Operational conditions:
Mole fraction of Trichloroethylene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0673 | -0.0958 |
0.1345 | -0.2424 |
0.2079 | -0.4434 |
0.3016 | -0.6367 |
0.3784 | -0.6414 |
0.4461 | -0.6140 |
0.4987 | -0.5847 |
0.6022 | -0.4612 |
0.6641 | -0.4271 |
0.7014 | -0.4102 |
0.7370 | -0.4084 |
0.8114 | -0.3575 |
0.8611 | -0.2953 |
0.9151 | -0.2011 |
Operational conditions:
Mole fraction of Trichloroethylene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0673 | -0.0958 |
0.1345 | -0.2424 |
0.2079 | -0.4434 |
0.3016 | -0.6367 |
0.3784 | -0.6414 |
0.4461 | -0.6140 |
0.4987 | -0.5847 |
0.6022 | -0.4612 |
0.6641 | -0.4271 |
0.7014 | -0.4102 |
0.7370 | -0.4084 |
0.8114 | -0.3575 |
0.8611 | -0.2953 |
0.9151 | -0.2011 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Trichloroethylene (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 460.95 |
0.0918 | 445.85 |
0.1653 | 432.15 |
0.3036 | 408.75 |
0.3480 | 402.45 |
0.6132 | 376.15 |
0.7255 | 369.35 |
0.8409 | 363.75 |
0.9275 | 360.25 |
1.0000 | 357.75 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Trichloroethylene (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 460.95 |
0.0918 | 445.85 |
0.1653 | 432.15 |
0.3036 | 408.75 |
0.3480 | 402.45 |
0.6132 | 376.15 |
0.7255 | 369.35 |
0.8409 | 363.75 |
0.9275 | 360.25 |
1.0000 | 357.75 |