A nonequilibrium model for three-phase distillation in a packed column: Modelling and experiments-Reference-Cited by-同舟云学术

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A nonequilibrium model for three-phase distillation in a packed column: Modelling and experiments

Published:2003 Issue: Volume: Page:881-886
ISSN:1570-7946
Container-title:Computer Aided Chemical Engineering
language:
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Author:

Repke Jens-Uwe,Villain Olivier,Wozny Günter

Publisher

Elsevier

Reference7 articles.

1. Application of the Rate-Based Approach to Three-Phase Distillation Columns;Eckert;Ind. Eng. Computers Chem. Engng.,1999

2. Modelling Mass Transfer in Three-Phase Distillation;Lao;Ind. Eng. Chem. Res.,1994

3. A Nonequilibrium Model for Three-Phase Distillation in a Packed Column;Repke;ADCHEM 2000, Pisa, Italy, 14.-16.06.2000,2000

4. Experimental Investigations of Three-Phase Distillation in a Packed Column;Repke;Chem. Eng. Techn.,2002

5. Experimentelle und theoretische Analyse der Dreiphasenrektifikation in Packungs- und Bodenkolonnen;Repke,2002

Cited by 1 articles. 订阅此论文施引文献订阅此论文施引文献，注册后可以免费订阅5篇论文的施引文献，订阅后可以查看论文全部施引文献

1. Fluid dynamics in multiphase distillation processes in packed towers;Computers & Chemical Engineering;2005-05

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