Operational conditions:
| Temperature, K - Liquid | Activity coefficient of Ethanol (1) - Liquid |
|---|---|
| 333.20 | 1.18 |
| 348.20 | 1.15 |
| 363.20 | 1.12 |
Operational conditions:
| Temperature, K - Liquid | Activity coefficient of Ethanol (1) - Liquid |
|---|---|
| 333.20 | 1.18 |
| 348.20 | 1.15 |
| 363.20 | 1.12 |
Operational conditions:
| Mole fraction of Triethylene glycol (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0313 | 0.1333 |
| 0.0606 | 0.2354 |
| 0.0883 | 0.3220 |
| 0.1143 | 0.3785 |
| 0.1623 | 0.4652 |
| 0.2047 | 0.5225 |
| 0.2792 | 0.5880 |
| 0.3405 | 0.6074 |
| 0.4365 | 0.6275 |
| 0.5376 | 0.6116 |
| 0.6078 | 0.6056 |
| 0.6992 | 0.5534 |
| 0.7560 | 0.4878 |
| 0.8230 | 0.4071 |
| 0.8613 | 0.3287 |
| 0.9029 | 0.2488 |
| 0.9490 | 0.1357 |
Operational conditions:
| Mole fraction of Ethanol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1040 | 0.1170 |
| 0.2042 | 0.2450 |
| 0.3010 | 0.3500 |
| 0.3990 | 0.4350 |
| 0.5002 | 0.4940 |
| 0.5990 | 0.5080 |
| 0.6993 | 0.4700 |
| 0.7995 | 0.4030 |
| 0.8992 | 0.2600 |
Operational conditions:
| Mole fraction of Triethylene glycol (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0313 | 0.1333 |
| 0.0606 | 0.2354 |
| 0.0883 | 0.3220 |
| 0.1143 | 0.3785 |
| 0.1623 | 0.4652 |
| 0.2047 | 0.5225 |
| 0.2792 | 0.5880 |
| 0.3405 | 0.6074 |
| 0.4365 | 0.6275 |
| 0.5376 | 0.6116 |
| 0.6078 | 0.6056 |
| 0.6992 | 0.5534 |
| 0.7560 | 0.4878 |
| 0.8230 | 0.4071 |
| 0.8613 | 0.3287 |
| 0.9029 | 0.2488 |
| 0.9490 | 0.1357 |
Operational conditions:
| Mole fraction of Ethanol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1040 | 0.1170 |
| 0.2042 | 0.2450 |
| 0.3010 | 0.3500 |
| 0.3990 | 0.4350 |
| 0.5002 | 0.4940 |
| 0.5990 | 0.5080 |
| 0.6993 | 0.4700 |
| 0.7995 | 0.4030 |
| 0.8992 | 0.2600 |