Forner, Florian and Brehelin, Mathias and Rouzineau, David and Meyer, Michel and Repke, Jens Uwe Startup of a reactive distillation process with a decanter. (2008) Chemical Engineering and Processing: Process Intensification, vol. 4 (n° 11). 1976 -1985. ISSN 0255-2701
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Official URL: http://dx.doi.org/10.1016/j.cep.2007.09.005
Abstract
The startup of a reactive distillation process for the production of propyl acetate including a decanter is studied. A simulation model is presented which describes the whole startup from a cold and empty state and takes into account the liquid phase split in the decanter. The simulation model is successfully validated with own dynamic experimental data. Different startup strategies are developed and analysed in simulation studies showing the high influence of the initial charging of decanter and reboiler on the startup time.
| Item Type: | Article |
|---|---|
| Additional Information: | Thanks to Elsevier editor. The definitive version is available at http://www.sciencedirect.com The original PDF of the article can be found at Chemical Engineering and Processing: Process Intensification website : http://www.sciencedirect.com/science/journal/02552701 |
| Audience (journal): | International peer-reviewed journal |
| Uncontrolled Keywords: | |
| Institution: | Université de Toulouse > Institut National Polytechnique de Toulouse - INPT Other partners > Technische Universität Berlin - TU Berlin (GERMANY) Université de Toulouse > Université Paul Sabatier-Toulouse III - UPS French research institutions > Centre National de la Recherche Scientifique - CNRS |
| Laboratory name: | Institute of Process and Plant Technology (Berlin, Germany) Laboratoire de Génie Chimique - LGC (Toulouse, France) - Réaction, mélange & séparation (RMS) |
| Statistics: | download |
| Total amount of citations (from ISI Web of Science): | 3 |
| Deposited By: | Hélène Dubernard |
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