Operational conditions:
Mole fraction of Benzene, nitro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0935 | 0.0761 |
0.1856 | 0.1786 |
0.2722 | 0.2547 |
0.3514 | 0.3129 |
0.4247 | 0.3567 |
0.4887 | 0.3849 |
0.5445 | 0.4002 |
0.5600 | 0.4043 |
0.6061 | 0.3929 |
0.6576 | 0.3749 |
0.7072 | 0.3509 |
0.7577 | 0.3179 |
0.8125 | 0.2697 |
0.8647 | 0.2147 |
0.9154 | 0.1459 |
0.9624 | 0.0697 |
Operational conditions:
Mole fraction of Benzene, nitro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0935 | 0.0761 |
0.1856 | 0.1786 |
0.2722 | 0.2547 |
0.3514 | 0.3129 |
0.4247 | 0.3567 |
0.4887 | 0.3849 |
0.5445 | 0.4002 |
0.5600 | 0.4043 |
0.6061 | 0.3929 |
0.6576 | 0.3749 |
0.7072 | 0.3509 |
0.7577 | 0.3179 |
0.8125 | 0.2697 |
0.8647 | 0.2147 |
0.9154 | 0.1459 |
0.9624 | 0.0697 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Benzene, nitro- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 460.95 |
0.0725 | 458.15 |
0.1290 | 458.15 |
0.2568 | 459.25 |
0.3519 | 460.85 |
0.5465 | 465.35 |
0.6593 | 468.85 |
0.8289 | 475.05 |
0.9175 | 479.05 |
1.0000 | 483.05 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Benzene, nitro- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 460.95 |
0.0725 | 458.15 |
0.1290 | 458.15 |
0.2568 | 459.25 |
0.3519 | 460.85 |
0.5465 | 465.35 |
0.6593 | 468.85 |
0.8289 | 475.05 |
0.9175 | 479.05 |
1.0000 | 483.05 |