Operational conditions:
Mole fraction of Di-n-propyl ether (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0529 | 0.0066 |
0.1001 | 0.0121 |
0.1500 | 0.0165 |
0.2001 | 0.0201 |
0.2500 | 0.0228 |
0.3002 | 0.0249 |
0.3499 | 0.0265 |
0.4001 | 0.0273 |
0.4501 | 0.0281 |
0.5001 | 0.0280 |
0.5001 | 0.0280 |
0.5500 | 0.0277 |
0.5998 | 0.0268 |
0.6499 | 0.0255 |
0.6996 | 0.0238 |
0.7500 | 0.0215 |
0.8003 | 0.0188 |
0.8500 | 0.0154 |
0.9000 | 0.0113 |
0.9500 | 0.0061 |
Operational conditions:
Mole fraction of Di-n-propyl ether (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0529 | 0.0066 |
0.1001 | 0.0121 |
0.1500 | 0.0165 |
0.2001 | 0.0201 |
0.2500 | 0.0228 |
0.3002 | 0.0249 |
0.3499 | 0.0265 |
0.4001 | 0.0273 |
0.4501 | 0.0281 |
0.5001 | 0.0280 |
0.5001 | 0.0280 |
0.5500 | 0.0277 |
0.5998 | 0.0268 |
0.6499 | 0.0255 |
0.6996 | 0.0238 |
0.7500 | 0.0215 |
0.8003 | 0.0188 |
0.8500 | 0.0154 |
0.9000 | 0.0113 |
0.9500 | 0.0061 |