TITO过程分散动态滑模控制器的设计与分析

Mukesh G. Ghogare, A. Laware, S. Patil, C. Patil
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引用次数: 3

摘要

本文将分散动态滑模控制(DySMC)策略应用于多变量水平控制系统。对于由原系统和积分器组成的增广系统,将DySMC控制输入的时间导数作为一个新的控制变量。该方法可以将不连续项转化为控制输入的一阶导数,有效地降低了系统的抖振。输入/输出变量之间的相互作用是多变量交互过程多环控制器设计中的一个普遍现象,也是一项具有挑战性的任务。为了减少变量间的相互作用,采用了理想解耦器。为每个解耦子系统设计了独立的对角控制器,将其简化为一阶加死区(FOPDT)模型。对工业规模聚合反应器系统进行了数值模拟试验。利用实验室级耦合罐系统进行了实验测试,以检查所提出的控制器的有效性。将该方法与滑模控制器(SMC)进行了比较。仿真和实验结果表明,DySMC方法有效地抑制了系统的抖振,补偿了外部干扰和参数不确定性的影响。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Design and Analysis of Decentralized Dynamic Sliding Mode Controller for TITO Process
In this paper, a decentralized dynamic sliding mode control (DySMC) strategy is applied to a multivariable level control system. The time derivative of the control input of the DySMC is considered a new control variable for an augmented system which is composed of the original system and the integrator. This DySMC can transfer discontinuous terms to the first-order derivative of the control input and effectively reduce the chattering. The interactions between input/output variables are a common phenomenon and a challenging task in the design of multi-loop controllers for interacting multivariable processes. For reducing the interaction among variables, ideal decouplers are used. Independent diagonal controllers are designed for each decoupled subsystem, which is reduced to the first-order plus dead-time (FOPDT) model. A numerical simulation test has been carried out on a reactor system of the Industrial-Scale Polymerization (ISP). Experimental tests are performed to check the efficacy of the proposed controller using a laboratory-level coupled tank system.  A comparison of the proposed approach and sliding mode controller (SMC) is presented. Simulation and experiment results show that the DySMC approach reduces the chattering, and compensates for the effect of the external disturbances, and parametric uncertainties.
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