Operational conditions:
Mole fraction of Benzene, bromo- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0325 | 0.0521 |
0.0701 | 0.1171 |
0.1122 | 0.1859 |
0.1574 | 0.2512 |
0.2039 | 0.3060 |
0.2518 | 0.3619 |
0.3014 | 0.4094 |
0.3485 | 0.4531 |
0.3767 | 0.4745 |
0.3955 | 0.4923 |
0.4091 | 0.4955 |
0.4468 | 0.5030 |
0.4960 | 0.5119 |
0.5567 | 0.5091 |
0.6277 | 0.4865 |
0.7077 | 0.4322 |
0.7985 | 0.3466 |
0.8979 | 0.2023 |
Operational conditions:
Mole fraction of Benzene, bromo- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0325 | 0.0521 |
0.0701 | 0.1171 |
0.1122 | 0.1859 |
0.1574 | 0.2512 |
0.2039 | 0.3060 |
0.2518 | 0.3619 |
0.3014 | 0.4094 |
0.3485 | 0.4531 |
0.3767 | 0.4745 |
0.3955 | 0.4923 |
0.4091 | 0.4955 |
0.4468 | 0.5030 |
0.4960 | 0.5119 |
0.5567 | 0.5091 |
0.6277 | 0.4865 |
0.7077 | 0.4322 |
0.7985 | 0.3466 |
0.8979 | 0.2023 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Benzene, bromo- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 460.95 |
0.1101 | 449.15 |
0.2198 | 441.05 |
0.3103 | 436.15 |
0.4521 | 430.75 |
0.6183 | 426.95 |
0.7297 | 425.45 |
0.8024 | 424.95 |
0.9012 | 424.65 |
1.0000 | 426.85 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Benzene, bromo- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 460.95 |
0.1101 | 449.15 |
0.2198 | 441.05 |
0.3103 | 436.15 |
0.4521 | 430.75 |
0.6183 | 426.95 |
0.7297 | 425.45 |
0.8024 | 424.95 |
0.9012 | 424.65 |
1.0000 | 426.85 |