Operational conditions:
Mole fraction of Tetrachloroethylene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0390 | -0.0100 |
0.0887 | -0.0122 |
0.1357 | -0.0050 |
0.2415 | 0.0293 |
0.2932 | 0.0574 |
0.3454 | 0.0895 |
0.5360 | 0.2607 |
0.6006 | 0.2967 |
0.6688 | 0.3361 |
0.7420 | 0.3242 |
0.8130 | 0.2953 |
0.8822 | 0.2367 |
0.9441 | 0.1429 |
Operational conditions:
Mole fraction of Tetrachloroethylene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0390 | -0.0100 |
0.0887 | -0.0122 |
0.1357 | -0.0050 |
0.2415 | 0.0293 |
0.2932 | 0.0574 |
0.3454 | 0.0895 |
0.5360 | 0.2607 |
0.6006 | 0.2967 |
0.6688 | 0.3361 |
0.7420 | 0.3242 |
0.8130 | 0.2953 |
0.8822 | 0.2367 |
0.9441 | 0.1429 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Tetrachloroethylene (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 473.25 |
0.1002 | 451.55 |
0.1899 | 437.85 |
0.4386 | 413.55 |
0.4839 | 410.35 |
0.6251 | 402.35 |
0.7500 | 397.05 |
0.8869 | 393.25 |
0.9313 | 392.55 |
1.0000 | 391.95 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Tetrachloroethylene (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 473.25 |
0.1002 | 451.55 |
0.1899 | 437.85 |
0.4386 | 413.55 |
0.4839 | 410.35 |
0.6251 | 402.35 |
0.7500 | 397.05 |
0.8869 | 393.25 |
0.9313 | 392.55 |
1.0000 | 391.95 |