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 |
|---|---|
| 0.0274 | 0.2006 |
| 0.0533 | 0.3611 |
| 0.0779 | 0.4921 |
| 0.1012 | 0.6018 |
| 0.1234 | 0.6945 |
| 0.1445 | 0.7733 |
| 0.1681 | 0.8511 |
| 0.1904 | 0.9164 |
| 0.2115 | 0.9720 |
| 0.2316 | 1.0317 |
| 0.2372 | 1.0456 |
| 0.2431 | 1.0584 |
| 0.2493 | 1.0718 |
| 0.2559 | 1.0857 |
| 0.2628 | 1.0993 |
| 0.2691 | 1.1112 |
| 0.2757 | 1.124 |
| 0.2826 | 1.1369 |
| 0.2899 | 1.1498 |
| 0.2975 | 1.1629 |
| 0.3056 | 1.1757 |
| 0.3129 | 1.1863 |
| 0.3204 | 1.1966 |
| 0.3284 | 1.2076 |
| 0.3368 | 1.2172 |
| 0.3456 | 1.2283 |
| 0.3548 | 1.2378 |
| 0.3630 | 1.2458 |
| 0.3715 | 1.2537 |
| 0.3805 | 1.2613 |
| 0.3899 | 1.2684 |
| 0.3998 | 1.2748 |
| 0.4012 | 1.2804 |
| 0.4103 | 1.2852 |
| 0.4199 | 1.2892 |
| 0.4299 | 1.2925 |
| 0.4404 | 1.2951 |
| 0.4514 | 1.2966 |
| 0.4630 | 1.2983 |
| 0.4734 | 1.2968 |
| 0.4843 | 1.2957 |
| 0.4958 | 1.2921 |
| 0.5077 | 1.2883 |
| 0.5203 | 1.2832 |
| 0.5335 | 1.2752 |
| 0.5453 | 1.266 |
| 0.5575 | 1.2566 |
| 0.5703 | 1.2443 |
| 0.5838 | 1.2311 |
| 0.5979 | 1.2145 |
| 0.6126 | 1.1966 |
| 0.6261 | 1.1771 |
| 0.6401 | 1.157 |
| 0.6548 | 1.1325 |
| 0.6702 | 1.107 |
| 0.6863 | 1.0782 |
| 0.7032 | 1.0433 |
| 0.7185 | 1.0109 |
| 0.7345 | 0.9727 |
| 0.7512 | 0.9328 |
| 0.7686 | 0.8889 |
| 0.7869 | 0.8368 |
| 0.8038 | 0.7860 |
| 0.8214 | 0.7325 |
| 0.8397 | 0.6710 |
| 0.8589 | 0.6061 |
| 0.8790 | 0.5312 |
| 0.9001 | 0.4513 |
| 0.9185 | 0.3740 |
| 0.9376 | 0.2928 |
| 0.9575 | 0.2041 |
| 0.9783 | 0.1068 |
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 |
|---|---|
| 0.0274 | 0.2006 |
| 0.0533 | 0.3611 |
| 0.0779 | 0.4921 |
| 0.1012 | 0.6018 |
| 0.1234 | 0.6945 |
| 0.1445 | 0.7733 |
| 0.1681 | 0.8511 |
| 0.1904 | 0.9164 |
| 0.2115 | 0.9720 |
| 0.2316 | 1.0317 |
| 0.2372 | 1.0456 |
| 0.2431 | 1.0584 |
| 0.2493 | 1.0718 |
| 0.2559 | 1.0857 |
| 0.2628 | 1.0993 |
| 0.2691 | 1.1112 |
| 0.2757 | 1.124 |
| 0.2826 | 1.1369 |
| 0.2899 | 1.1498 |
| 0.2975 | 1.1629 |
| 0.3056 | 1.1757 |
| 0.3129 | 1.1863 |
| 0.3204 | 1.1966 |
| 0.3284 | 1.2076 |
| 0.3368 | 1.2172 |
| 0.3456 | 1.2283 |
| 0.3548 | 1.2378 |
| 0.3630 | 1.2458 |
| 0.3715 | 1.2537 |
| 0.3805 | 1.2613 |
| 0.3899 | 1.2684 |
| 0.3998 | 1.2748 |
| 0.4012 | 1.2804 |
| 0.4103 | 1.2852 |
| 0.4199 | 1.2892 |
| 0.4299 | 1.2925 |
| 0.4404 | 1.2951 |
| 0.4514 | 1.2966 |
| 0.4630 | 1.2983 |
| 0.4734 | 1.2968 |
| 0.4843 | 1.2957 |
| 0.4958 | 1.2921 |
| 0.5077 | 1.2883 |
| 0.5203 | 1.2832 |
| 0.5335 | 1.2752 |
| 0.5453 | 1.266 |
| 0.5575 | 1.2566 |
| 0.5703 | 1.2443 |
| 0.5838 | 1.2311 |
| 0.5979 | 1.2145 |
| 0.6126 | 1.1966 |
| 0.6261 | 1.1771 |
| 0.6401 | 1.157 |
| 0.6548 | 1.1325 |
| 0.6702 | 1.107 |
| 0.6863 | 1.0782 |
| 0.7032 | 1.0433 |
| 0.7185 | 1.0109 |
| 0.7345 | 0.9727 |
| 0.7512 | 0.9328 |
| 0.7686 | 0.8889 |
| 0.7869 | 0.8368 |
| 0.8038 | 0.7860 |
| 0.8214 | 0.7325 |
| 0.8397 | 0.6710 |
| 0.8589 | 0.6061 |
| 0.8790 | 0.5312 |
| 0.9001 | 0.4513 |
| 0.9185 | 0.3740 |
| 0.9376 | 0.2928 |
| 0.9575 | 0.2041 |
| 0.9783 | 0.1068 |