| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 4998369 | Chemical Engineering and Processing: Process Intensification | 2016 | 18 Pages |
Abstract
The dynamic controllability of this highly heat integrated and interacting process is studied in this paper. A detailed dynamic simulation is constructed, and an effective control structure is developed that handles large disturbances in throughput and feed composition. The numerical example considers the dehydration of tert-butanol using cyclohexane as the entrainer in heterogeneous azeotropic distillation.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Process Chemistry and Technology
Authors
William L. Luyben,