Closed-Loop Stability of a Non-Minimum Phase Quadruple Tank System Using a Nonlinear Model Predictive Controller with EKF

IF 2.8 Q2 ENGINEERING, CHEMICAL ChemEngineering Pub Date : 2023-08-17 DOI:10.3390/chemengineering7040074
Ismaila A. Oyehan, A. Osunleke, Olanrewaju O. Ajani
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Abstract

The dynamics of a quadruple tank system (QTS) represent an extensive class of multivariate nonlinear uncertain systems found in the industry. It has been established that changes in split fractions affect the transmission zero location, thereby altering the operating conditions between the minimum and non-minimum phase regions. The latter is difficult to control as more fluid flows into the two upper tanks than into the two bottom tanks, resulting in competing effects between the initial and final system responses. This attribute, alongside nonlinearity, uncertainties, constraints, and a multivariate nature, can degrade closed-loop system performance, leading to instability. In this study, we addressed the aforementioned challenges by designing controllers for the regulation of the water flow in the two bottom tanks of the QTS. For comparative analysis, three controller algorithms—a nonlinear model predictive controller (NMPC), NMPC augmented with an extended Kalman filter (i.e., NMPC-EKF) and linear model predictive controller (LMPC)—were considered in the analysis and design of the control mechanism for the quadruple water level system in a non-minimum phase condition via the Matrix Laboratory (MATLAB) simulation package environment. The simulated and real-time results in the closed loop were analyzed, and the controller performances were considered based on faster setpoint responses, less oscillation, settling time, overshoot, and smaller integral absolute error (IAE) and integral square error (ISE) under various operational conditions. The study showed that the NMPC, when augmented with an EKF, is effective for the control of a QTS in the non-minimum phase and could be designed for more complex, nonlinear, and multivariable dynamics systems, even in the presence of constraints.
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基于EKF非线性模型预测控制器的非最小相位四缸系统闭环稳定性
四缸系统动力学(QTS)代表了工业中广泛存在的一类多变量非线性不确定系统。已经确定,分裂分数的变化影响传输零点位置,从而改变最小相位区域和非最小相位区域之间的操作条件。后者很难控制,因为流入两个上部储罐的流体比流入两个底部储罐的流体多,导致初始和最终系统响应之间的竞争效应。这种属性,加上非线性、不确定性、约束和多变量性质,可能会降低闭环系统的性能,导致不稳定。在这项研究中,我们通过设计用于调节QTS两个底部水箱中的水流的控制器来解决上述挑战。比较分析了三种控制器算法——非线性模型预测控制器(NMPC),在非最小相位条件下,通过矩阵实验室(MATLAB)仿真软件包环境,对四重水位系统的控制机制进行分析和设计时,考虑了扩展卡尔曼滤波器(即NMPC-EKF)和线性模型预测控制器(LMPC)增强的NMPC。分析了闭环中的模拟和实时结果,并考虑了控制器在各种操作条件下基于更快的设定点响应、更少的振荡、稳定时间、超调以及更小的积分绝对误差(IAE)和积分平方误差(ISE)的性能。研究表明,当增加EKF时,NMPC对于非最小阶段的QTS的控制是有效的,并且可以设计用于更复杂、非线性和多变量的动力学系统,即使在存在约束的情况下也是如此。
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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来源期刊
ChemEngineering
ChemEngineering Engineering-Engineering (all)
CiteScore
4.00
自引率
4.00%
发文量
88
审稿时长
11 weeks
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