The temperature control of a solution polymerization reactor with different control algorithms is considered. The plant is characterized by strong nonlinear static and open-loop unstable dynamic behavior; additional difficulties arise from control-variable (cooling oil flow rate) constraints and the
β¦ LIBER β¦
Model predictive control of an open-loop unstable train of polymerization reactors
β Scribed by F. Gobin; L.C. Zullo; J.-P. Calvet
- Publisher
- Elsevier Science
- Year
- 1994
- Tongue
- English
- Weight
- 310 KB
- Volume
- 18
- Category
- Article
- ISSN
- 0098-1354
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