Operational conditions:
Mole fraction of Tetraethylene glycol (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0244 | -0.1579 |
0.0475 | -0.2793 |
0.0697 | -0.3660 |
0.0908 | -0.4379 |
0.1303 | -0.5326 |
0.1665 | -0.5915 |
0.2305 | -0.6406 |
0.2853 | -0.6805 |
0.3747 | -0.7080 |
0.4734 | -0.7339 |
0.5451 | -0.7273 |
0.6425 | -0.6723 |
0.7056 | -0.6094 |
0.7824 | -0.4768 |
0.8274 | -0.3856 |
0.8778 | -0.2588 |
0.9349 | -0.1212 |
Operational conditions:
Mole fraction of Tetraethylene glycol (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0244 | -0.1579 |
0.0475 | -0.2793 |
0.0697 | -0.3660 |
0.0908 | -0.4379 |
0.1303 | -0.5326 |
0.1665 | -0.5915 |
0.2305 | -0.6406 |
0.2853 | -0.6805 |
0.3747 | -0.7080 |
0.4734 | -0.7339 |
0.5451 | -0.7273 |
0.6425 | -0.6723 |
0.7056 | -0.6094 |
0.7824 | -0.4768 |
0.8274 | -0.3856 |
0.8778 | -0.2588 |
0.9349 | -0.1212 |
Operational conditions:
Mole fraction of Tetraethylene glycol (2) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0793 | 1044.72 |
0.1126 | 1048.88 |
0.2056 | 1059.34 |
0.2511 | 1063.96 |
0.3592 | 1073.84 |
0.4688 | 1082.58 |
0.5786 | 1090.24 |
0.6885 | 1096.97 |
0.7489 | 1100.31 |
0.8169 | 1103.87 |
0.9226 | 1108.94 |
0.9433 | 1109.85 |
Operational conditions:
Mole fraction of Tetraethylene glycol (2) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0793 | 1044.72 |
0.1126 | 1048.88 |
0.2056 | 1059.34 |
0.2511 | 1063.96 |
0.3592 | 1073.84 |
0.4688 | 1082.58 |
0.5786 | 1090.24 |
0.6885 | 1096.97 |
0.7489 | 1100.31 |
0.8169 | 1103.87 |
0.9226 | 1108.94 |
0.9433 | 1109.85 |