Operational conditions:
Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.1042 | -0.3170 |
0.1790 | -0.4900 |
0.2794 | -0.6820 |
0.3677 | -0.7980 |
0.4368 | -0.8430 |
0.4659 | -0.8580 |
0.5377 | -0.8450 |
0.6357 | -0.7630 |
0.6994 | -0.6940 |
0.8231 | -0.4630 |
0.8858 | -0.3090 |
Operational conditions:
Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.1042 | -0.3170 |
0.1790 | -0.4900 |
0.2794 | -0.6820 |
0.3677 | -0.7980 |
0.4368 | -0.8430 |
0.4659 | -0.8580 |
0.5377 | -0.8450 |
0.6357 | -0.7630 |
0.6994 | -0.6940 |
0.8231 | -0.4630 |
0.8858 | -0.3090 |
Operational condition: Pressure, kPa = 94.7 (Liquid)
Mole fraction of Ethylbenzene (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 416.95 |
0.1251 | 416.45 |
0.2224 | 415.95 |
0.3003 | 415.45 |
0.4178 | 414.55 |
0.6318 | 412.35 |
0.7202 | 411.15 |
0.8370 | 409.55 |
0.9116 | 408.45 |
1.0000 | 406.95 |
Operational condition: Pressure, kPa = 94.7 (Liquid)
Mole fraction of Ethylbenzene (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 416.95 |
0.1251 | 416.45 |
0.2224 | 415.95 |
0.3003 | 415.45 |
0.4178 | 414.55 |
0.6318 | 412.35 |
0.7202 | 411.15 |
0.8370 | 409.55 |
0.9116 | 408.45 |
1.0000 | 406.95 |