Operational conditions:
Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0331 | -0.4736 |
0.0582 | -0.8596 |
0.0765 | -1.0713 |
0.1279 | -1.7834 |
0.1292 | -1.727 |
0.1796 | -2.3226 |
0.2318 | -2.945 |
0.2344 | -2.908 |
0.2880 | -3.5053 |
0.3219 | -3.7362 |
0.3400 | -4.0278 |
0.4028 | -4.2331 |
0.4675 | -4.567 |
0.5226 | -4.7498 |
0.5688 | -4.8414 |
0.5953 | -4.8531 |
0.6265 | -4.5472 |
0.6815 | -4.1867 |
0.7384 | -3.7221 |
0.7933 | -3.1047 |
0.8536 | -2.2318 |
0.9099 | -1.4803 |
0.9574 | -0.7502 |
Operational conditions:
Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0331 | -0.4736 |
0.0582 | -0.8596 |
0.0765 | -1.0713 |
0.1279 | -1.7834 |
0.1292 | -1.727 |
0.1796 | -2.3226 |
0.2318 | -2.945 |
0.2344 | -2.908 |
0.2880 | -3.5053 |
0.3219 | -3.7362 |
0.3400 | -4.0278 |
0.4028 | -4.2331 |
0.4675 | -4.567 |
0.5226 | -4.7498 |
0.5688 | -4.8414 |
0.5953 | -4.8531 |
0.6265 | -4.5472 |
0.6815 | -4.1867 |
0.7384 | -3.7221 |
0.7933 | -3.1047 |
0.8536 | -2.2318 |
0.9099 | -1.4803 |
0.9574 | -0.7502 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 473.25 |
0.0755 | 469.35 |
0.1319 | 466.65 |
0.3474 | 455.35 |
0.5776 | 441.55 |
0.6458 | 437.25 |
0.7848 | 428.25 |
0.9162 | 420.85 |
0.9623 | 418.55 |
1.0000 | 417.05 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 473.25 |
0.0755 | 469.35 |
0.1319 | 466.65 |
0.3474 | 455.35 |
0.5776 | 441.55 |
0.6458 | 437.25 |
0.7848 | 428.25 |
0.9162 | 420.85 |
0.9623 | 418.55 |
1.0000 | 417.05 |