Study on the Switching Model Predictive Control Algorithm in Batch Polymerization Process

IF 3 Q2 ENGINEERING, CHEMICAL
Jong Nam Kim , Chun Bae Ma , Hyok Jo , Un Chol Han , Hyon-Tae Pak , Son Il Hong , Ri Myong Kim
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引用次数: 0

Abstract

In the batch polymerization process, temperature control is generally a challenging task. In this paper, a new switching model predictive control algorithm that can be effectively used for the temperature control of batch polymerization process is developed and its effectiveness is verified by introducing it to industrial batch polyvinyl chloride polymerization process. Firstly, a general analysis of the polymerization process is conducted, and based on this, the reaction starting point is determined. Secondly, a switching model identification method considering the reaction starting point and the reaction heat generated after the reaction starts is proposed. Finally, a switching model predictive control algorithm that determines the optimal manipulated value based on the on-line updated step response model is constructed, and a cascade control system using this algorithm is introduced to the temperature control of batch polyvinyl chloride suspension polymerization process. The results show that the proposed control system can significantly improve temperature control performance (overshoot: 0.2%, root mean square error: 0.3) compared to before introduction (overshoot: 1.1%, root mean square error: 1.2ྟC) .
间歇聚合过程中切换模型预测控制算法的研究
在间歇聚合过程中,温度控制通常是一个具有挑战性的任务。本文提出了一种可有效用于间歇聚合过程温度控制的切换模型预测控制算法,并将其应用于工业间歇聚氯乙烯聚合过程中,验证了该算法的有效性。首先对聚合过程进行总体分析,在此基础上确定反应起始点。其次,提出了考虑反应起始点和反应开始后产生的反应热的切换模型辨识方法。最后,构建了基于在线更新阶跃响应模型确定最优操纵值的切换模型预测控制算法,并将该算法引入到间歇聚氯乙烯悬浮聚合过程的温度控制中。结果表明,与引入前(超调量:1.1%,均方根误差:1.2)相比,该控制系统能显著提高温度控制性能(超调量:0.2%,均方根误差:0.3)。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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