Operational conditions:
Mole fraction of Ethane, 1,1,1-trichloro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0243 | -0.0425 |
0.0579 | -0.0961 |
0.1090 | -0.1765 |
0.1532 | -0.2354 |
0.1973 | -0.2840 |
0.2440 | -0.3332 |
0.2857 | -0.3638 |
0.3462 | -0.3899 |
0.4106 | -0.4124 |
0.4797 | -0.4129 |
0.5571 | -0.3955 |
0.6064 | -0.3635 |
0.6632 | -0.3241 |
0.7189 | -0.2785 |
0.7771 | -0.2201 |
0.8537 | -0.1351 |
0.9297 | -0.0428 |
Operational conditions:
Mole fraction of Ethane, 1,1,1-trichloro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0243 | -0.0425 |
0.0579 | -0.0961 |
0.1090 | -0.1765 |
0.1532 | -0.2354 |
0.1973 | -0.2840 |
0.2440 | -0.3332 |
0.2857 | -0.3638 |
0.3462 | -0.3899 |
0.4106 | -0.4124 |
0.4797 | -0.4129 |
0.5571 | -0.3955 |
0.6064 | -0.3635 |
0.6632 | -0.3241 |
0.7189 | -0.2785 |
0.7771 | -0.2201 |
0.8537 | -0.1351 |
0.9297 | -0.0428 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Ethane, 1,1,1-trichloro- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 460.95 |
0.0728 | 428.15 |
0.1741 | 402.05 |
0.3598 | 376.55 |
0.4574 | 367.95 |
0.5880 | 359.25 |
0.7405 | 351.85 |
0.8771 | 347.45 |
0.9235 | 346.45 |
1.0000 | 345.45 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Ethane, 1,1,1-trichloro- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 460.95 |
0.0728 | 428.15 |
0.1741 | 402.05 |
0.3598 | 376.55 |
0.4574 | 367.95 |
0.5880 | 359.25 |
0.7405 | 351.85 |
0.8771 | 347.45 |
0.9235 | 346.45 |
1.0000 | 345.45 |