Datasets
-
Henry's Law constant (mole fraction scale), kPa (2)
-
η - Viscosity, Pa*s (2)
-
ρl - Mass density, kg/m3 (2)
Henry's Law constant (mole fraction scale), kPa of Ethanol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Henry's Law constant (mole fraction scale), kPa of Ethanol (1) - Liquid |
293.20 |
0.0000 |
28.0 |
Henry's Law constant (mole fraction scale), kPa of Ethanol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Henry's Law constant (mole fraction scale), kPa of Ethanol (1) - Liquid |
293.20 |
0.0000 |
28.0 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
283.15 |
0.0000 |
0.0135 |
293.15 |
0.0000 |
0.0090 |
298.15 |
0.0000 |
0.0074 |
303.15 |
0.0000 |
0.0063 |
313.15 |
0.0000 |
0.0046 |
283.15 |
0.1001 |
0.0116 |
293.15 |
0.1001 |
0.0080 |
298.15 |
0.1001 |
0.0066 |
303.15 |
0.1001 |
0.0057 |
313.15 |
0.1001 |
0.0042 |
293.15 |
0.2001 |
0.0070 |
283.15 |
0.2001 |
0.0100 |
298.15 |
0.2001 |
0.0058 |
303.15 |
0.2001 |
0.0050 |
313.15 |
0.2001 |
0.0037 |
298.15 |
0.3003 |
0.0051 |
283.15 |
0.3003 |
0.0084 |
303.15 |
0.3003 |
0.0044 |
293.15 |
0.3003 |
0.0060 |
313.15 |
0.3003 |
0.0033 |
293.15 |
0.3999 |
0.0050 |
298.15 |
0.3999 |
0.0044 |
303.15 |
0.3999 |
0.0037 |
283.15 |
0.3999 |
0.0069 |
313.15 |
0.3999 |
0.0029 |
298.15 |
0.5004 |
0.0037 |
293.15 |
0.5004 |
0.0042 |
283.15 |
0.5004 |
0.0056 |
303.15 |
0.5004 |
0.0032 |
313.15 |
0.5004 |
0.0025 |
293.15 |
0.6006 |
0.0034 |
298.15 |
0.6006 |
0.0030 |
303.15 |
0.6006 |
0.0027 |
283.15 |
0.6006 |
0.0045 |
313.15 |
0.6006 |
0.0021 |
303.15 |
0.7000 |
0.0022 |
283.15 |
0.7000 |
0.0035 |
293.15 |
0.7000 |
0.0027 |
298.15 |
0.7000 |
0.0024 |
313.15 |
0.7000 |
0.0018 |
303.15 |
0.7999 |
0.0017 |
298.15 |
0.7999 |
0.0020 |
293.15 |
0.7999 |
0.0021 |
283.15 |
0.7999 |
0.0027 |
313.15 |
0.7999 |
0.0014 |
283.15 |
0.8998 |
0.0020 |
293.15 |
0.8998 |
0.0016 |
298.15 |
0.8998 |
0.0015 |
303.15 |
0.8998 |
0.0013 |
313.15 |
0.8998 |
0.0011 |
303.15 |
1.0000 |
0.0010 |
298.15 |
1.0000 |
0.0011 |
283.15 |
1.0000 |
0.0015 |
293.15 |
1.0000 |
0.0012 |
313.15 |
1.0000 |
0.0008 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
283.15 |
0.0000 |
0.0135 |
293.15 |
0.0000 |
0.0090 |
298.15 |
0.0000 |
0.0074 |
303.15 |
0.0000 |
0.0063 |
313.15 |
0.0000 |
0.0046 |
283.15 |
0.1001 |
0.0116 |
293.15 |
0.1001 |
0.0080 |
298.15 |
0.1001 |
0.0066 |
303.15 |
0.1001 |
0.0057 |
313.15 |
0.1001 |
0.0042 |
293.15 |
0.2001 |
0.0070 |
283.15 |
0.2001 |
0.0100 |
298.15 |
0.2001 |
0.0058 |
303.15 |
0.2001 |
0.0050 |
313.15 |
0.2001 |
0.0037 |
298.15 |
0.3003 |
0.0051 |
283.15 |
0.3003 |
0.0084 |
303.15 |
0.3003 |
0.0044 |
293.15 |
0.3003 |
0.0060 |
313.15 |
0.3003 |
0.0033 |
293.15 |
0.3999 |
0.0050 |
298.15 |
0.3999 |
0.0044 |
303.15 |
0.3999 |
0.0037 |
283.15 |
0.3999 |
0.0069 |
313.15 |
0.3999 |
0.0029 |
298.15 |
0.5004 |
0.0037 |
293.15 |
0.5004 |
0.0042 |
283.15 |
0.5004 |
0.0056 |
303.15 |
0.5004 |
0.0032 |
313.15 |
0.5004 |
0.0025 |
293.15 |
0.6006 |
0.0034 |
298.15 |
0.6006 |
0.0030 |
303.15 |
0.6006 |
0.0027 |
283.15 |
0.6006 |
0.0045 |
313.15 |
0.6006 |
0.0021 |
303.15 |
0.7000 |
0.0022 |
283.15 |
0.7000 |
0.0035 |
293.15 |
0.7000 |
0.0027 |
298.15 |
0.7000 |
0.0024 |
313.15 |
0.7000 |
0.0018 |
303.15 |
0.7999 |
0.0017 |
298.15 |
0.7999 |
0.0020 |
293.15 |
0.7999 |
0.0021 |
283.15 |
0.7999 |
0.0027 |
313.15 |
0.7999 |
0.0014 |
283.15 |
0.8998 |
0.0020 |
293.15 |
0.8998 |
0.0016 |
298.15 |
0.8998 |
0.0015 |
303.15 |
0.8998 |
0.0013 |
313.15 |
0.8998 |
0.0011 |
303.15 |
1.0000 |
0.0010 |
298.15 |
1.0000 |
0.0011 |
283.15 |
1.0000 |
0.0015 |
293.15 |
1.0000 |
0.0012 |
313.15 |
1.0000 |
0.0008 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.0000 |
832.1 |
293.15 |
0.0000 |
825.2 |
298.15 |
0.0000 |
821.9 |
303.15 |
0.0000 |
818.4 |
313.15 |
0.0000 |
811.4 |
283.15 |
0.1001 |
831.8 |
293.15 |
0.1001 |
824.1 |
298.15 |
0.1001 |
821.3 |
303.15 |
0.1001 |
817.8 |
313.15 |
0.1001 |
810.7 |
293.15 |
0.2001 |
822.4 |
283.15 |
0.2001 |
829.4 |
298.15 |
0.2001 |
818.9 |
303.15 |
0.2001 |
815.4 |
313.15 |
0.2001 |
808.3 |
298.15 |
0.3003 |
817.0 |
283.15 |
0.3003 |
827.3 |
303.15 |
0.3003 |
813.4 |
293.15 |
0.3003 |
820.6 |
313.15 |
0.3003 |
806.2 |
293.15 |
0.3999 |
818.2 |
298.15 |
0.3999 |
814.7 |
303.15 |
0.3999 |
811.5 |
283.15 |
0.3999 |
825.4 |
313.15 |
0.3999 |
803.7 |
298.15 |
0.5004 |
811.7 |
293.15 |
0.5004 |
815.3 |
283.15 |
0.5004 |
822.6 |
303.15 |
0.5004 |
808.1 |
313.15 |
0.5004 |
800.7 |
293.15 |
0.6006 |
812.7 |
298.15 |
0.6006 |
809.0 |
303.15 |
0.6006 |
805.2 |
283.15 |
0.6006 |
820.1 |
313.15 |
0.6006 |
797.7 |
303.15 |
0.7000 |
801.7 |
283.15 |
0.7000 |
816.8 |
293.15 |
0.7000 |
809.3 |
298.15 |
0.7000 |
805.4 |
313.15 |
0.7000 |
793.9 |
303.15 |
0.7999 |
796.1 |
298.15 |
0.7999 |
800.0 |
293.15 |
0.7999 |
803.9 |
283.15 |
0.7999 |
811.7 |
313.15 |
0.7999 |
788.1 |
283.15 |
0.9001 |
805.0 |
293.15 |
0.9001 |
796.8 |
303.15 |
0.9001 |
788.6 |
298.15 |
0.9001 |
792.7 |
313.15 |
0.9001 |
780.4 |
303.15 |
1.0000 |
781.1 |
298.15 |
1.0000 |
785.2 |
283.15 |
1.0000 |
798.0 |
293.15 |
1.0000 |
789.5 |
313.15 |
1.0000 |
772.3 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.0000 |
832.1 |
293.15 |
0.0000 |
825.2 |
298.15 |
0.0000 |
821.9 |
303.15 |
0.0000 |
818.4 |
313.15 |
0.0000 |
811.4 |
283.15 |
0.1001 |
831.8 |
293.15 |
0.1001 |
824.1 |
298.15 |
0.1001 |
821.3 |
303.15 |
0.1001 |
817.8 |
313.15 |
0.1001 |
810.7 |
293.15 |
0.2001 |
822.4 |
283.15 |
0.2001 |
829.4 |
298.15 |
0.2001 |
818.9 |
303.15 |
0.2001 |
815.4 |
313.15 |
0.2001 |
808.3 |
298.15 |
0.3003 |
817.0 |
283.15 |
0.3003 |
827.3 |
303.15 |
0.3003 |
813.4 |
293.15 |
0.3003 |
820.6 |
313.15 |
0.3003 |
806.2 |
293.15 |
0.3999 |
818.2 |
298.15 |
0.3999 |
814.7 |
303.15 |
0.3999 |
811.5 |
283.15 |
0.3999 |
825.4 |
313.15 |
0.3999 |
803.7 |
298.15 |
0.5004 |
811.7 |
293.15 |
0.5004 |
815.3 |
283.15 |
0.5004 |
822.6 |
303.15 |
0.5004 |
808.1 |
313.15 |
0.5004 |
800.7 |
293.15 |
0.6006 |
812.7 |
298.15 |
0.6006 |
809.0 |
303.15 |
0.6006 |
805.2 |
283.15 |
0.6006 |
820.1 |
313.15 |
0.6006 |
797.7 |
303.15 |
0.7000 |
801.7 |
283.15 |
0.7000 |
816.8 |
293.15 |
0.7000 |
809.3 |
298.15 |
0.7000 |
805.4 |
313.15 |
0.7000 |
793.9 |
303.15 |
0.7999 |
796.1 |
298.15 |
0.7999 |
800.0 |
293.15 |
0.7999 |
803.9 |
283.15 |
0.7999 |
811.7 |
313.15 |
0.7999 |
788.1 |
283.15 |
0.9001 |
805.0 |
293.15 |
0.9001 |
796.8 |
303.15 |
0.9001 |
788.6 |
298.15 |
0.9001 |
792.7 |
313.15 |
0.9001 |
780.4 |
303.15 |
1.0000 |
781.1 |
298.15 |
1.0000 |
785.2 |
283.15 |
1.0000 |
798.0 |
293.15 |
1.0000 |
789.5 |
313.15 |
1.0000 |
772.3 |
Sources