Operational conditions:
| Mole fraction of Di-n-propyl ether (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0500 | 0.0022 |
| 0.1000 | 0.0043 |
| 0.1500 | 0.0059 |
| 0.2001 | 0.0073 |
| 0.2500 | 0.0086 |
| 0.3000 | 0.0096 |
| 0.3500 | 0.0103 |
| 0.3998 | 0.0109 |
| 0.4497 | 0.0115 |
| 0.4998 | 0.0118 |
| 0.5004 | 0.0118 |
| 0.5500 | 0.0119 |
| 0.6001 | 0.0118 |
| 0.6500 | 0.0113 |
| 0.6999 | 0.0106 |
| 0.7500 | 0.0095 |
| 0.8000 | 0.0082 |
| 0.8503 | 0.0067 |
| 0.9000 | 0.0046 |
| 0.9500 | 0.0026 |
Operational conditions:
| Mole fraction of Di-n-propyl ether (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0500 | 0.0022 |
| 0.1000 | 0.0043 |
| 0.1500 | 0.0059 |
| 0.2001 | 0.0073 |
| 0.2500 | 0.0086 |
| 0.3000 | 0.0096 |
| 0.3500 | 0.0103 |
| 0.3998 | 0.0109 |
| 0.4497 | 0.0115 |
| 0.4998 | 0.0118 |
| 0.5004 | 0.0118 |
| 0.5500 | 0.0119 |
| 0.6001 | 0.0118 |
| 0.6500 | 0.0113 |
| 0.6999 | 0.0106 |
| 0.7500 | 0.0095 |
| 0.8000 | 0.0082 |
| 0.8503 | 0.0067 |
| 0.9000 | 0.0046 |
| 0.9500 | 0.0026 |