Operational condition: Temperature, K = 298.15 (Liquid)
Mole fraction of Valeric anhydride (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0319 | 0.2533 |
0.0618 | 0.4605 |
0.0899 | 0.6220 |
0.1164 | 0.7609 |
0.1414 | 0.8718 |
0.1650 | 0.9694 |
0.1873 | 1.051 |
0.2126 | 1.1326 |
0.2363 | 1.2005 |
0.2587 | 1.2539 |
0.2798 | 1.3009 |
0.2997 | 1.3403 |
0.3186 | 1.3728 |
0.3364 | 1.3998 |
0.3569 | 1.4321 |
0.3714 | 1.4658 |
0.3810 | 1.4748 |
0.3911 | 1.4845 |
0.4020 | 1.4935 |
0.4130 | 1.5012 |
0.4294 | 1.5079 |
0.4312 | 1.5131 |
0.4416 | 1.5165 |
0.4524 | 1.5198 |
0.4638 | 1.5211 |
0.4757 | 1.5224 |
0.4883 | 1.5218 |
0.5015 | 1.5192 |
0.5127 | 1.5166 |
0.5245 | 1.5112 |
0.5369 | 1.5042 |
0.5498 | 1.4953 |
0.5633 | 1.4838 |
0.5776 | 1.4699 |
0.5926 | 1.4543 |
0.6049 | 1.4399 |
0.6178 | 1.4232 |
0.6313 | 1.4022 |
0.6454 | 1.3798 |
0.6601 | 1.3544 |
0.6754 | 1.3255 |
0.6916 | 1.2901 |
0.7052 | 1.2588 |
0.7194 | 1.2258 |
0.7341 | 1.1878 |
0.7495 | 1.1467 |
0.7655 | 1.0985 |
0.7822 | 1.0474 |
0.7997 | 0.9884 |
0.8145 | 0.9360 |
0.8299 | 0.8784 |
0.8459 | 0.8151 |
0.8625 | 0.7459 |
0.8798 | 0.6690 |
0.8978 | 0.5846 |
0.9133 | 0.5068 |
0.9294 | 0.4222 |
0.9461 | 0.3302 |
0.9634 | 0.2297 |
0.9814 | 0.1200 |
Operational condition: Temperature, K = 298.15 (Liquid)
Mole fraction of Valeric anhydride (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0319 | 0.2533 |
0.0618 | 0.4605 |
0.0899 | 0.6220 |
0.1164 | 0.7609 |
0.1414 | 0.8718 |
0.1650 | 0.9694 |
0.1873 | 1.051 |
0.2126 | 1.1326 |
0.2363 | 1.2005 |
0.2587 | 1.2539 |
0.2798 | 1.3009 |
0.2997 | 1.3403 |
0.3186 | 1.3728 |
0.3364 | 1.3998 |
0.3569 | 1.4321 |
0.3714 | 1.4658 |
0.3810 | 1.4748 |
0.3911 | 1.4845 |
0.4020 | 1.4935 |
0.4130 | 1.5012 |
0.4294 | 1.5079 |
0.4312 | 1.5131 |
0.4416 | 1.5165 |
0.4524 | 1.5198 |
0.4638 | 1.5211 |
0.4757 | 1.5224 |
0.4883 | 1.5218 |
0.5015 | 1.5192 |
0.5127 | 1.5166 |
0.5245 | 1.5112 |
0.5369 | 1.5042 |
0.5498 | 1.4953 |
0.5633 | 1.4838 |
0.5776 | 1.4699 |
0.5926 | 1.4543 |
0.6049 | 1.4399 |
0.6178 | 1.4232 |
0.6313 | 1.4022 |
0.6454 | 1.3798 |
0.6601 | 1.3544 |
0.6754 | 1.3255 |
0.6916 | 1.2901 |
0.7052 | 1.2588 |
0.7194 | 1.2258 |
0.7341 | 1.1878 |
0.7495 | 1.1467 |
0.7655 | 1.0985 |
0.7822 | 1.0474 |
0.7997 | 0.9884 |
0.8145 | 0.9360 |
0.8299 | 0.8784 |
0.8459 | 0.8151 |
0.8625 | 0.7459 |
0.8798 | 0.6690 |
0.8978 | 0.5846 |
0.9133 | 0.5068 |
0.9294 | 0.4222 |
0.9461 | 0.3302 |
0.9634 | 0.2297 |
0.9814 | 0.1200 |