Abstract
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.
| Original language | English |
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| Pages (from-to) | 2090-2091 |
| Number of pages | 2 |
| Journal | Proceedings of the American Control Conference |
| State | Published - 1987 |
| Externally published | Yes |