Resumen
This paper proposes a modified Smith predictor scheme for temperature control during the formulation of injectable drugs in chemical reactors. The dynamic model of this process is obtained from an identification procedure applied in a real chemical reactor of the pharmaceutical industry. This identification procedure yields a second order with dominant time delay transfer function. A PI controller combined with a modified Smith predictor is therefore designed which behaves robustly against the effect of measured or unmeasured external disturbances. Simulated results compare the performance of the proposed controller with a standard PI controller, also combined with a conventional Smith predictor, and with Astrom modified Smith predictor. Four performance indexes have been used in this comparison: three related to the output performance (settling time, overshooting, and IAE), and a fourth one related to the control effort (EU). The analysis of these indexes shows that the proposed controller provides lower values of the compared indexes.
| Idioma original | Inglés |
|---|---|
| Número de artículo | 7106355 |
| Páginas (desde-hasta) | 1041-1047 |
| Número de páginas | 7 |
| Publicación | IEEE Latin America Transactions |
| Volumen | 13 |
| N.º | 4 |
| DOI | |
| Estado | Publicada - 1 abr. 2015 |
| Publicado de forma externa | Sí |
Huella
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