Operational conditions:
| Mole fraction of Propane, 1-nitro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.5521 | 1.716 |
| 0.5615 | 1.744 |
| 0.5661 | 1.748 |
| 0.5664 | 1.748 |
| 0.5746 | 1.745 |
| 0.5825 | 1.744 |
| 0.5915 | 1.738 |
| 0.5915 | 1.726 |
Operational conditions:
| Mole fraction of Propane, 1-nitro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.5521 | 1.716 |
| 0.5615 | 1.744 |
| 0.5661 | 1.748 |
| 0.5664 | 1.748 |
| 0.5746 | 1.745 |
| 0.5825 | 1.744 |
| 0.5915 | 1.738 |
| 0.5915 | 1.726 |
Operational condition: Mole fraction = 0.571 (Liquid mixture 1)
| Pressure, kPa - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 316.00 | 281.69 |
| 605.00 | 281.71 |
| 811.00 | 281.73 |
| 1198.00 | 281.78 |
| 1424.00 | 281.80 |
| 1897.00 | 281.84 |
| 2505.00 | 281.89 |
| 3121.00 | 281.96 |
| 4226.00 | 282.07 |
Operational condition: Mole fraction = 0.571 (Liquid mixture 1)
| Pressure, kPa - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 316.00 | 281.69 |
| 605.00 | 281.71 |
| 811.00 | 281.73 |
| 1198.00 | 281.78 |
| 1424.00 | 281.80 |
| 1897.00 | 281.84 |
| 2505.00 | 281.89 |
| 3121.00 | 281.96 |
| 4226.00 | 282.07 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of Propane, 1-nitro- (1) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.5803 | 5.5200e-07 |
| 0.5901 | 5.5000e-07 |
| 0.6003 | 5.4700e-07 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of Propane, 1-nitro- (1) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.5803 | 5.5200e-07 |
| 0.5901 | 5.5000e-07 |
| 0.6003 | 5.4700e-07 |