Operational conditions:
| Mole fraction of Di-n-propyl ether (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0500 | 0.0523 |
| 0.1000 | 0.0969 |
| 0.1501 | 0.1361 |
| 0.2000 | 0.1682 |
| 0.2498 | 0.1959 |
| 0.2998 | 0.2169 |
| 0.3503 | 0.2328 |
| 0.3998 | 0.2426 |
| 0.4500 | 0.2473 |
| 0.4998 | 0.2483 |
| 0.4998 | 0.2486 |
| 0.5499 | 0.2446 |
| 0.5999 | 0.2363 |
| 0.6502 | 0.2237 |
| 0.7003 | 0.2062 |
| 0.7499 | 0.1845 |
| 0.7999 | 0.1594 |
| 0.8500 | 0.1277 |
| 0.9000 | 0.0905 |
| 0.9500 | 0.0481 |
Operational conditions:
| Mole fraction of Di-n-propyl ether (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0500 | 0.0523 |
| 0.1000 | 0.0969 |
| 0.1501 | 0.1361 |
| 0.2000 | 0.1682 |
| 0.2498 | 0.1959 |
| 0.2998 | 0.2169 |
| 0.3503 | 0.2328 |
| 0.3998 | 0.2426 |
| 0.4500 | 0.2473 |
| 0.4998 | 0.2483 |
| 0.4998 | 0.2486 |
| 0.5499 | 0.2446 |
| 0.5999 | 0.2363 |
| 0.6502 | 0.2237 |
| 0.7003 | 0.2062 |
| 0.7499 | 0.1845 |
| 0.7999 | 0.1594 |
| 0.8500 | 0.1277 |
| 0.9000 | 0.0905 |
| 0.9500 | 0.0481 |