Control of a Nonlinear Tank Process using Dynamic Matrix Controller

M. Mirudubaashini, Jayaprasanth D
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Abstract

. The level process is widely used in many process industries for storing the liquids for mixing purpose in sugar mills, as settling tank and for water treatment plants. Most of the chemical plants are multivariable processes which exhibit nonlinear behaviour due to the existence of interactions between the input and output variables. The level control of the cylindrical tank is difficult because of its nonlinearity. Linear PID (Proportional Integral Derivative) controllers are generally used in many industrial control systemsbecause of its simple structure and robustness, but whenit comes to the control of nonlinear and multivariable processes, the controller parameters have to be continuously adjusted in order to deal with the nonlinearities, uncertainties and interaction betweenthevariables.The major objective of this work is to control the level of a nonlinear tank process. This is achieved by modelling a nonlinear controller which can adapt to the nonlinear performanceof the process. To achieve this goal, the mathematical modelling of a tank process is obtained. Dynamic Matrix Control (DMC) Controller is designed using the mathematical model to control the tank system. The performance of the controller can be analyzedthrough extensive simulation studies.
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用动态矩阵控制器控制非线性储罐过程
。液位法在许多加工工业中被广泛应用于糖厂、沉淀池和水处理厂的混合液体储存。大多数化工厂是多变量过程,由于输入和输出变量之间存在相互作用而表现出非线性行为。由于筒形储罐的非线性特性,其液位控制是一个难点。线性PID (Proportional Integral Derivative,比例积分导数)控制器由于其结构简单、鲁棒性好,被广泛应用于许多工业控制系统中,但在非线性和多变量过程的控制中,为了处理非线性、不确定性和变量之间的相互作用,控制器参数必须不断调整。本工作的主要目的是控制非线性储罐过程的液位。这是通过建模一个非线性控制器来实现的,该控制器可以适应过程的非线性性能。为实现这一目标,建立了储罐过程的数学模型。利用数学模型设计了动态矩阵控制(DMC)控制器,对储罐系统进行控制。控制器的性能可以通过广泛的仿真研究来分析。
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