Özet
In this study, the control performance of a reactive distillation column with double reactive sections is evaluated. The reactions taking place in the column are two-stage consecutive reversible liquid-phase reactions. A hypothetical ideal reaction system is selected as case study. Different control structures including temperature and/or composition control loops are developed and tested for different load disturbances. The closed loop results of different control structures demonstrate that a workable control structure should include direct control of compositions. A control structure with two temperature controllers and two composition controllers provides an effective control for the column with double reactive sections.
| Orijinal dil | İngilizce |
|---|---|
| Sayfa (başlangıç-bitiş) | 86-93 |
| Sayfa sayısı | 8 |
| Dergi | Chemical Engineering and Processing - Process Intensification |
| Hacim | 113 |
| DOI'lar | |
| Yayın durumu | Yayınlandı - 2017 |
Bibliyografik not
Publisher Copyright:© 2016 Elsevier B.V.
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