Abstract
Based on the element mass balance concept, a graphical design method and a stage-to-stage multicomponent design method for reactive distillation columns have been developed. For distillation columns comprising reactive and non-reactive stages, a simple design strategy based on reactive and non-reactive bubble point calculations is proposed. This strategy tracks the conversion and temperature between the feed and the end stages of the column. An illustrative example highlights the verification of the design strategy through rigorous simulation.
| Original language | English |
|---|---|
| Title of host publication | European Symposium on Computer Aided Process Engineering - 11 : 34th European symposium of the Working Party on Computer Aided Process Engineering : ESCAPE-11, 27-30 May, 2001, Kolding, Denmark |
| Number of pages | 1186 |
| Publisher | Elsevier |
| Publication date | 2001 |
| Pages | 517-522 |
| ISBN (Print) | 0-44450-70-94 |
| DOIs | |
| Publication status | Published - 2001 |
| Event | 11th European Symposium on Computer Aided Process Engineering: 34th European symposium of the Working Party on Computer Aided Process Engineering - Kolding, Denmark Duration: 27 May 2001 → 30 May 2001 Conference number: 11 |
Conference
| Conference | 11th European Symposium on Computer Aided Process Engineering |
|---|---|
| Number | 11 |
| Country/Territory | Denmark |
| City | Kolding |
| Period | 27/05/2001 → 30/05/2001 |
| Series | Computer Aided Chemical Engineering |
|---|---|
| Volume | 9 |
| ISSN | 1570-7946 |
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