## Abstract Chemical and biological fedβbatch stirred tank reactors (FSTRs) are often good candidates for the application of adaptive nonβlinear control techniques because in many cases their dynamical models include highly uncertain kinetic parameters. A general unified methodology for the design
Process dynamics and temperature control of fed-batch reactors
β Scribed by F. Szeifert; T. Chovan; L. Nagy
- Publisher
- Elsevier Science
- Year
- 1995
- Tongue
- English
- Weight
- 453 KB
- Volume
- 19
- Category
- Article
- ISSN
- 0098-1354
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