Abstract
A new approach for the design of sliding mode controllers based on a first-order-plus-deadtime model of the process, is developed. This approach results in a fixed structure controller with a set of tuning equations as a function of the characteristic parameters of the model. The controller performance is judged by simulations on two nonlinear chemical processes
| Original language | English |
|---|---|
| Pages (from-to) | 205-218 |
| Number of pages | 14 |
| Journal | ISA Transactions |
| Volume | 39 |
| Issue number | 2 |
| DOIs | |
| State | Published - 2000 |
| Externally published | Yes |
Keywords
- Nonlinear chemical processes
- Sliding mode control
- Variable structure control
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