Abstract
For the batch crystallization process, the tracking of temperature trajectory, which involves severe nonlinear and non-stationary features, is somewhat difficult to achieve. In this paper, three model-based control strategies, globally linearizing control, generic model control and multi-model based model predictive control, are applied to a batch crystallization process. Simulation results show that all three model-based controllers can provide superior trajectory tracking, disturbance rejection capability and robustness to the modelling errors in the process model as compared with conventional PI controller.
| Original language | English |
|---|---|
| Pages (from-to) | 456-464 |
| Number of pages | 9 |
| Journal | Journal of Chemical Engineering of Japan |
| Volume | 32 |
| Issue number | 4 |
| DOIs | |
| Publication status | Published - Aug 1999 |
| Externally published | Yes |
Keywords
- Batch Crystallization Process
- Batch Process Control
- Generic Model Control
- Globally Linearizing Control
- Model Predictive Control
ASJC Scopus subject areas
- General Chemistry
- General Chemical Engineering