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The control of both bottom and distillate compositions is achieved by using conventional two point feedback control (WoodandBerry1) and non-interacting control (WoodandBerry2). Because of coupling, conventional control has a poorer performance when compared to the non interacting control system. Feed is regarded as a perturbation that is properly rejected by the non interacting control system. Transfer functions are taken from the book of Jean-Pierre Corriou (Commande des Procédés, Génie des Procédés de l?Ecole de Nancy, 1996) or in R. K. WOOD and M. W. BERRY, Terminal composition control of a binary distillation column, Chemical Engineering Science, 1973, Vol. 28, pp. 1707-1717.
Cita come
Housam Binous (2026). Control of the Wood and Berry Distillation Column Using Simulink (https://it.mathworks.com/matlabcentral/fileexchange/12132-control-of-the-wood-and-berry-distillation-column-using-simulink), MATLAB Central File Exchange. Recuperato .
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- Versione 1.0.0.0 (21,4 KB)
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| Versione | Pubblicato | Note della release | Action |
|---|---|---|---|
| 1.0.0.0 |
