Расчеты и прогнозирование свойств органических соединений
Корреляция Риделя
где 
приведенная температура кипения.
| А | В | С | D | θ | αc | ψ |
| 15,0009 | 15,4295 | -9,1285 | 0,4286 | -0,4286 | 8,87251 | 0,816197 |
| Т | Тr | Pvp,r | Pvp, bar |
| 298 | 0,44 | 0.0000 | 0.0001 |
| 323 | 0,48 | 0.0000 | 0.0006 |
| 348 | 0,52 | 0.0001 | 0.0029 |
| 373 | 0,55 | 0.0006 | 0.0114 |
| 398 | 0,59 | 0.0018 | 0.0367 |
| 423 | 0,63 | 0.0050 | 0.0993 |
| 448 | 0,66 | 0.0117 | 0.2343 |
| 473 | 0,70 | 0.0247 | 0.4938 |
| 498 | 0,74 | 0.0474 | 0.9479 |
| 523 | 0,78 | 0.0842 | 1.6843 |
| 548 | 0,81 | 0.1404 | 2.8081 |
| 573 | 0,85 | 0.2221 | 4.4426 |
| 598 | 0,89 | 0.3368 | 6.7356 |
| 623 | 0,92 | 0.4936 | 9.8713 |
| 648 | 0,96 | 0.7046 | 14.0926 |
Корреляция Амброуза-Уолтона.
где 
| Т | Тr | τ | f(0) | f(1) | f(2) | Pvp,r | Pvp, bar |
| 298 | 0.44 | 0.56 | -6.7645 | -9.0581 | -0.3883 | 0.0000 | 0.0001 |
| 323 | 0.48 | 0.52 | -5.8078 | -7.4026 | -0.2935 | 0.0000 | 0.0006 |
| 348 | 0.52 | 0.48 | -4.9973 | -6.0773 | -0.2119 | 0.0002 | 0.0031 |
| 373 | 0.55 | 0.45 | -4.3019 | -5.0038 | -0.1440 | 0.0006 | 0.0122 |
| 398 | 0.59 | 0.41 | -3.6985 | -4.1249 | -0.0898 | 0.0019 | 0.0388 |
| 423 | 0.63 | 0.37 | -3.1695 | -3.3981 | -0.0484 | 0.0052 | 0.1041 |
| 448 | 0.66 | 0.34 | -2.7013 | -2.7913 | -0.0187 | 0.0122 | 0.2433 |
| 473 | 0.70 | 0.30 | -2.2836 | -2.2799 | 0.0007 | 0.0254 | 0.5082 |
| 498 | 0.74 | 0.26 | -1.9077 | -1.8451 | 0.0113 | 0.0484 | 0.9684 |
| 523 | 0.78 | 0.22 | -1.5672 | -1.4721 | 0.0147 | 0.0855 | 1.7109 |
| 548 | 0.81 | 0.19 | -1.2565 | -1.1492 | 0.0128 | 0.1420 | 2.8398 |
| 573 | 0.85 | 0.15 | -0.9710 | -0.8672 | 0.0073 | 0.2239 | 4.4772 |
| 598 | 0.89 | 0.11 | -0.7070 | -0.6183 | 0.0003 | 0.3383 | 6.7669 |
| 623 | 0.92 | 0.08 | -0.4610 | -0.3962 | -0.0059 | 0.4943 | 9.8860 |
| 648 | 0.96 | 0.04 | -0.2297 | -0.1948 | -0.0083 | 0.7036 | 14.0725 |
