Operational conditions:
| Mole fraction of Di-n-propyl ether (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0500 | 0.0379 |
| 0.1000 | 0.0681 |
| 0.1500 | 0.0897 |
| 0.2000 | 0.1094 |
| 0.2499 | 0.1246 |
| 0.2998 | 0.1371 |
| 0.3499 | 0.1459 |
| 0.3998 | 0.1508 |
| 0.4501 | 0.1547 |
| 0.4995 | 0.1547 |
| 0.5497 | 0.1511 |
| 0.6001 | 0.1451 |
| 0.6500 | 0.1358 |
| 0.7001 | 0.1248 |
| 0.7503 | 0.1110 |
| 0.8001 | 0.0945 |
| 0.8500 | 0.0748 |
| 0.9000 | 0.0532 |
| 0.9500 | 0.0283 |
Operational conditions:
| Mole fraction of Di-n-propyl ether (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0500 | 0.0379 |
| 0.1000 | 0.0681 |
| 0.1500 | 0.0897 |
| 0.2000 | 0.1094 |
| 0.2499 | 0.1246 |
| 0.2998 | 0.1371 |
| 0.3499 | 0.1459 |
| 0.3998 | 0.1508 |
| 0.4501 | 0.1547 |
| 0.4995 | 0.1547 |
| 0.5497 | 0.1511 |
| 0.6001 | 0.1451 |
| 0.6500 | 0.1358 |
| 0.7001 | 0.1248 |
| 0.7503 | 0.1110 |
| 0.8001 | 0.0945 |
| 0.8500 | 0.0748 |
| 0.9000 | 0.0532 |
| 0.9500 | 0.0283 |