Operational conditions:
| Mole fraction of Di-n-propyl ether (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0500 | 0.0354 |
| 0.1000 | 0.0636 |
| 0.1500 | 0.0860 |
| 0.2001 | 0.1054 |
| 0.2500 | 0.1205 |
| 0.3001 | 0.1342 |
| 0.3499 | 0.1446 |
| 0.4000 | 0.1525 |
| 0.4498 | 0.1564 |
| 0.4998 | 0.1573 |
| 0.4998 | 0.1576 |
| 0.5500 | 0.1555 |
| 0.5999 | 0.1503 |
| 0.6501 | 0.1424 |
| 0.7000 | 0.1315 |
| 0.7502 | 0.1170 |
| 0.8000 | 0.1014 |
| 0.8500 | 0.0809 |
| 0.9000 | 0.0579 |
| 0.9500 | 0.0314 |
Operational conditions:
| Mole fraction of Di-n-propyl ether (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0500 | 0.0354 |
| 0.1000 | 0.0636 |
| 0.1500 | 0.0860 |
| 0.2001 | 0.1054 |
| 0.2500 | 0.1205 |
| 0.3001 | 0.1342 |
| 0.3499 | 0.1446 |
| 0.4000 | 0.1525 |
| 0.4498 | 0.1564 |
| 0.4998 | 0.1573 |
| 0.4998 | 0.1576 |
| 0.5500 | 0.1555 |
| 0.5999 | 0.1503 |
| 0.6501 | 0.1424 |
| 0.7000 | 0.1315 |
| 0.7502 | 0.1170 |
| 0.8000 | 0.1014 |
| 0.8500 | 0.0809 |
| 0.9000 | 0.0579 |
| 0.9500 | 0.0314 |