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Extending Batch Extractive Distillation Thermodynamic Feasibility Insights to Continuous for Class 1.0-2 Case A

Benyounes, Hassiba and Shen, Weifeng and Gerbaud, Vincent Extending Batch Extractive Distillation Thermodynamic Feasibility Insights to Continuous for Class 1.0-2 Case A. (2011) In: 2nd International Conference on Chemistry and Chemical Engineering (ICCCE), 2011, 29-31 Jul 2011, Chengdu, China .

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Official URL: http://www.etlibrary.org/?m=fbook&a=details&aid=3595

Abstract

The feasibility of batch and continuous extractive distillation analysis for the separation azeotropic mixtures is addressed. Based on batch feasibility knowledge, batch and continuous separation feasibility is studied under reflux ratio and entrainer flow-rate for a working example ternary system acetone-chloroform-benzene, which belonging to the 1.0-2 class case (a). Possible feasible regions are determined by finding the feasible points based on continuous methodology, they show minimum and maximum feed ratio as a function of the reflux, and a lower bound for the reflux ratio. Later on, simulations verified the feasibility of calculating results based on theoretical methodology

Item Type:Conference or Workshop Item (Speech)
Additional Information:Thanks to IACSIT Press. This conference article of ICCCE 2011 is availbale in the volume 14, pp. 84-88 - ISBN 978-981-08-9082-7
Audience (conference):International conference proceedings
Uncontrolled Keywords:
Institution:French research institutions > Centre National de la Recherche Scientifique - CNRS (FRANCE)
Université de Toulouse > Institut National Polytechnique de Toulouse - INPT (FRANCE)
Université de Toulouse > Université Paul Sabatier-Toulouse III - UPS (FRANCE)
Other partners > Université des Sciences et de la Technologie Mohamed Boudiaf d'Oran - USTO (ALGERIA)
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Deposited By: Vincent GERBAUD
Deposited On:20 Dec 2012 14:53

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