Operational conditions:
| Mole fraction of 2-Decanone (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0282 | 0.1510 |
| 0.0549 | 0.2780 |
| 0.0805 | 0.3850 |
| 0.1041 | 0.4750 |
| 0.1268 | 0.5530 |
| 0.1484 | 0.6200 |
| 0.1741 | 0.6910 |
| 0.1983 | 0.7520 |
| 0.2212 | 0.8030 |
| 0.2427 | 0.8460 |
| 0.2632 | 0.8820 |
| 0.2825 | 0.9110 |
| 0.3044 | 0.9410 |
| 0.3250 | 0.9640 |
| 0.3444 | 0.9830 |
| 0.3628 | 0.9970 |
| 0.3801 | 1.008 |
| 0.3965 | 1.017 |
| 0.4145 | 1.023 |
| 0.4313 | 1.027 |
| 0.4472 | 1.029 |
| 0.4623 | 1.028 |
| 0.4765 | 1.026 |
| 0.4901 | 1.023 |
| 0.5029 | 1.019 |
| 0.5151 | 1.014 |
| 0.5292 | 1.007 |
| 0.5425 | 0.9980 |
| 0.5550 | 0.9890 |
| 0.5669 | 0.9790 |
| 0.5782 | 0.9690 |
| 0.5889 | 0.9580 |
| 0.5991 | 0.9480 |
| 0.6088 | 0.9370 |
| 0.6201 | 0.9240 |
| 0.6308 | 0.9100 |
| 0.6408 | 0.8960 |
| 0.6504 | 0.8830 |
| 0.6594 | 0.8700 |
| 0.6680 | 0.8570 |
| 0.6762 | 0.8440 |
| 0.6840 | 0.8310 |
| 0.7031 | 0.7900 |
| 0.7191 | 0.7630 |
| 0.7334 | 0.7370 |
| 0.7483 | 0.7090 |
| 0.7638 | 0.6780 |
| 0.7799 | 0.6440 |
| 0.7968 | 0.6060 |
| 0.8144 | 0.5650 |
| 0.8298 | 0.5270 |
| 0.8458 | 0.4860 |
| 0.8624 | 0.4420 |
| 0.8797 | 0.3930 |
| 0.8977 | 0.3410 |
| 0.9133 | 0.2930 |
| 0.9294 | 0.2420 |
| 0.9461 | 0.1890 |
| 0.9634 | 0.1300 |
| 0.9814 | 0.0670 |
Operational conditions:
| Mole fraction of 2-Decanone (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0282 | 0.1510 |
| 0.0549 | 0.2780 |
| 0.0805 | 0.3850 |
| 0.1041 | 0.4750 |
| 0.1268 | 0.5530 |
| 0.1484 | 0.6200 |
| 0.1741 | 0.6910 |
| 0.1983 | 0.7520 |
| 0.2212 | 0.8030 |
| 0.2427 | 0.8460 |
| 0.2632 | 0.8820 |
| 0.2825 | 0.9110 |
| 0.3044 | 0.9410 |
| 0.3250 | 0.9640 |
| 0.3444 | 0.9830 |
| 0.3628 | 0.9970 |
| 0.3801 | 1.008 |
| 0.3965 | 1.017 |
| 0.4145 | 1.023 |
| 0.4313 | 1.027 |
| 0.4472 | 1.029 |
| 0.4623 | 1.028 |
| 0.4765 | 1.026 |
| 0.4901 | 1.023 |
| 0.5029 | 1.019 |
| 0.5151 | 1.014 |
| 0.5292 | 1.007 |
| 0.5425 | 0.9980 |
| 0.5550 | 0.9890 |
| 0.5669 | 0.9790 |
| 0.5782 | 0.9690 |
| 0.5889 | 0.9580 |
| 0.5991 | 0.9480 |
| 0.6088 | 0.9370 |
| 0.6201 | 0.9240 |
| 0.6308 | 0.9100 |
| 0.6408 | 0.8960 |
| 0.6504 | 0.8830 |
| 0.6594 | 0.8700 |
| 0.6680 | 0.8570 |
| 0.6762 | 0.8440 |
| 0.6840 | 0.8310 |
| 0.7031 | 0.7900 |
| 0.7191 | 0.7630 |
| 0.7334 | 0.7370 |
| 0.7483 | 0.7090 |
| 0.7638 | 0.6780 |
| 0.7799 | 0.6440 |
| 0.7968 | 0.6060 |
| 0.8144 | 0.5650 |
| 0.8298 | 0.5270 |
| 0.8458 | 0.4860 |
| 0.8624 | 0.4420 |
| 0.8797 | 0.3930 |
| 0.8977 | 0.3410 |
| 0.9133 | 0.2930 |
| 0.9294 | 0.2420 |
| 0.9461 | 0.1890 |
| 0.9634 | 0.1300 |
| 0.9814 | 0.0670 |