Operational conditions:
Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0732 | -0.0591 |
0.1296 | -0.0918 |
0.1713 | -0.1075 |
0.2259 | -0.1260 |
0.2783 | -0.1511 |
0.3275 | -0.1915 |
0.3609 | -0.2291 |
0.4054 | -0.2979 |
0.4636 | -0.3762 |
0.5266 | -0.4621 |
0.6133 | -0.5779 |
0.6613 | -0.5986 |
0.7158 | -0.5474 |
0.7593 | -0.5309 |
0.8032 | -0.4451 |
0.8610 | -0.2831 |
0.9269 | -0.1191 |
Operational conditions:
Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0732 | -0.0591 |
0.1296 | -0.0918 |
0.1713 | -0.1075 |
0.2259 | -0.1260 |
0.2783 | -0.1511 |
0.3275 | -0.1915 |
0.3609 | -0.2291 |
0.4054 | -0.2979 |
0.4636 | -0.3762 |
0.5266 | -0.4621 |
0.6133 | -0.5779 |
0.6613 | -0.5986 |
0.7158 | -0.5474 |
0.7593 | -0.5309 |
0.8032 | -0.4451 |
0.8610 | -0.2831 |
0.9269 | -0.1191 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 460.95 |
0.0748 | 436.85 |
0.1307 | 423.25 |
0.3107 | 395.25 |
0.4286 | 383.85 |
0.5197 | 376.95 |
0.6433 | 369.55 |
0.8440 | 360.45 |
0.9253 | 357.45 |
1.0000 | 355.05 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 460.95 |
0.0748 | 436.85 |
0.1307 | 423.25 |
0.3107 | 395.25 |
0.4286 | 383.85 |
0.5197 | 376.95 |
0.6433 | 369.55 |
0.8440 | 360.45 |
0.9253 | 357.45 |
1.0000 | 355.05 |