Model predictive control of integrated unit operations: Control of a divided wall column

被引:92
作者
Adrian, T
Schoenmakers, H
Boll, M
机构
[1] Mannheim Univ Appl Sci, Dept Proc Engn, D-68163 Mannheim, Germany
[2] BASF AG, GCT A L540, D-67056 Ludwigshafen, Germany
[3] BASF AG, DWF AM L440, D-67056 Ludwigshafen, Germany
关键词
chemical processes; divided wall column; model predictive controller;
D O I
10.1016/S0255-2701(03)00114-4
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The integration of several unit operations into one common apparatus (process intensification) has the potential to substantially improve the economics of chemical processes if applied to adequate problems. On the other hand, the integration typically causes strong interactions of different process quantities and a loss in degrees of freedom. This may require a more elaborate automatic control scheme. In this study, the control of a divided wall column has been investigated in comparison to the control with a single loop PI controller concept. Although the PI controller concept can be implemented successfully, the model predictive controller shows a considerably improved control behaviour in respect to maximum deviations of the controlled variables and the time to reach steady state. (C) 2003 Elsevier B.V. All rights reserved.
引用
收藏
页码:347 / 355
页数:9
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