Operational conditions:
| Mole fraction of Benzene, nitro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1037 | 0.7067 |
| 0.2036 | 1.2038 |
| 0.3063 | 1.5222 |
| 0.4034 | 1.7126 |
| 0.4956 | 1.8093 |
| 0.4993 | 1.8081 |
| 0.5930 | 1.7987 |
| 0.6975 | 1.7059 |
| 0.7978 | 1.4697 |
| 0.9025 | 1.0121 |
Operational conditions:
| Mole fraction of Benzene, nitro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1037 | 0.7067 |
| 0.2036 | 1.2038 |
| 0.3063 | 1.5222 |
| 0.4034 | 1.7126 |
| 0.4956 | 1.8093 |
| 0.4993 | 1.8081 |
| 0.5930 | 1.7987 |
| 0.6975 | 1.7059 |
| 0.7978 | 1.4697 |
| 0.9025 | 1.0121 |
Operational condition: Pressure, kPa = 94.95 (Liquid)
| Mole fraction of 1-Propanol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 481.15 |
| 0.0853 | 429.75 |
| 0.1730 | 414.65 |
| 0.2332 | 407.75 |
| 0.2957 | 401.95 |
| 0.3721 | 395.95 |
| 0.4570 | 390.35 |
| 0.5231 | 386.55 |
| 0.5971 | 382.85 |
| 0.6605 | 379.95 |
| 0.7427 | 376.75 |
| 0.8202 | 373.95 |
| 0.8989 | 371.55 |
| 0.9506 | 370.05 |
| 1.0000 | 368.75 |
Operational condition: Pressure, kPa = 94.95 (Liquid)
| Mole fraction of 1-Propanol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 481.15 |
| 0.0853 | 429.75 |
| 0.1730 | 414.65 |
| 0.2332 | 407.75 |
| 0.2957 | 401.95 |
| 0.3721 | 395.95 |
| 0.4570 | 390.35 |
| 0.5231 | 386.55 |
| 0.5971 | 382.85 |
| 0.6605 | 379.95 |
| 0.7427 | 376.75 |
| 0.8202 | 373.95 |
| 0.8989 | 371.55 |
| 0.9506 | 370.05 |
| 1.0000 | 368.75 |