## Abstract The static estimator of part I is incorporated into a dynamic control system. The system structure minimizes output feedback and thereby achieves stability even in the event of significant modeling errors. This inherent stability permits the use of simple and economical leadโlag compens
Inferential control of processes: Part III. Construction of optimal and suboptimal dynamic estimators
โ Scribed by Babu Joseph; Coleman Brosilow
- Publisher
- American Institute of Chemical Engineers
- Year
- 1978
- Tongue
- English
- Weight
- 961 KB
- Volume
- 24
- Category
- Article
- ISSN
- 0001-1541
No coin nor oath required. For personal study only.
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