Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Acetylacetone (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 298.15 | 0.0997 | -0.0095 |
| 298.15 | 0.2003 | -0.0220 |
| 298.15 | 0.2503 | -0.0278 |
| 298.15 | 0.3006 | -0.0318 |
| 298.15 | 0.3498 | -0.0347 |
| 298.15 | 0.4005 | -0.0372 |
| 298.15 | 0.4502 | -0.0362 |
| 298.15 | 0.5001 | -0.0356 |
| 298.15 | 0.5503 | -0.0339 |
| 298.15 | 0.5994 | -0.0315 |
| 298.15 | 0.6499 | -0.0283 |
| 298.15 | 0.6995 | -0.0241 |
| 298.15 | 0.7992 | -0.0148 |
| 298.15 | 0.8998 | -0.0064 |
| 313.15 | 0.0997 | -0.0231 |
| 313.15 | 0.2003 | -0.0471 |
| 313.15 | 0.2503 | -0.0601 |
| 313.15 | 0.3006 | -0.0698 |
| 313.15 | 0.3498 | -0.0758 |
| 313.15 | 0.4005 | -0.0790 |
| 313.15 | 0.4502 | -0.0800 |
| 313.15 | 0.5001 | -0.0787 |
| 313.15 | 0.5503 | -0.0759 |
| 313.15 | 0.5994 | -0.0719 |
| 313.15 | 0.6499 | -0.0664 |
| 313.15 | 0.6995 | -0.0598 |
| 313.15 | 0.7992 | -0.0427 |
| 313.15 | 0.8998 | -0.0236 |
| 328.15 | 0.0997 | -0.0335 |
| 328.15 | 0.2003 | -0.0663 |
| 328.15 | 0.2503 | -0.0828 |
| 328.15 | 0.3006 | -0.0970 |
| 328.15 | 0.3498 | -0.1073 |
| 328.15 | 0.4005 | -0.1125 |
| 328.15 | 0.4502 | -0.1149 |
| 328.15 | 0.5001 | -0.1152 |
| 328.15 | 0.5503 | -0.1124 |
| 328.15 | 0.5994 | -0.1071 |
| 328.15 | 0.6499 | -0.0991 |
| 328.15 | 0.6995 | -0.0881 |
| 328.15 | 0.7992 | -0.0583 |
| 328.15 | 0.8998 | -0.0243 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Acetylacetone (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 298.15 | 0.0997 | -0.0095 |
| 298.15 | 0.2003 | -0.0220 |
| 298.15 | 0.2503 | -0.0278 |
| 298.15 | 0.3006 | -0.0318 |
| 298.15 | 0.3498 | -0.0347 |
| 298.15 | 0.4005 | -0.0372 |
| 298.15 | 0.4502 | -0.0362 |
| 298.15 | 0.5001 | -0.0356 |
| 298.15 | 0.5503 | -0.0339 |
| 298.15 | 0.5994 | -0.0315 |
| 298.15 | 0.6499 | -0.0283 |
| 298.15 | 0.6995 | -0.0241 |
| 298.15 | 0.7992 | -0.0148 |
| 298.15 | 0.8998 | -0.0064 |
| 313.15 | 0.0997 | -0.0231 |
| 313.15 | 0.2003 | -0.0471 |
| 313.15 | 0.2503 | -0.0601 |
| 313.15 | 0.3006 | -0.0698 |
| 313.15 | 0.3498 | -0.0758 |
| 313.15 | 0.4005 | -0.0790 |
| 313.15 | 0.4502 | -0.0800 |
| 313.15 | 0.5001 | -0.0787 |
| 313.15 | 0.5503 | -0.0759 |
| 313.15 | 0.5994 | -0.0719 |
| 313.15 | 0.6499 | -0.0664 |
| 313.15 | 0.6995 | -0.0598 |
| 313.15 | 0.7992 | -0.0427 |
| 313.15 | 0.8998 | -0.0236 |
| 328.15 | 0.0997 | -0.0335 |
| 328.15 | 0.2003 | -0.0663 |
| 328.15 | 0.2503 | -0.0828 |
| 328.15 | 0.3006 | -0.0970 |
| 328.15 | 0.3498 | -0.1073 |
| 328.15 | 0.4005 | -0.1125 |
| 328.15 | 0.4502 | -0.1149 |
| 328.15 | 0.5001 | -0.1152 |
| 328.15 | 0.5503 | -0.1124 |
| 328.15 | 0.5994 | -0.1071 |
| 328.15 | 0.6499 | -0.0991 |
| 328.15 | 0.6995 | -0.0881 |
| 328.15 | 0.7992 | -0.0583 |
| 328.15 | 0.8998 | -0.0243 |