Operational condition: Temperature, K = 298.15 (Liquid)
Mole fraction of Hexanoic acid, anhydride (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0213 | 0.1530 |
0.0417 | 0.2794 |
0.0612 | 0.3858 |
0.0800 | 0.4763 |
0.0980 | 0.5583 |
0.1154 | 0.6270 |
0.1349 | 0.6965 |
0.1536 | 0.7562 |
0.1714 | 0.8102 |
0.1886 | 0.8551 |
0.2050 | 0.8947 |
0.2208 | 0.9291 |
0.2374 | 0.9613 |
0.2533 | 0.9895 |
0.2625 | 1.0214 |
0.2688 | 1.0318 |
0.2754 | 1.0426 |
0.2824 | 1.0537 |
0.2897 | 1.0643 |
0.2974 | 1.0752 |
0.3056 | 1.0858 |
0.3134 | 1.095 |
0.3215 | 1.1045 |
0.3301 | 1.1137 |
0.3392 | 1.1223 |
0.3471 | 1.1293 |
0.3555 | 1.1362 |
0.3642 | 1.1433 |
0.3733 | 1.1502 |
0.3830 | 1.1563 |
0.3931 | 1.1615 |
0.4023 | 1.166 |
0.4120 | 1.1692 |
0.4222 | 1.1718 |
0.4329 | 1.1735 |
0.4442 | 1.175 |
0.4560 | 1.1749 |
0.4672 | 1.1741 |
0.4789 | 1.1722 |
0.4913 | 1.1675 |
0.5043 | 1.1622 |
0.5162 | 1.1556 |
0.5286 | 1.149 |
0.5417 | 1.1395 |
0.5554 | 1.1298 |
0.5698 | 1.1161 |
0.5850 | 1.1014 |
0.5987 | 1.0856 |
0.6130 | 1.0678 |
0.6280 | 1.0489 |
0.6438 | 1.0253 |
0.6604 | 1.0006 |
0.6778 | 0.9699 |
0.6941 | 0.9393 |
0.7112 | 0.9075 |
0.7291 | 0.8694 |
0.7480 | 0.8290 |
0.7678 | 0.7815 |
0.7854 | 0.7360 |
0.8039 | 0.6960 |
0.8233 | 0.6337 |
0.8436 | 0.5729 |
0.8649 | 0.5074 |
0.8874 | 0.4321 |
0.9079 | 0.3597 |
0.9293 | 0.2827 |
0.9517 | 0.1973 |
0.9753 | 0.1032 |
Operational condition: Temperature, K = 298.15 (Liquid)
Mole fraction of Hexanoic acid, anhydride (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0213 | 0.1530 |
0.0417 | 0.2794 |
0.0612 | 0.3858 |
0.0800 | 0.4763 |
0.0980 | 0.5583 |
0.1154 | 0.6270 |
0.1349 | 0.6965 |
0.1536 | 0.7562 |
0.1714 | 0.8102 |
0.1886 | 0.8551 |
0.2050 | 0.8947 |
0.2208 | 0.9291 |
0.2374 | 0.9613 |
0.2533 | 0.9895 |
0.2625 | 1.0214 |
0.2688 | 1.0318 |
0.2754 | 1.0426 |
0.2824 | 1.0537 |
0.2897 | 1.0643 |
0.2974 | 1.0752 |
0.3056 | 1.0858 |
0.3134 | 1.095 |
0.3215 | 1.1045 |
0.3301 | 1.1137 |
0.3392 | 1.1223 |
0.3471 | 1.1293 |
0.3555 | 1.1362 |
0.3642 | 1.1433 |
0.3733 | 1.1502 |
0.3830 | 1.1563 |
0.3931 | 1.1615 |
0.4023 | 1.166 |
0.4120 | 1.1692 |
0.4222 | 1.1718 |
0.4329 | 1.1735 |
0.4442 | 1.175 |
0.4560 | 1.1749 |
0.4672 | 1.1741 |
0.4789 | 1.1722 |
0.4913 | 1.1675 |
0.5043 | 1.1622 |
0.5162 | 1.1556 |
0.5286 | 1.149 |
0.5417 | 1.1395 |
0.5554 | 1.1298 |
0.5698 | 1.1161 |
0.5850 | 1.1014 |
0.5987 | 1.0856 |
0.6130 | 1.0678 |
0.6280 | 1.0489 |
0.6438 | 1.0253 |
0.6604 | 1.0006 |
0.6778 | 0.9699 |
0.6941 | 0.9393 |
0.7112 | 0.9075 |
0.7291 | 0.8694 |
0.7480 | 0.8290 |
0.7678 | 0.7815 |
0.7854 | 0.7360 |
0.8039 | 0.6960 |
0.8233 | 0.6337 |
0.8436 | 0.5729 |
0.8649 | 0.5074 |
0.8874 | 0.4321 |
0.9079 | 0.3597 |
0.9293 | 0.2827 |
0.9517 | 0.1973 |
0.9753 | 0.1032 |