15 | 0.8995 | 0.0037 |
298.15 | 1.0000 | 0.0033 |
303.15 | 0.0000 | 0.0016 |
303.15 | 0.0515 | 0.0017 |
303.15 | 0.0983 | 0.0018 |
303.15 | 0.1506 | 0.0019 |
303.15 | 0.2011 | 0.0020 |
303.15 | 0.2971 | 0.0023 |
303.15 | 0.4020 | 0.0025 |
303.15 | 0.4982 | 0.0028 |
303.15 | 0.6001 | 0.0030 |
303.15 | 0.6995 | 0.0032 |
303.15 | 0.7978 | 0.0032 |
303.15 | 0.8995 | 0.0031 |
303.15 | 1.0000 | 0.0028 |
Operational condition: Pressure, kPa = 101.325 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0000 | 903.78 |
293.15 | 0.0515 | 901.11 |
293.15 | 0.0983 | 898.38 |
293.15 | 0.1506 | 895.07 |
293.15 | 0.2011 | 891.66 |
293.15 | 0.2971 | 884.72 |
293.15 | 0.4020 | 876.51 |
293.15 | 0.4982 | 868.29 |
293.15 | 0.6001 | 858.58 |
293.15 | 0.6995 | 847.72 |
293.15 | 0.7978 | 835.15 |
293.15 | 0.8995 | 819.74 |
293.15 | 1.0000 | 801.58 |
298.15 | 0.0000 | 899.8 |
298.15 | 0.0515 | 897.16 |
298.15 | 0.0983 | 894.46 |
298.15 | 0.1506 | 891.19 |
298.15 | 0.2011 | 887.82 |
298.15 | 0.2971 | 880.97 |
298.15 | 0.4020 | 872.85 |
298.15 | 0.4982 | 864.71 |
298.15 | 0.6001 | 855.07 |
298.15 | 0.6995 | 844.25 |
298.15 | 0.7978 | 831.71 |
298.15 | 0.8995 | 816.28 |
298.15 | 1.0000 | 798.09 |
303.15 | 0.0000 | 894.55 |
303.15 | 0.0515 | 891.98 |
303.15 | 0.0983 | 889.35 |
303.15 | 0.1506 | 886.16 |
303.15 | 0.2011 | 882.88 |
303.15 | 0.2971 | 876.18 |
303.15 | 0.4020 | 868.24 |
303.15 | 0.4982 | 860.24 |
303.15 | 0.6001 | 850.74 |
303.15 | 0.6995 | 840.04 |
303.15 | 0.7978 | 827.6 |
303.15 | 0.8995 | 812.25 |
303.15 | 1.0000 | 794.09 |
Operational condition: Pressure, kPa = 101.325 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0000 | 903.78 |
293.15 | 0.0515 | 901.11 |
293.15 | 0.0983 | 898.38 |
293.15 | 0.1506 | 895.07 |
293.15 | 0.2011 | 891.66 |
293.15 | 0.2971 | 884.72 |
293.15 | 0.4020 | 876.51 |
293.15 | 0.4982 | 868.29 |
293.15 | 0.6001 | 858.58 |
293.15 | 0.6995 | 847.72 |
293.15 | 0.7978 | 835.15 |
293.15 | 0.8995 | 819.74 |
293.15 | 1.0000 | 801.58 |
298.15 | 0.0000 | 899.8 |
298.15 | 0.0515 | 897.16 |
298.15 | 0.0983 | 894.46 |
298.15 | 0.1506 | 891.19 |
298.15 | 0.2011 | 887.82 |
298.15 | 0.2971 | 880.97 |
298.15 | 0.4020 | 872.85 |
298.15 | 0.4982 | 864.71 |
298.15 | 0.6001 | 855.07 |
298.15 | 0.6995 | 844.25 |
298.15 | 0.7978 | 831.71 |
298.15 | 0.8995 | 816.28 |
298.15 | 1.0000 | 798.09 |
303.15 | 0.0000 | 894.55 |
303.15 | 0.0515 | 891.98 |
303.15 | 0.0983 | 889.35 |
303.15 | 0.1506 | 886.16 |
303.15 | 0.2011 | 882.88 |
303.15 | 0.2971 | 876.18 |
303.15 | 0.4020 | 868.24 |
303.15 | 0.4982 | 860.24 |
303.15 | 0.6001 | 850.74 |
303.15 | 0.6995 | 840.04 |
303.15 | 0.7978 | 827.6 |
303.15 | 0.8995 | 812.25 |
303.15 | 1.0000 | 794.09 |