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 |