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 |