Conceptual design of single-feed hybrid reactive distillation columns

被引:21
作者
Dragomir, RM [1 ]
Jobson, M [1 ]
机构
[1] Univ Manchester, Sch Chem Engn & Analyt Sci, Ctr Proc Integrat, Manchester M60 1QD, Lancs, England
关键词
chemical processes; design; reactive distillation; hybrid column; process synthesis; stage composition lines;
D O I
10.1016/j.ces.2005.03.009
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
It is well known that reactive distillation offers benefits by integrating distillation and reaction within a single unit. While there are procedures available for the synthesis of non-reactive distillation processes and of reaction-separation systems, the design of reactive distillation columns is still a challenge. This work presents a new synthesis and design methodology for hybrid reactive distillation columns, featuring both reactive and non-reactive sections; reactive equilibrium is assumed. The approach is based on graphical techniques; therefore it is restricted to systems with two degrees of freedom according to Gibbs phase rule. The design method allows rapid and relatively simple screening of different reactive distillation column configurations. The results are useful for initialising more rigorous calculations. The methodology is illustrated for MTBE and ethyl formate production. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4377 / 4395
页数:19
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