Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of 1-Hexanol (2) - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
0.0000 | 298.15 | 0.0454 |
0.0000 | 303.15 | 0.0340 |
0.0000 | 308.15 | 0.0263 |
0.0771 | 298.15 | 0.0333 |
0.0771 | 303.15 | 0.0243 |
0.0771 | 308.15 | 0.0201 |
0.1213 | 298.15 | 0.0284 |
0.1213 | 303.15 | 0.0208 |
0.1213 | 308.15 | 0.0173 |
0.2425 | 298.15 | 0.0186 |
0.2425 | 303.15 | 0.0139 |
0.2425 | 308.15 | 0.0120 |
0.3311 | 298.15 | 0.0144 |
0.3311 | 303.15 | 0.0113 |
0.3311 | 308.15 | 0.0096 |
0.5225 | 298.15 | 0.0095 |
0.5225 | 303.15 | 0.0081 |
0.5225 | 308.15 | 0.0064 |
0.5377 | 298.15 | 0.0091 |
0.5377 | 303.15 | 0.0078 |
0.5377 | 308.15 | 0.0063 |
0.6309 | 298.15 | 0.0076 |
0.6309 | 303.15 | 0.0067 |
0.6309 | 308.15 | 0.0053 |
0.7444 | 298.15 | 0.0063 |
0.7444 | 303.15 | 0.0052 |
0.7444 | 308.15 | 0.0045 |
0.8611 | 298.15 | 0.0053 |
0.8611 | 303.15 | 0.0046 |
0.8611 | 308.15 | 0.0039 |
1.0000 | 298.15 | 0.0046 |
1.0000 | 303.15 | 0.0040 |
1.0000 | 308.15 | 0.0035 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of 1-Hexanol (2) - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
0.0000 | 298.15 | 0.0454 |
0.0000 | 303.15 | 0.0340 |
0.0000 | 308.15 | 0.0263 |
0.0771 | 298.15 | 0.0333 |
0.0771 | 303.15 | 0.0243 |
0.0771 | 308.15 | 0.0201 |
0.1213 | 298.15 | 0.0284 |
0.1213 | 303.15 | 0.0208 |
0.1213 | 308.15 | 0.0173 |
0.2425 | 298.15 | 0.0186 |
0.2425 | 303.15 | 0.0139 |
0.2425 | 308.15 | 0.0120 |
0.3311 | 298.15 | 0.0144 |
0.3311 | 303.15 | 0.0113 |
0.3311 | 308.15 | 0.0096 |
0.5225 | 298.15 | 0.0095 |
0.5225 | 303.15 | 0.0081 |
0.5225 | 308.15 | 0.0064 |
0.5377 | 298.15 | 0.0091 |
0.5377 | 303.15 | 0.0078 |
0.5377 | 308.15 | 0.0063 |
0.6309 | 298.15 | 0.0076 |
0.6309 | 303.15 | 0.0067 |
0.6309 | 308.15 | 0.0053 |
0.7444 | 298.15 | 0.0063 |
0.7444 | 303.15 | 0.0052 |
0.7444 | 308.15 | 0.0045 |
0.8611 | 298.15 | 0.0053 |
0.8611 | 303.15 | 0.0046 |
0.8611 | 308.15 | 0.0039 |
1.0000 | 298.15 | 0.0046 |
1.0000 | 303.15 | 0.0040 |
1.0000 | 308.15 | 0.0035 |
Operational conditions:
Mole fraction of Propylene Glycol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0905 | 0.3487 |
0.1929 | 0.5773 |
0.2872 | 0.6911 |
0.3828 | 0.7465 |
0.4778 | 0.7564 |
0.5711 | 0.7235 |
0.6718 | 0.6564 |
0.7021 | 0.6117 |
0.7996 | 0.4848 |
0.9040 | 0.2816 |
Operational conditions:
Mole fraction of Propylene Glycol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0905 | 0.3487 |
0.1929 | 0.5773 |
0.2872 | 0.6911 |
0.3828 | 0.7465 |
0.4778 | 0.7564 |
0.5711 | 0.7235 |
0.6718 | 0.6564 |
0.7021 | 0.6117 |
0.7996 | 0.4848 |
0.9040 | 0.2816 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Propylene Glycol (1) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0000 | 818.749 |
293.15 | 0.1014 | 831.496 |
293.15 | 0.1998 | 845.231 |
293.15 | 0.2999 | 860.667 |
293.15 | 0.4003 | 877.818 |
293.15 | 0.4939 | 895.533 |
293.15 | 0.5996 | 917.945 |
293.15 | 0.6965 | 941.028 |
293.15 | 0.7989 | 968.795 |
293.15 | 0.9005 | 1000.458 |
293.15 | 1.0000 | 1036.209 |
298.15 | 0.0000 | 815.188 |
298.15 | 0.1014 | 827.881 |
298.15 | 0.1998 | 841.574 |
298.15 | 0.2999 | 856.979 |
298.15 | 0.4003 | 874.105 |
298.15 | 0.4939 | 891.801 |
298.15 | 0.5996 | 914.203 |
298.15 | 0.6965 | 937.285 |
298.15 | 0.7989 | 965.064 |
298.15 | 0.9005 | 996.753 |
298.15 | 1.0000 | 1032.548 |
303.15 | 0.0000 | 811.6 |
303.15 | 0.1014 | 824.235 |
303.15 | 0.1998 | 837.887 |
303.15 | 0.2999 | 853.262 |
303.15 | 0.4003 | 870.363 |
303.15 | 0.4939 | 888.041 |
303.15 | 0.5996 | 910.432 |
303.15 | 0.6965 | 933.51 |
303.15 | 0.7989 | 961.302 |
303.15 | 0.9005 | 993.003 |
303.15 | 1.0000 | 1028.837 |
308.15 | 0.0000 | 807.984 |
308.15 | 0.1014 | 820.566 |
308.15 | 0.1998 | 834.178 |
308.15 | 0.2999 | 849.521 |
308.15 | 0.4003 | 866.596 |
308.15 | 0.4939 | 884.256 |
308.15 | 0.5996 | 906.63 |
308.15 | 0.6965 | 929.702 |
308.15 | 0.7989 | 957.503 |
308.15 | 0.9005 | 989.222 |
308.15 | 1.0000 | 1025.088 |
313.15 | 0.0000 | 804.339 |
313.15 | 0.1014 | 816.869 |
313.15 | 0.1998 | 830.44 |
313.15 | 0.2999 | 845.751 |
313.15 | 0.4003 | 862.8 |
313.15 | 0.4939 | 880.441 |
313.15 | 0.5996 | 902.801 |
313.15 | 0.6965 | 925.868 |
313.15 | 0.7989 | 953.677 |
313.15 | 0.9005 | 985.406 |
313.15 | 1.0000 | 1021.309 |
318.15 | 0.0000 | 800.657 |
318.15 | 0.1014 | 813.142 |
318.15 | 0.1998 | 826.676 |
318.15 | 0.2999 | 841.952 |
318.15 | 0.4003 | 858.977 |
318.15 | 0.4939 | 876.599 |
318.15 | 0.5996 | 898.941 |
318.15 | 0.6965 | 922.002 |
318.15 | 0.7989 | 949.81 |
318.15 | 0.9005 | 981.555 |
318.15 | 1.0000 | 1017.488 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of 1-Hexanol (2) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
0.0000 | 298.15 | 1033.1 |
0.0000 | 303.15 | 1029.9 |
0.0000 | 308.15 | 1025.4 |
0.0771 | 298.15 | 1004.5 |
0.0771 | 303.15 | 1000.9 |
0.0771 | 308.15 | 996.1 |
0.1213 | 298.15 | 989.9 |
0.1213 | 303.15 | 986.2 |
0.1213 | 308.15 | 981.6 |
0.2425 | 298.15 | 953.6 |
0.2425 | 303.15 | 949.9 |
0.2425 | 308.15 | 945.8 |
0.3311 | 298.15 | 930.7 |
0.3311 | 303.15 | 927.0 |
0.3311 | 308.15 | 923.1 |
0.5225 | 298.15 | 888.7 |
0.5225 | 303.15 | 884.9 |
0.5225 | 308.15 | 881.3 |
0.5377 | 298.15 | 885.7 |
0.5377 | 303.15 | 881.9 |
0.5377 | 308.15 | 878.2 |
0.6309 | 298.15 | 868.9 |
0.6309 | 303.15 | 865.1 |
0.6309 | 308.15 | 861.5 |
0.7444 | 298.15 | 850.3 |
0.7444 | 303.15 | 846.4 |
0.7444 | 308.15 | 842.9 |
0.8611 | 298.15 | 833.3 |
0.8611 | 303.15 | 829.4 |
0.8611 | 308.15 | 826.0 |
1.0000 | 298.15 | 815.4 |
1.0000 | 303.15 | 811.5 |
1.0000 | 308.15 | 808.3 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Propylene Glycol (1) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0000 | 818.749 |
293.15 | 0.1014 | 831.496 |
293.15 | 0.1998 | 845.231 |
293.15 | 0.2999 | 860.667 |
293.15 | 0.4003 | 877.818 |
293.15 | 0.4939 | 895.533 |
293.15 | 0.5996 | 917.945 |
293.15 | 0.6965 | 941.028 |
293.15 | 0.7989 | 968.795 |
293.15 | 0.9005 | 1000.458 |
293.15 | 1.0000 | 1036.209 |
298.15 | 0.0000 | 815.188 |
298.15 | 0.1014 | 827.881 |
298.15 | 0.1998 | 841.574 |
298.15 | 0.2999 | 856.979 |
298.15 | 0.4003 | 874.105 |
298.15 | 0.4939 | 891.801 |
298.15 | 0.5996 | 914.203 |
298.15 | 0.6965 | 937.285 |
298.15 | 0.7989 | 965.064 |
298.15 | 0.9005 | 996.753 |
298.15 | 1.0000 | 1032.548 |
303.15 | 0.0000 | 811.6 |
303.15 | 0.1014 | 824.235 |
303.15 | 0.1998 | 837.887 |
303.15 | 0.2999 | 853.262 |
303.15 | 0.4003 | 870.363 |
303.15 | 0.4939 | 888.041 |
303.15 | 0.5996 | 910.432 |
303.15 | 0.6965 | 933.51 |
303.15 | 0.7989 | 961.302 |
303.15 | 0.9005 | 993.003 |
303.15 | 1.0000 | 1028.837 |
308.15 | 0.0000 | 807.984 |
308.15 | 0.1014 | 820.566 |
308.15 | 0.1998 | 834.178 |
308.15 | 0.2999 | 849.521 |
308.15 | 0.4003 | 866.596 |
308.15 | 0.4939 | 884.256 |
308.15 | 0.5996 | 906.63 |
308.15 | 0.6965 | 929.702 |
308.15 | 0.7989 | 957.503 |
308.15 | 0.9005 | 989.222 |
308.15 | 1.0000 | 1025.088 |
313.15 | 0.0000 | 804.339 |
313.15 | 0.1014 | 816.869 |
313.15 | 0.1998 | 830.44 |
313.15 | 0.2999 | 845.751 |
313.15 | 0.4003 | 862.8 |
313.15 | 0.4939 | 880.441 |
313.15 | 0.5996 | 902.801 |
313.15 | 0.6965 | 925.868 |
313.15 | 0.7989 | 953.677 |
313.15 | 0.9005 | 985.406 |
313.15 | 1.0000 | 1021.309 |
318.15 | 0.0000 | 800.657 |
318.15 | 0.1014 | 813.142 |
318.15 | 0.1998 | 826.676 |
318.15 | 0.2999 | 841.952 |
318.15 | 0.4003 | 858.977 |
318.15 | 0.4939 | 876.599 |
318.15 | 0.5996 | 898.941 |
318.15 | 0.6965 | 922.002 |
318.15 | 0.7989 | 949.81 |
318.15 | 0.9005 | 981.555 |
318.15 | 1.0000 | 1017.488 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of 1-Hexanol (2) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
0.0000 | 298.15 | 1033.1 |
0.0000 | 303.15 | 1029.9 |
0.0000 | 308.15 | 1025.4 |
0.0771 | 298.15 | 1004.5 |
0.0771 | 303.15 | 1000.9 |
0.0771 | 308.15 | 996.1 |
0.1213 | 298.15 | 989.9 |
0.1213 | 303.15 | 986.2 |
0.1213 | 308.15 | 981.6 |
0.2425 | 298.15 | 953.6 |
0.2425 | 303.15 | 949.9 |
0.2425 | 308.15 | 945.8 |
0.3311 | 298.15 | 930.7 |
0.3311 | 303.15 | 927.0 |
0.3311 | 308.15 | 923.1 |
0.5225 | 298.15 | 888.7 |
0.5225 | 303.15 | 884.9 |
0.5225 | 308.15 | 881.3 |
0.5377 | 298.15 | 885.7 |
0.5377 | 303.15 | 881.9 |
0.5377 | 308.15 | 878.2 |
0.6309 | 298.15 | 868.9 |
0.6309 | 303.15 | 865.1 |
0.6309 | 308.15 | 861.5 |
0.7444 | 298.15 | 850.3 |
0.7444 | 303.15 | 846.4 |
0.7444 | 308.15 | 842.9 |
0.8611 | 298.15 | 833.3 |
0.8611 | 303.15 | 829.4 |
0.8611 | 308.15 | 826.0 |
1.0000 | 298.15 | 815.4 |
1.0000 | 303.15 | 811.5 |
1.0000 | 308.15 | 808.3 |