变参数长死区非线性过程:滑模与线性代数控制器的比较。

Alisson Moya, Yaritza Vinueza, O. Camacho
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引用次数: 0

摘要

本文介绍了不同控制技术在控制混合槽变参数和显性延迟时间下的设计、仿真和比较。该工艺包括在一个液体体积可变的罐内混合两种流体。冷进口流通过控制阀操纵,并与热进口流混合,以获得具有所需温度的出口流。控制储罐的目的是使罐内的液体温度恒定,并且还必须通过引入热流扰动w1 (t)来保持该温度。经典的PI控制器将与两种先进的控制技术进行比较,例如基于一阶加死区(FOPDT)模型的滑模控制和线性代数。这些模型捕捉了几个工业过程的基本动态,简化了控制器的设计和调整。利用ISE和ISU性能指标,对混合槽进行参考变化和扰动,分析控制器的性能。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
A Nonlinear Process with Variable Parameters and Long Deadtime: Sliding Mode and Linear Algebra Controller's Comparison.
This paper presents the design, simulation, and comparison of different control techniques applied to control a mixing tank's temperature with variable parameters and dominant delay time. The process consists of mixing two fluids inside a tank with variable liquid volume. The cold inlet flow is manipulated through a control valve, and it is mixed with a hot inlet flow to obtain an outlet flow with the desired temperature. The aim of controlling the tank is to have a constant liquid temperature inside it, and it must also maintain that temperature by introducing hot flow disturbancesW1(t). A classic PI controller will be compared with two advanced control techniques, such as Sliding Mode Control and Linear Algebra, based on First Order Plus Dead Time (FOPDT) models. These models capture the essential dynamics of several industrial processes simplifying controller design and tuning. Using ISE and ISU performance indexes, the mixing tank is subj ected to reference changes and disturbances to analyze the controller's performance.
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