## Abstract Nonstationary dynamics, finite‐time operation, large thermodynamical uncertainty and delayed composition measurements make the control of batch distillation processes a challenging and interesting problem. In this paper, a cascade control design to regulate the overhead composition of a
Dynamic rate-based model for multicomponent batch distillation
✍ Scribed by L. U. Kreul; A. Górak; P. I. Barton
- Publisher
- American Institute of Chemical Engineers
- Year
- 1999
- Tongue
- English
- Weight
- 465 KB
- Volume
- 45
- Category
- Article
- ISSN
- 0001-1541
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