Operational conditions:
Mole fraction of Trichloroethylene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0381 | -0.1900 |
0.0886 | -0.4430 |
0.1426 | -0.6629 |
0.2005 | -0.9026 |
0.2675 | -1.1538 |
0.3373 | -1.4331 |
0.4001 | -1.6473 |
0.6547 | -1.4343 |
0.7095 | -1.3164 |
0.7643 | -1.1706 |
0.8186 | -0.9626 |
0.8730 | -0.7349 |
0.9254 | -0.4694 |
0.9678 | -0.2110 |
Operational conditions:
Mole fraction of Trichloroethylene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0381 | -0.1900 |
0.0886 | -0.4430 |
0.1426 | -0.6629 |
0.2005 | -0.9026 |
0.2675 | -1.1538 |
0.3373 | -1.4331 |
0.4001 | -1.6473 |
0.6547 | -1.4343 |
0.7095 | -1.3164 |
0.7643 | -1.1706 |
0.8186 | -0.9626 |
0.8730 | -0.7349 |
0.9254 | -0.4694 |
0.9678 | -0.2110 |
Operational condition: Pressure, kPa = 93.5 (Liquid)
Mole fraction of Trichloroethylene (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 473.25 |
0.0725 | 458.55 |
0.1507 | 443.15 |
0.3078 | 415.65 |
0.4447 | 396.95 |
0.6156 | 379.65 |
0.7193 | 371.75 |
0.8102 | 366.15 |
0.9275 | 360.45 |
1.0000 | 358.25 |
Operational condition: Pressure, kPa = 93.5 (Liquid)
Mole fraction of Trichloroethylene (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 473.25 |
0.0725 | 458.55 |
0.1507 | 443.15 |
0.3078 | 415.65 |
0.4447 | 396.95 |
0.6156 | 379.65 |
0.7193 | 371.75 |
0.8102 | 366.15 |
0.9275 | 360.45 |
1.0000 | 358.25 |