Shortcut design of reactive distillation columns

被引:20
作者
Avami, Akram [2 ]
Marquardt, Wolfgang [3 ]
Saboohi, Yadollah [1 ]
Kraemer, Korbinian [3 ]
机构
[1] Sharif Univ Technol, SERI, Tehran, Iran
[2] Sharif Univ Technol, Dept Mech Engn, Tehran, Iran
[3] Rhein Westfal TH Aachen, Aachen, Germany
关键词
Chemical processes; Distillation; Reaction engineering; Reactive distillation; Pinch points; Energy demand; MINIMUM-REFLUX CALCULATIONS; NONIDEAL MULTICOMPONENT DISTILLATION; METHYL ACETATE; MINLP OPTIMIZATION; CHEMICAL-REACTIONS; FEASIBLE PRODUCTS; CONCEPTUAL DESIGN; SYSTEMS; EQUILIBRIUM; MIXTURES;
D O I
10.1016/j.ces.2011.12.021
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Shortcut design methods can be valuable tools for rapid screening of different separation process alternatives to assess feasibility and determine minimum energy demand. This work presents a variant of the feed angle method (Kraemer et al., 2011), which applies to single- and double-feed reactive distillation columns. The proposed method relies on pinch point analysis and determines the minimum energy demand from the calculation of a tray at the feed pinch. It is fully algorithmic and insensitive to impurities in product specifications. Its validity and performance is illustrated by a variety of case studies covering multi-component and multi-reaction systems, mixtures with potential liquid-liquid phase split, and double-feed columns. The results show that the method is sufficiently accurate and computationally efficient, even for highly non-ideal systems and complex configurations. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:166 / 177
页数:12
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