Operational conditions:
Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.1040 | 0.5210 |
0.2071 | 0.8760 |
0.2583 | 1.036 |
0.3171 | 1.176 |
0.3579 | 1.28 |
0.4106 | 1.313 |
0.4816 | 1.332 |
0.5110 | 1.358 |
0.5822 | 1.311 |
0.6501 | 1.237 |
0.7359 | 1.082 |
0.8069 | 0.8920 |
0.8814 | 0.6030 |
0.9330 | 0.3580 |
Operational conditions:
Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.1040 | 0.5210 |
0.2071 | 0.8760 |
0.2583 | 1.036 |
0.3171 | 1.176 |
0.3579 | 1.28 |
0.4106 | 1.313 |
0.4816 | 1.332 |
0.5110 | 1.358 |
0.5822 | 1.311 |
0.6501 | 1.237 |
0.7359 | 1.082 |
0.8069 | 0.8920 |
0.8814 | 0.6030 |
0.9330 | 0.3580 |
Operational condition: Pressure, kPa = 95.8 (Liquid)
Mole fraction of Heptane (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 417.35 |
0.0937 | 409.45 |
0.1703 | 403.75 |
0.2911 | 396.05 |
0.4181 | 389.15 |
0.5571 | 382.75 |
0.6264 | 379.95 |
0.7155 | 376.75 |
0.8342 | 373.35 |
0.9197 | 371.35 |
1.0000 | 369.75 |
Operational condition: Pressure, kPa = 95.8 (Liquid)
Mole fraction of Heptane (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 417.35 |
0.0937 | 409.45 |
0.1703 | 403.75 |
0.2911 | 396.05 |
0.4181 | 389.15 |
0.5571 | 382.75 |
0.6264 | 379.95 |
0.7155 | 376.75 |
0.8342 | 373.35 |
0.9197 | 371.35 |
1.0000 | 369.75 |