Model Reference Adaptive Control for Temperature Regulation of Continuous Stirred Tank Reactor

A. Abougarair, N. A. Shashoa
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引用次数: 4

Abstract

CSTR (Continuous Stirred Tank Reactor) is a major challenge in process control that has sparked a lot of research in the chemical and control engineering. The nonlinear and coupled nature of CSTR makes designing a robust control with a larger working region difficult. Conventional PID (Proportional Integral Derivative) and adaptive control are described in this work for temperature control. For adaptive control system, the MRAC strategy is utilized and the control law is created by the Lyapunov stability method. Additionally, the robustness and efficacy of the MRAC are confirmed compared with PID controller. The suggested controllers' performance is verified using the steady-state error, time specification criteria and tracking of the reference signal in presence of uncertainty. The simulation results clearly show that the MRAC method provides adequate performance in terms of process functional improvements, and more flexibility, in addition to, improves system-tracking precision in control action compared with the PID.
连续搅拌釜式反应器温度调节模型参考自适应控制
连续搅拌槽式反应器(CSTR)是过程控制领域的一个重大挑战,引起了化学和控制工程领域的大量研究。CSTR的非线性和耦合特性使得设计具有更大工作区域的鲁棒控制变得困难。本文介绍了传统PID(比例积分导数)和自适应控制的温度控制方法。对于自适应控制系统,采用MRAC策略,利用李雅普诺夫稳定性方法建立控制律。通过与PID控制器的比较,验证了MRAC的鲁棒性和有效性。利用稳态误差、时间规范标准和存在不确定性时参考信号的跟踪来验证所建议控制器的性能。仿真结果清楚地表明,与PID相比,MRAC方法在过程功能改进方面提供了足够的性能,并且具有更大的灵活性,并且在控制动作上提高了系统跟踪精度。
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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