Abstract
This paper presents the nonlinear dynamic analysis of an ideal two-reactant-two product reactive distillation. The impact of disturbance magnitudes and directions on openloop stability of the system is studied. An analysis of the physicochemical phenomena present in reactive distillation processes that, under certain operational conditions, causes special types of nonlinear behavior is carried. Operating two-reactant-two-product reactive distillation with excess of heavy reactant is found to enhance openloop stability, but decreases the products purity. However, excess of more volatile reactant drifts the system to another state. It is found that openloop reactive distillation system has a better dynamics when operated with fixing reflux ratio instead of reflux rate.
| Original language | English |
|---|---|
| Pages (from-to) | 811-816 |
| Number of pages | 6 |
| Journal | Computer Aided Chemical Engineering |
| Volume | 20 |
| Issue number | C |
| DOIs | |
| State | Published - 2005 |
Bibliographical note
Funding Information:The authors would like to acknowledge the support of King Fahd University of Petroleum & Minerals for funding this research.
Keywords
- Reactive distillation
- nonlinear dynamic simulation
- system stability
ASJC Scopus subject areas
- General Chemical Engineering
- Computer Science Applications
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