Resumen
A binary distillation column modeled by nonlinear differential equations is controlled by means of a state feedback and feedforward control law that eliminates the effect of disturbances on the process output. The control scheme needs a state vector observer; so an asymptotic state observer is included in the control structure. The results obtained in simulation are shown.
Idioma original | Inglés |
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Páginas (desde-hasta) | 2090-2091 |
Número de páginas | 2 |
Publicación | Proceedings of the American Control Conference |
Estado | Publicada - 1987 |
Publicado de forma externa | Sí |