Novel operational strategy for the separation of ternary mixtures via cyclic operation of a batch distillation column with side withdrawal-Reference-Cited by-同舟云学术

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Novel operational strategy for the separation of ternary mixtures via cyclic operation of a batch distillation column with side withdrawal

Published:2003 Issue: Volume: Page:629-634
ISSN:1570-7946
Container-title:Computer Aided Chemical Engineering
language:
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Author:

Demicoli D.,Stichlmair J.

Publisher

Elsevier

Reference4 articles.

1. Comparison of regular and inverted batch distillation;Sørensen;Chem. Engng. Sci.,1996

2. A cyclic operating policy for batch distillation—Theory and practice;Sørensen;Comp. Chem. Engng.,1997

3. Batch distillation of zeotropic mixtures in a column with a middle vessel;Warter;Comp. Aided Chem. Engng.,2002

4. Total reflux operation of multivessel batch distillation;Wittgens;Comp. Chem. Engng.,1996

Cited by 3 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. A review of ternary azeotropic mixtures advanced separation strategies;Theoretical Foundations of Chemical Engineering;2016-01

2. Extension of Thermodynamic Insights on Batch Extractive Distillation to Continuous Operation. 2. Azeotropic Mixtures with a Light Entrainer;Industrial & Engineering Chemistry Research;2013-03-12

3. Separation of ternary mixtures in a batch distillation column with side withdrawal;Computers & Chemical Engineering;2004-05

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