Operational conditions:
| Mole fraction of Benzene, nitro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1038 | 0.8704 |
| 0.2065 | 1.4168 |
| 0.3060 | 1.7561 |
| 0.3954 | 1.9486 |
| 0.4911 | 2.043 |
| 0.5906 | 2.0295 |
| 0.6999 | 1.8852 |
| 0.8042 | 1.5944 |
| 0.8996 | 1.103 |
Operational conditions:
| Mole fraction of Benzene, nitro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1038 | 0.8704 |
| 0.2065 | 1.4168 |
| 0.3060 | 1.7561 |
| 0.3954 | 1.9486 |
| 0.4911 | 2.043 |
| 0.5906 | 2.0295 |
| 0.6999 | 1.8852 |
| 0.8042 | 1.5944 |
| 0.8996 | 1.103 |
Operational condition: Pressure, kPa = 94.95 (Liquid)
| Mole fraction of Isopropyl Alcohol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 481.15 |
| 0.0851 | 434.55 |
| 0.1706 | 414.25 |
| 0.2308 | 404.85 |
| 0.2915 | 397.25 |
| 0.3707 | 389.35 |
| 0.4514 | 382.55 |
| 0.5221 | 377.45 |
| 0.5916 | 372.95 |
| 0.6663 | 368.55 |
| 0.7421 | 364.45 |
| 0.8386 | 359.85 |
| 0.8968 | 357.35 |
| 0.9508 | 355.25 |
| 1.0000 | 353.85 |
Operational condition: Pressure, kPa = 94.95 (Liquid)
| Mole fraction of Isopropyl Alcohol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 481.15 |
| 0.0851 | 434.55 |
| 0.1706 | 414.25 |
| 0.2308 | 404.85 |
| 0.2915 | 397.25 |
| 0.3707 | 389.35 |
| 0.4514 | 382.55 |
| 0.5221 | 377.45 |
| 0.5916 | 372.95 |
| 0.6663 | 368.55 |
| 0.7421 | 364.45 |
| 0.8386 | 359.85 |
| 0.8968 | 357.35 |
| 0.9508 | 355.25 |
| 1.0000 | 353.85 |