Abstract
This article proposes the use of a sliding mode controller based on a first-order-plus-deadtime model of the system for controlling higher-order chemical processes with inverse response. The controller has a simple and fixed structure with a set of tuning equations as a function of the characteristic parameters of the first order-plus-deadtime model. The controller performance was judged via computer simulations using linear and nonlinear models of chemical processes with inverse response.
| Original language | English |
|---|---|
| Pages (from-to) | 55-72 |
| Number of pages | 18 |
| Journal | ISA Transactions |
| Volume | 38 |
| Issue number | 1 |
| DOIs | |
| State | Published - Jan 1999 |
| Externally published | Yes |
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