Operational conditions:
| Mole fraction of 2-Octanone (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0446 | 0.2501 |
| 0.0854 | 0.4468 |
| 0.1228 | 0.6044 |
| 0.1573 | 0.7311 |
| 0.1926 | 0.8448 |
| 0.2251 | 0.9341 |
| 0.2550 | 1.0081 |
| 0.2827 | 1.0652 |
| 0.3084 | 1.1109 |
| 0.3324 | 1.1473 |
| 0.3585 | 1.1807 |
| 0.3826 | 1.2053 |
| 0.4050 | 1.2233 |
| 0.4258 | 1.2359 |
| 0.4480 | 1.2452 |
| 0.4685 | 1.2493 |
| 0.4876 | 1.25 |
| 0.4933 | 1.2544 |
| 0.5044 | 1.2546 |
| 0.5161 | 1.2528 |
| 0.5282 | 1.2504 |
| 0.5410 | 1.2461 |
| 0.5519 | 1.2421 |
| 0.5633 | 1.236 |
| 0.5751 | 1.2291 |
| 0.5874 | 1.2194 |
| 0.6003 | 1.2087 |
| 0.6138 | 1.1958 |
| 0.6257 | 1.1825 |
| 0.6508 | 1.1502 |
| 0.6642 | 1.1308 |
| 0.6781 | 1.1085 |
| 0.6926 | 1.0835 |
| 0.7048 | 1.061 |
| 0.7174 | 1.0368 |
| 0.7370 | 1.0087 |
| 0.7443 | 0.9789 |
| 0.7583 | 0.9449 |
| 0.7732 | 0.9079 |
| 0.7861 | 0.8732 |
| 0.7993 | 0.8369 |
| 0.8131 | 0.7962 |
| 0.8273 | 0.7528 |
| 0.8400 | 0.7108 |
| 0.8531 | 0.6667 |
| 0.8666 | 0.6178 |
| 0.8805 | 0.5661 |
| 0.8949 | 0.5095 |
| 0.9075 | 0.4570 |
| 0.9204 | 0.4019 |
| 0.9337 | 0.3427 |
| 0.9473 | 0.2789 |
| 0.9614 | 0.2089 |
| 0.9739 | 0.1448 |
| 0.9868 | 0.0742 |
Operational conditions:
| Mole fraction of 2-Octanone (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0446 | 0.2501 |
| 0.0854 | 0.4468 |
| 0.1228 | 0.6044 |
| 0.1573 | 0.7311 |
| 0.1926 | 0.8448 |
| 0.2251 | 0.9341 |
| 0.2550 | 1.0081 |
| 0.2827 | 1.0652 |
| 0.3084 | 1.1109 |
| 0.3324 | 1.1473 |
| 0.3585 | 1.1807 |
| 0.3826 | 1.2053 |
| 0.4050 | 1.2233 |
| 0.4258 | 1.2359 |
| 0.4480 | 1.2452 |
| 0.4685 | 1.2493 |
| 0.4876 | 1.25 |
| 0.4933 | 1.2544 |
| 0.5044 | 1.2546 |
| 0.5161 | 1.2528 |
| 0.5282 | 1.2504 |
| 0.5410 | 1.2461 |
| 0.5519 | 1.2421 |
| 0.5633 | 1.236 |
| 0.5751 | 1.2291 |
| 0.5874 | 1.2194 |
| 0.6003 | 1.2087 |
| 0.6138 | 1.1958 |
| 0.6257 | 1.1825 |
| 0.6508 | 1.1502 |
| 0.6642 | 1.1308 |
| 0.6781 | 1.1085 |
| 0.6926 | 1.0835 |
| 0.7048 | 1.061 |
| 0.7174 | 1.0368 |
| 0.7370 | 1.0087 |
| 0.7443 | 0.9789 |
| 0.7583 | 0.9449 |
| 0.7732 | 0.9079 |
| 0.7861 | 0.8732 |
| 0.7993 | 0.8369 |
| 0.8131 | 0.7962 |
| 0.8273 | 0.7528 |
| 0.8400 | 0.7108 |
| 0.8531 | 0.6667 |
| 0.8666 | 0.6178 |
| 0.8805 | 0.5661 |
| 0.8949 | 0.5095 |
| 0.9075 | 0.4570 |
| 0.9204 | 0.4019 |
| 0.9337 | 0.3427 |
| 0.9473 | 0.2789 |
| 0.9614 | 0.2089 |
| 0.9739 | 0.1448 |
| 0.9868 | 0.0742 |