Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 | 0.1071 | 0.7382 |
298.15 | 0.1572 | 0.8822 |
298.15 | 0.1921 | 0.9765 |
298.15 | 0.2514 | 1.0312 |
298.15 | 0.2956 | 1.0853 |
298.15 | 0.3568 | 1.1358 |
298.15 | 0.4563 | 1.1383 |
298.15 | 0.4997 | 1.1368 |
298.15 | 0.5787 | 1.0826 |
298.15 | 0.6247 | 1.0556 |
298.15 | 0.6723 | 0.9975 |
298.15 | 0.7350 | 0.9059 |
298.15 | 0.7771 | 0.8293 |
298.15 | 0.8331 | 0.6809 |
298.15 | 0.8704 | 0.6028 |
298.15 | 0.9049 | 0.4574 |
298.15 | 0.9209 | 0.4097 |
298.15 | 0.9539 | 0.2472 |
308.15 | 0.0654 | 0.6480 |
308.15 | 0.1274 | 0.9151 |
308.15 | 0.1934 | 1.0981 |
308.15 | 0.2171 | 1.1413 |
308.15 | 0.2626 | 1.2102 |
308.15 | 0.3223 | 1.2803 |
308.15 | 0.3568 | 1.3046 |
308.15 | 0.3997 | 1.3107 |
308.15 | 0.4542 | 1.32 |
308.15 | 0.4997 | 1.3233 |
308.15 | 0.5711 | 1.2849 |
308.15 | 0.6247 | 1.2408 |
308.15 | 0.6723 | 1.1395 |
308.15 | 0.6754 | 1.1491 |
308.15 | 0.6893 | 1.126 |
308.15 | 0.7351 | 1.0439 |
308.15 | 0.7690 | 0.9552 |
308.15 | 0.8062 | 0.8703 |
308.15 | 0.8332 | 0.7908 |
308.15 | 0.8535 | 0.7115 |
308.15 | 0.9210 | 0.4717 |
308.15 | 0.9539 | 0.2863 |
318.15 | 0.1071 | 1.0394 |
318.15 | 0.1722 | 1.1921 |
318.15 | 0.2257 | 1.309 |
318.15 | 0.3223 | 1.4357 |
318.15 | 0.3568 | 1.4752 |
318.15 | 0.3997 | 1.4928 |
318.15 | 0.4542 | 1.4863 |
318.15 | 0.4997 | 1.4863 |
318.15 | 0.5552 | 1.4452 |
318.15 | 0.5711 | 1.425 |
318.15 | 0.6247 | 1.3704 |
318.15 | 0.6893 | 1.2562 |
318.15 | 0.7351 | 1.1473 |
318.15 | 0.7690 | 1.0663 |
318.15 | 0.7966 | 0.9843 |
318.15 | 0.8062 | 0.9497 |
318.15 | 0.8535 | 0.7900 |
318.15 | 0.9300 | 0.4622 |
318.15 | 0.9696 | 0.2166 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 | 0.1071 | 0.7382 |
298.15 | 0.1572 | 0.8822 |
298.15 | 0.1921 | 0.9765 |
298.15 | 0.2514 | 1.0312 |
298.15 | 0.2956 | 1.0853 |
298.15 | 0.3568 | 1.1358 |
298.15 | 0.4563 | 1.1383 |
298.15 | 0.4997 | 1.1368 |
298.15 | 0.5787 | 1.0826 |
298.15 | 0.6247 | 1.0556 |
298.15 | 0.6723 | 0.9975 |
298.15 | 0.7350 | 0.9059 |
298.15 | 0.7771 | 0.8293 |
298.15 | 0.8331 | 0.6809 |
298.15 | 0.8704 | 0.6028 |
298.15 | 0.9049 | 0.4574 |
298.15 | 0.9209 | 0.4097 |
298.15 | 0.9539 | 0.2472 |
308.15 | 0.0654 | 0.6480 |
308.15 | 0.1274 | 0.9151 |
308.15 | 0.1934 | 1.0981 |
308.15 | 0.2171 | 1.1413 |
308.15 | 0.2626 | 1.2102 |
308.15 | 0.3223 | 1.2803 |
308.15 | 0.3568 | 1.3046 |
308.15 | 0.3997 | 1.3107 |
308.15 | 0.4542 | 1.32 |
308.15 | 0.4997 | 1.3233 |
308.15 | 0.5711 | 1.2849 |
308.15 | 0.6247 | 1.2408 |
308.15 | 0.6723 | 1.1395 |
308.15 | 0.6754 | 1.1491 |
308.15 | 0.6893 | 1.126 |
308.15 | 0.7351 | 1.0439 |
308.15 | 0.7690 | 0.9552 |
308.15 | 0.8062 | 0.8703 |
308.15 | 0.8332 | 0.7908 |
308.15 | 0.8535 | 0.7115 |
308.15 | 0.9210 | 0.4717 |
308.15 | 0.9539 | 0.2863 |
318.15 | 0.1071 | 1.0394 |
318.15 | 0.1722 | 1.1921 |
318.15 | 0.2257 | 1.309 |
318.15 | 0.3223 | 1.4357 |
318.15 | 0.3568 | 1.4752 |
318.15 | 0.3997 | 1.4928 |
318.15 | 0.4542 | 1.4863 |
318.15 | 0.4997 | 1.4863 |
318.15 | 0.5552 | 1.4452 |
318.15 | 0.5711 | 1.425 |
318.15 | 0.6247 | 1.3704 |
318.15 | 0.6893 | 1.2562 |
318.15 | 0.7351 | 1.1473 |
318.15 | 0.7690 | 1.0663 |
318.15 | 0.7966 | 0.9843 |
318.15 | 0.8062 | 0.9497 |
318.15 | 0.8535 | 0.7900 |
318.15 | 0.9300 | 0.4622 |
318.15 | 0.9696 | 0.2166 |