Operational conditions:
| Mole fraction of Propane, 1-nitro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.6886 | 1.83 |
| 0.6918 | 1.831 |
| 0.6924 | 1.831 |
| 0.7024 | 1.806 |
| 0.7032 | 1.814 |
| 0.7058 | 1.787 |
| 0.7083 | 1.778 |
| 0.7117 | 1.762 |
Operational condition: Mole fraction = 0.7 (Liquid mixture 1)
| Pressure, kPa - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 485.00 | 300.81 |
| 831.00 | 300.86 |
| 1157.00 | 300.90 |
| 1552.00 | 300.96 |
| 2151.00 | 301.04 |
| 2513.00 | 301.09 |
| 3929.00 | 301.28 |
| 4677.00 | 301.38 |
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Propane, 1-nitro- (1) - Liquid | Pressure, kPa - Liquid | Excess molar volume, m3/mol - Liquid |
| 0.7089 | 101.00 | 7.7300e-07 |
Note: These property values are available through the Cheméo API. A free account gives you an access key.