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 |
|---|---|
| 0.0307 | 0.2323 |
| 0.0596 | 0.4155 |
| 0.0868 | 0.5629 |
| 0.1125 | 0.6839 |
| 0.1368 | 0.7899 |
| 0.1597 | 0.8764 |
| 0.1815 | 0.9496 |
| 0.2022 | 1.0126 |
| 0.2219 | 1.0667 |
| 0.2406 | 1.1127 |
| 0.2627 | 1.1612 |
| 0.2820 | 1.2112 |
| 0.2889 | 1.2255 |
| 0.2962 | 1.2398 |
| 0.3038 | 1.2544 |
| 0.3118 | 1.2688 |
| 0.3202 | 1.2833 |
| 0.3291 | 1.2967 |
| 0.3373 | 1.309 |
| 0.3460 | 1.3206 |
| 0.3550 | 1.3325 |
| 0.3646 | 1.3435 |
| 0.3747 | 1.3546 |
| 0.3853 | 1.3653 |
| 0.3954 | 1.3748 |
| 0.4059 | 1.3833 |
| 0.4170 | 1.3916 |
| 0.4262 | 1.3952 |
| 0.4357 | 1.3988 |
| 0.4457 | 1.402 |
| 0.4562 | 1.4046 |
| 0.4671 | 1.4061 |
| 0.4787 | 1.406 |
| 0.4907 | 1.405 |
| 0.5034 | 1.402 |
| 0.5144 | 1.3979 |
| 0.5258 | 1.3925 |
| 0.5377 | 1.386 |
| 0.5502 | 1.3795 |
| 0.5633 | 1.3703 |
| 0.5771 | 1.3591 |
| 0.5893 | 1.347 |
| 0.6020 | 1.331 |
| 0.6153 | 1.3145 |
| 0.6292 | 1.2964 |
| 0.6437 | 1.2738 |
| 0.6589 | 1.2497 |
| 0.6721 | 1.2244 |
| 0.6857 | 1.1966 |
| 0.6999 | 1.1664 |
| 0.7147 | 1.132 |
| 0.7287 | 1.0981 |
| 0.7433 | 1.0611 |
| 0.7584 | 1.0204 |
| 0.7742 | 0.9753 |
| 0.7907 | 0.9250 |
| 0.8078 | 0.8706 |
| 0.8233 | 0.8180 |
| 0.8393 | 0.7582 |
| 0.8560 | 0.6956 |
| 0.8733 | 0.6270 |
| 0.8914 | 0.5515 |
| 0.9102 | 0.4682 |
| 0.9269 | 0.3895 |
| 0.9411 | 0.3035 |
| 0.9620 | 0.2062 |
| 0.9807 | 0.1108 |
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 |
|---|---|
| 0.0307 | 0.2323 |
| 0.0596 | 0.4155 |
| 0.0868 | 0.5629 |
| 0.1125 | 0.6839 |
| 0.1368 | 0.7899 |
| 0.1597 | 0.8764 |
| 0.1815 | 0.9496 |
| 0.2022 | 1.0126 |
| 0.2219 | 1.0667 |
| 0.2406 | 1.1127 |
| 0.2627 | 1.1612 |
| 0.2820 | 1.2112 |
| 0.2889 | 1.2255 |
| 0.2962 | 1.2398 |
| 0.3038 | 1.2544 |
| 0.3118 | 1.2688 |
| 0.3202 | 1.2833 |
| 0.3291 | 1.2967 |
| 0.3373 | 1.309 |
| 0.3460 | 1.3206 |
| 0.3550 | 1.3325 |
| 0.3646 | 1.3435 |
| 0.3747 | 1.3546 |
| 0.3853 | 1.3653 |
| 0.3954 | 1.3748 |
| 0.4059 | 1.3833 |
| 0.4170 | 1.3916 |
| 0.4262 | 1.3952 |
| 0.4357 | 1.3988 |
| 0.4457 | 1.402 |
| 0.4562 | 1.4046 |
| 0.4671 | 1.4061 |
| 0.4787 | 1.406 |
| 0.4907 | 1.405 |
| 0.5034 | 1.402 |
| 0.5144 | 1.3979 |
| 0.5258 | 1.3925 |
| 0.5377 | 1.386 |
| 0.5502 | 1.3795 |
| 0.5633 | 1.3703 |
| 0.5771 | 1.3591 |
| 0.5893 | 1.347 |
| 0.6020 | 1.331 |
| 0.6153 | 1.3145 |
| 0.6292 | 1.2964 |
| 0.6437 | 1.2738 |
| 0.6589 | 1.2497 |
| 0.6721 | 1.2244 |
| 0.6857 | 1.1966 |
| 0.6999 | 1.1664 |
| 0.7147 | 1.132 |
| 0.7287 | 1.0981 |
| 0.7433 | 1.0611 |
| 0.7584 | 1.0204 |
| 0.7742 | 0.9753 |
| 0.7907 | 0.9250 |
| 0.8078 | 0.8706 |
| 0.8233 | 0.8180 |
| 0.8393 | 0.7582 |
| 0.8560 | 0.6956 |
| 0.8733 | 0.6270 |
| 0.8914 | 0.5515 |
| 0.9102 | 0.4682 |
| 0.9269 | 0.3895 |
| 0.9411 | 0.3035 |
| 0.9620 | 0.2062 |
| 0.9807 | 0.1108 |