Operational conditions:
Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0378 | -0.2946 |
0.0688 | -0.6239 |
0.1005 | -0.9566 |
0.1295 | -1.2863 |
0.1325 | -1.2912 |
0.1565 | -1.5557 |
0.1793 | -1.7718 |
0.2167 | -2.0662 |
0.2914 | -2.7285 |
0.3555 | -3.2401 |
0.4111 | -3.5093 |
0.4577 | -3.5259 |
0.4979 | -3.5138 |
0.5577 | -3.4158 |
0.6277 | -3.161 |
0.6654 | -2.9783 |
0.7123 | -2.7776 |
0.7577 | -2.5478 |
0.8121 | -2.1495 |
0.8537 | -1.8201 |
0.9099 | -1.0532 |
Operational conditions:
Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0378 | -0.2946 |
0.0688 | -0.6239 |
0.1005 | -0.9566 |
0.1295 | -1.2863 |
0.1325 | -1.2912 |
0.1565 | -1.5557 |
0.1793 | -1.7718 |
0.2167 | -2.0662 |
0.2914 | -2.7285 |
0.3555 | -3.2401 |
0.4111 | -3.5093 |
0.4577 | -3.5259 |
0.4979 | -3.5138 |
0.5577 | -3.4158 |
0.6277 | -3.161 |
0.6654 | -2.9783 |
0.7123 | -2.7776 |
0.7577 | -2.5478 |
0.8121 | -2.1495 |
0.8537 | -1.8201 |
0.9099 | -1.0532 |
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 | 460.95 |
0.0728 | 454.55 |
0.1447 | 449.35 |
0.2880 | 441.35 |
0.3829 | 437.05 |
0.4774 | 433.25 |
0.6190 | 428.15 |
0.8025 | 422.45 |
0.9125 | 419.35 |
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 | 460.95 |
0.0728 | 454.55 |
0.1447 | 449.35 |
0.2880 | 441.35 |
0.3829 | 437.05 |
0.4774 | 433.25 |
0.6190 | 428.15 |
0.8025 | 422.45 |
0.9125 | 419.35 |
1.0000 | 417.05 |