Dynamics and control of benzene hydrogenation via reactive distillation

被引:12
作者
Mahindrakar, Vishal [1 ]
Hahn, Juergen [1 ,2 ]
机构
[1] Rensselaer Polytech Inst, Dept Chem & Biol Engn, Troy, NY 12180 USA
[2] Rensselaer Polytech Inst, Dept Biomed Engn, Troy, NY 12180 USA
关键词
Reactive distillation; Packed column; Dynamic modeling; Feedback control; Feedforward control; CONTROL CONFIGURATION; COLUMNS; RECYCLE; MODELS; EQUILIBRIUM; SIMULATION; SYSTEMS; DESIGN; MTBE; TAME;
D O I
10.1016/j.jprocont.2014.01.005
中图分类号
TP [自动化技术、计算机技术];
学科分类号
0812 ;
摘要
This work develops a dynamic, first principles-based model of a reactive distillation column used for benzene hydrogenation of a reformate stream and investigates different control structures for this process. The model is used initially to develop and evaluate a feedback control strategy which provides good regulatory performance for small disturbances, however, it tends to be sluggish for significant disturbances in the feed composition. In order to address this point, adding a feedforward controller to the feedback structure has also been investigated. However, the feedforward controller can only be implemented if composition measurements of the feed are taken. As online composition measurements are expensive in practice, several different scenarios have been investigated where samples of the feed are taken and subsequently analyzed in a lab, as represented by measurement time delays. Simulation results show that adding feedforward control to the feedback scheme can be very beneficial for this process, however, this is only the case if the composition disturbance measurements do not involve a significant time delay. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:113 / 124
页数:12
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