Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of n-Butyl ether (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 | 0.0979 | 0.3980 |
298.15 | 0.1702 | 0.6640 |
298.15 | 0.2558 | 0.9170 |
298.15 | 0.3242 | 1.074 |
298.15 | 0.4033 | 1.182 |
298.15 | 0.4684 | 1.262 |
298.15 | 0.5438 | 1.313 |
298.15 | 0.6374 | 1.301 |
298.15 | 0.7023 | 1.254 |
298.15 | 0.7739 | 1.127 |
298.15 | 0.8554 | 0.8960 |
298.15 | 0.9278 | 0.5390 |
308.15 | 0.0991 | 0.4050 |
308.15 | 0.1692 | 0.6570 |
308.15 | 0.2350 | 0.8460 |
308.15 | 0.3202 | 1.046 |
308.15 | 0.3985 | 1.155 |
308.15 | 0.5414 | 1.28 |
308.15 | 0.6464 | 1.281 |
308.15 | 0.7326 | 1.213 |
308.15 | 0.8110 | 1.03 |
308.15 | 0.8986 | 0.7610 |
308.15 | 0.9603 | 0.3420 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of n-Butyl ether (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 | 0.0979 | 0.3980 |
298.15 | 0.1702 | 0.6640 |
298.15 | 0.2558 | 0.9170 |
298.15 | 0.3242 | 1.074 |
298.15 | 0.4033 | 1.182 |
298.15 | 0.4684 | 1.262 |
298.15 | 0.5438 | 1.313 |
298.15 | 0.6374 | 1.301 |
298.15 | 0.7023 | 1.254 |
298.15 | 0.7739 | 1.127 |
298.15 | 0.8554 | 0.8960 |
298.15 | 0.9278 | 0.5390 |
308.15 | 0.0991 | 0.4050 |
308.15 | 0.1692 | 0.6570 |
308.15 | 0.2350 | 0.8460 |
308.15 | 0.3202 | 1.046 |
308.15 | 0.3985 | 1.155 |
308.15 | 0.5414 | 1.28 |
308.15 | 0.6464 | 1.281 |
308.15 | 0.7326 | 1.213 |
308.15 | 0.8110 | 1.03 |
308.15 | 0.8986 | 0.7610 |
308.15 | 0.9603 | 0.3420 |