Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of n-Butyl ether (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 | 0.0920 | 0.2310 |
298.15 | 0.1608 | 0.3900 |
298.15 | 0.2389 | 0.5510 |
298.15 | 0.3161 | 0.6700 |
298.15 | 0.3993 | 0.7830 |
298.15 | 0.4694 | 0.8520 |
298.15 | 0.5458 | 0.9050 |
298.15 | 0.6389 | 0.9250 |
298.15 | 0.7088 | 0.8840 |
298.15 | 0.7760 | 0.8120 |
298.15 | 0.8626 | 0.6450 |
298.15 | 0.9423 | 0.3500 |
308.15 | 0.0836 | 0.2260 |
308.15 | 0.1547 | 0.3980 |
308.15 | 0.2348 | 0.5760 |
308.15 | 0.3248 | 0.7350 |
308.15 | 0.4249 | 0.8460 |
308.15 | 0.4894 | 0.9200 |
308.15 | 0.5775 | 0.9520 |
308.15 | 0.6519 | 0.9440 |
308.15 | 0.7302 | 0.8950 |
308.15 | 0.7870 | 0.8110 |
308.15 | 0.8553 | 0.6740 |
308.15 | 0.9681 | 0.2360 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of n-Butyl ether (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 | 0.0920 | 0.2310 |
298.15 | 0.1608 | 0.3900 |
298.15 | 0.2389 | 0.5510 |
298.15 | 0.3161 | 0.6700 |
298.15 | 0.3993 | 0.7830 |
298.15 | 0.4694 | 0.8520 |
298.15 | 0.5458 | 0.9050 |
298.15 | 0.6389 | 0.9250 |
298.15 | 0.7088 | 0.8840 |
298.15 | 0.7760 | 0.8120 |
298.15 | 0.8626 | 0.6450 |
298.15 | 0.9423 | 0.3500 |
308.15 | 0.0836 | 0.2260 |
308.15 | 0.1547 | 0.3980 |
308.15 | 0.2348 | 0.5760 |
308.15 | 0.3248 | 0.7350 |
308.15 | 0.4249 | 0.8460 |
308.15 | 0.4894 | 0.9200 |
308.15 | 0.5775 | 0.9520 |
308.15 | 0.6519 | 0.9440 |
308.15 | 0.7302 | 0.8950 |
308.15 | 0.7870 | 0.8110 |
308.15 | 0.8553 | 0.6740 |
308.15 | 0.9681 | 0.2360 |