Datasets
-
Activity coefficient (4)
-
Henry's Law constant (mole fraction scale), kPa (22)
-
Excess molar enthalpy (molar enthalpy (2)
-
ρl - Mass density, kg/m3 (2)
Activity coefficient of 2-Hexanone (1)
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 2-Hexanone (1) - Liquid |
| 278.15 |
257.0 |
| 288.15 |
331.0 |
| 298.15 |
384.0 |
| 308.15 |
422.0 |
| 318.15 |
471.0 |
| 328.15 |
456.0 |
Activity coefficient of 2-Hexanone (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 2-Hexanone (1) - Liquid |
| 297.85 |
319.0 |
| 298.15 |
265.0 |
Activity coefficient of 2-Hexanone (1)
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 2-Hexanone (1) - Liquid |
| 278.15 |
257.0 |
| 288.15 |
331.0 |
| 298.15 |
384.0 |
| 308.15 |
422.0 |
| 318.15 |
471.0 |
| 328.15 |
456.0 |
Activity coefficient of 2-Hexanone (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 2-Hexanone (1) - Liquid |
| 297.85 |
319.0 |
| 298.15 |
265.0 |
Henry's Law constant (mole fraction scale), kPa of 2-Hexanone (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of 2-Hexanone (1) - Liquid |
| 323.15 |
2462.2 |
| 333.15 |
3890.9 |
| 343.15 |
5866.7 |
| 353.15 |
9656.3 |
Mass fraction of 2-Hexanone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of 2-Hexanone (1) - Liquid mixture 2 |
| 298.20 |
0.9773 |
| 313.20 |
0.9732 |
Mass fraction of 2-Hexanone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of 2-Hexanone (1) - Liquid mixture 1 |
| 298.20 |
0.0158 |
| 313.20 |
0.0120 |
Mole fraction of 2-Hexanone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 2-Hexanone (1) - Liquid mixture 2 |
| 333.20 |
0.8530 |
| 353.20 |
0.8360 |
Mole fraction of 2-Hexanone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 2-Hexanone (1) - Liquid mixture 1 |
| 333.20 |
0.0020 |
| 353.20 |
0.0020 |
Mole fraction of 2-Hexanone (1)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 2 |
Temperature, K - Liquid mixture 2 |
Mole fraction of 2-Hexanone (1) - Liquid mixture 1 |
| 101.30 |
313.20 |
0.8672 |
Mole fraction of 2-Hexanone (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of 2-Hexanone (1) - Liquid mixture 2 |
| 313.20 |
101.30 |
0.0022 |
Henry's Law constant (mole fraction scale), kPa of 2-Hexanone (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of 2-Hexanone (1) - Liquid |
| 297.85 |
319.0 |
| 298.15 |
265.0 |
Henry's Law constant (molality scale), kPa*kg/mol of 2-Hexanone (1)
[ref]
Operational condition: Molality, mol/kg =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (molality scale), kPa*kg/mol of 2-Hexanone (1) - Liquid |
| 274.15 |
0.5514 |
| 294.65 |
4.8855 |
| 294.65 |
5.9131 |
| 296.15 |
7.0729 |
| 310.15 |
17.901 |
| 320.15 |
48.244 |
| 331.15 |
121.57 |
| 333.15 |
136.04 |
Mass fraction of 2-Hexanone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass fraction of 2-Hexanone (1) - Liquid mixture 1 |
| 298.15 |
0.9773 |
| 323.15 |
0.9709 |
Mass fraction of 2-Hexanone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass fraction of 2-Hexanone (1) - Liquid mixture 2 |
| 298.15 |
0.0158 |
| 323.15 |
0.0109 |
Henry's Law constant (mole fraction scale), kPa of 2-Hexanone (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of 2-Hexanone (1) - Liquid |
| 323.15 |
2462.2 |
| 333.15 |
3890.9 |
| 343.15 |
5866.7 |
| 353.15 |
9656.3 |
Mass fraction of 2-Hexanone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of 2-Hexanone (1) - Liquid mixture 2 |
| 298.20 |
0.9773 |
| 313.20 |
0.9732 |
Mass fraction of 2-Hexanone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of 2-Hexanone (1) - Liquid mixture 1 |
| 298.20 |
0.0158 |
| 313.20 |
0.0120 |
Mole fraction of 2-Hexanone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 2-Hexanone (1) - Liquid mixture 2 |
| 333.20 |
0.8530 |
| 353.20 |
0.8360 |
Mole fraction of 2-Hexanone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 2-Hexanone (1) - Liquid mixture 1 |
| 333.20 |
0.0020 |
| 353.20 |
0.0020 |
Mole fraction of 2-Hexanone (1)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 2 |
Temperature, K - Liquid mixture 2 |
Mole fraction of 2-Hexanone (1) - Liquid mixture 1 |
| 101.30 |
313.20 |
0.8672 |
Mole fraction of 2-Hexanone (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of 2-Hexanone (1) - Liquid mixture 2 |
| 313.20 |
101.30 |
0.0022 |
Henry's Law constant (mole fraction scale), kPa of 2-Hexanone (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of 2-Hexanone (1) - Liquid |
| 297.85 |
319.0 |
| 298.15 |
265.0 |
Henry's Law constant (molality scale), kPa*kg/mol of 2-Hexanone (1)
[ref]
Operational condition: Molality, mol/kg =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (molality scale), kPa*kg/mol of 2-Hexanone (1) - Liquid |
| 274.15 |
0.5514 |
| 294.65 |
4.8855 |
| 294.65 |
5.9131 |
| 296.15 |
7.0729 |
| 310.15 |
17.901 |
| 320.15 |
48.244 |
| 331.15 |
121.57 |
| 333.15 |
136.04 |
Mass fraction of 2-Hexanone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass fraction of 2-Hexanone (1) - Liquid mixture 1 |
| 298.15 |
0.9773 |
| 323.15 |
0.9709 |
Mass fraction of 2-Hexanone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass fraction of 2-Hexanone (1) - Liquid mixture 2 |
| 298.15 |
0.0158 |
| 323.15 |
0.0109 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
| Fixed |
Measured |
| Mole fraction of 2-Hexanone (1) - Liquid |
Temperature, K - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0017 |
288.15 |
-0.0210 |
| 0.0017 |
288.15 |
-0.0211 |
| 0.0014 |
288.15 |
-0.0177 |
| 0.0014 |
288.15 |
-0.0176 |
| 0.0012 |
288.15 |
-0.0143 |
| 0.0012 |
288.15 |
-0.0142 |
| 0.0009 |
288.15 |
-0.0107 |
| 0.0009 |
288.15 |
-0.0106 |
| 0.0017 |
298.15 |
-0.0163 |
| 0.0017 |
298.15 |
-0.0165 |
| 0.0014 |
298.15 |
-0.0138 |
| 0.0014 |
298.15 |
-0.0134 |
| 0.0012 |
298.15 |
-0.0110 |
| 0.0012 |
298.15 |
-0.0110 |
| 0.0009 |
298.15 |
-0.0083 |
| 0.0009 |
298.15 |
-0.0083 |
| 0.0017 |
308.15 |
-0.0114 |
| 0.0017 |
308.15 |
-0.0114 |
| 0.0014 |
308.15 |
-0.0095 |
| 0.0014 |
308.15 |
-0.0094 |
| 0.0012 |
308.15 |
-0.0075 |
| 0.0012 |
308.15 |
-0.0076 |
| 0.0009 |
308.15 |
-0.0058 |
| 0.0009 |
308.15 |
-0.0058 |
| 0.0017 |
318.15 |
-0.0068 |
| 0.0017 |
318.15 |
-0.0069 |
| 0.0017 |
318.15 |
-0.0067 |
| 0.0014 |
318.15 |
-0.0056 |
| 0.0014 |
318.15 |
-0.0055 |
| 0.0014 |
318.15 |
-0.0056 |
| 0.0012 |
318.15 |
-0.0047 |
| 0.0012 |
318.15 |
-0.0045 |
| 0.0012 |
318.15 |
-0.0046 |
| 0.0009 |
318.15 |
-0.0034 |
| 0.0009 |
318.15 |
-0.0034 |
| 0.0009 |
318.15 |
-0.0034 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
| Fixed |
Measured |
| Mole fraction of 2-Hexanone (1) - Liquid |
Temperature, K - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0017 |
288.15 |
-0.0210 |
| 0.0017 |
288.15 |
-0.0211 |
| 0.0014 |
288.15 |
-0.0177 |
| 0.0014 |
288.15 |
-0.0176 |
| 0.0012 |
288.15 |
-0.0143 |
| 0.0012 |
288.15 |
-0.0142 |
| 0.0009 |
288.15 |
-0.0107 |
| 0.0009 |
288.15 |
-0.0106 |
| 0.0017 |
298.15 |
-0.0163 |
| 0.0017 |
298.15 |
-0.0165 |
| 0.0014 |
298.15 |
-0.0138 |
| 0.0014 |
298.15 |
-0.0134 |
| 0.0012 |
298.15 |
-0.0110 |
| 0.0012 |
298.15 |
-0.0110 |
| 0.0009 |
298.15 |
-0.0083 |
| 0.0009 |
298.15 |
-0.0083 |
| 0.0017 |
308.15 |
-0.0114 |
| 0.0017 |
308.15 |
-0.0114 |
| 0.0014 |
308.15 |
-0.0095 |
| 0.0014 |
308.15 |
-0.0094 |
| 0.0012 |
308.15 |
-0.0075 |
| 0.0012 |
308.15 |
-0.0076 |
| 0.0009 |
308.15 |
-0.0058 |
| 0.0009 |
308.15 |
-0.0058 |
| 0.0017 |
318.15 |
-0.0068 |
| 0.0017 |
318.15 |
-0.0069 |
| 0.0017 |
318.15 |
-0.0067 |
| 0.0014 |
318.15 |
-0.0056 |
| 0.0014 |
318.15 |
-0.0055 |
| 0.0014 |
318.15 |
-0.0056 |
| 0.0012 |
318.15 |
-0.0047 |
| 0.0012 |
318.15 |
-0.0045 |
| 0.0012 |
318.15 |
-0.0046 |
| 0.0009 |
318.15 |
-0.0034 |
| 0.0009 |
318.15 |
-0.0034 |
| 0.0009 |
318.15 |
-0.0034 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
| Fixed |
Measured |
| Mole fraction of 2-Hexanone (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0017 |
288.15 |
997.852 |
| 0.0017 |
288.15 |
997.853 |
| 0.0014 |
288.15 |
998.054 |
| 0.0014 |
288.15 |
998.054 |
| 0.0012 |
288.15 |
998.248 |
| 0.0012 |
288.15 |
998.255 |
| 0.0009 |
288.15 |
998.466 |
| 0.0009 |
288.15 |
998.439 |
| 0.0017 |
298.15 |
995.681 |
| 0.0017 |
298.15 |
995.664 |
| 0.0014 |
298.15 |
995.903 |
| 0.0014 |
298.15 |
995.926 |
| 0.0012 |
298.15 |
996.137 |
| 0.0012 |
298.15 |
996.128 |
| 0.0009 |
298.15 |
996.364 |
| 0.0009 |
298.15 |
996.347 |
| 0.0017 |
308.15 |
992.573 |
| 0.0017 |
308.15 |
992.571 |
| 0.0014 |
308.15 |
992.84 |
| 0.0014 |
308.15 |
992.834 |
| 0.0012 |
308.15 |
993.074 |
| 0.0012 |
308.15 |
993.08 |
| 0.0009 |
308.15 |
993.309 |
| 0.0009 |
308.15 |
993.32 |
| 0.0017 |
318.15 |
988.651 |
| 0.0017 |
318.15 |
988.636 |
| 0.0017 |
318.15 |
988.678 |
| 0.0014 |
318.15 |
988.931 |
| 0.0014 |
318.15 |
988.956 |
| 0.0014 |
318.15 |
988.934 |
| 0.0012 |
318.15 |
989.168 |
| 0.0012 |
318.15 |
989.197 |
| 0.0012 |
318.15 |
989.173 |
| 0.0009 |
318.15 |
989.446 |
| 0.0009 |
318.15 |
989.455 |
| 0.0009 |
318.15 |
989.45 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
| Fixed |
Measured |
| Mole fraction of 2-Hexanone (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0017 |
288.15 |
997.852 |
| 0.0017 |
288.15 |
997.853 |
| 0.0014 |
288.15 |
998.054 |
| 0.0014 |
288.15 |
998.054 |
| 0.0012 |
288.15 |
998.248 |
| 0.0012 |
288.15 |
998.255 |
| 0.0009 |
288.15 |
998.466 |
| 0.0009 |
288.15 |
998.439 |
| 0.0017 |
298.15 |
995.681 |
| 0.0017 |
298.15 |
995.664 |
| 0.0014 |
298.15 |
995.903 |
| 0.0014 |
298.15 |
995.926 |
| 0.0012 |
298.15 |
996.137 |
| 0.0012 |
298.15 |
996.128 |
| 0.0009 |
298.15 |
996.364 |
| 0.0009 |
298.15 |
996.347 |
| 0.0017 |
308.15 |
992.573 |
| 0.0017 |
308.15 |
992.571 |
| 0.0014 |
308.15 |
992.84 |
| 0.0014 |
308.15 |
992.834 |
| 0.0012 |
308.15 |
993.074 |
| 0.0012 |
308.15 |
993.08 |
| 0.0009 |
308.15 |
993.309 |
| 0.0009 |
308.15 |
993.32 |
| 0.0017 |
318.15 |
988.651 |
| 0.0017 |
318.15 |
988.636 |
| 0.0017 |
318.15 |
988.678 |
| 0.0014 |
318.15 |
988.931 |
| 0.0014 |
318.15 |
988.956 |
| 0.0014 |
318.15 |
988.934 |
| 0.0012 |
318.15 |
989.168 |
| 0.0012 |
318.15 |
989.197 |
| 0.0012 |
318.15 |
989.173 |
| 0.0009 |
318.15 |
989.446 |
| 0.0009 |
318.15 |
989.455 |
| 0.0009 |
318.15 |
989.45 |
Sources