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 | 0.0916 | 0.2330 |
298.15 | 0.1591 | 0.4100 |
298.15 | 0.2403 | 0.5890 |
298.15 | 0.3201 | 0.7520 |
298.15 | 0.3985 | 0.8780 |
298.15 | 0.4755 | 0.9790 |
298.15 | 0.5445 | 1.043 |
298.15 | 0.6392 | 1.078 |
298.15 | 0.6992 | 1.068 |
298.15 | 0.7733 | 0.9910 |
298.15 | 0.8569 | 0.8330 |
298.15 | 0.9330 | 0.5130 |
308.15 | 0.0919 | 0.2720 |
308.15 | 0.1603 | 0.4530 |
308.15 | 0.2403 | 0.6490 |
308.15 | 0.3244 | 0.7880 |
308.15 | 0.4034 | 0.9070 |
308.15 | 0.4760 | 1.022 |
308.15 | 0.5541 | 1.097 |
308.15 | 0.7020 | 1.139 |
308.15 | 0.7747 | 1.079 |
308.15 | 0.8671 | 0.8540 |
308.15 | 0.9322 | 0.5400 |
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 | 0.0916 | 0.2330 |
298.15 | 0.1591 | 0.4100 |
298.15 | 0.2403 | 0.5890 |
298.15 | 0.3201 | 0.7520 |
298.15 | 0.3985 | 0.8780 |
298.15 | 0.4755 | 0.9790 |
298.15 | 0.5445 | 1.043 |
298.15 | 0.6392 | 1.078 |
298.15 | 0.6992 | 1.068 |
298.15 | 0.7733 | 0.9910 |
298.15 | 0.8569 | 0.8330 |
298.15 | 0.9330 | 0.5130 |
308.15 | 0.0919 | 0.2720 |
308.15 | 0.1603 | 0.4530 |
308.15 | 0.2403 | 0.6490 |
308.15 | 0.3244 | 0.7880 |
308.15 | 0.4034 | 0.9070 |
308.15 | 0.4760 | 1.022 |
308.15 | 0.5541 | 1.097 |
308.15 | 0.7020 | 1.139 |
308.15 | 0.7747 | 1.079 |
308.15 | 0.8671 | 0.8540 |
308.15 | 0.9322 | 0.5400 |