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Liquid level control of a couple tank system based on smooth trajectory tracking using PID controller

机译:基于PID控制器的轨迹平滑跟踪的耦合罐系统液位控制。

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摘要

Industries such as petro-chemical industries, paper making industries, waste management and others are the vital industries where liquid level and flow control are essential. Liquids will be processed by chemical or mixing treatment in the tanks, but always the level fluid in the tanks must be controlled, and the flow between tanks must be regulated in the presence of nonlinearity and inexact model description of the plant. This project investigates the usage of Proportional-Integral-Derivative (PID) controller in controlling the liquid level in the second tank of Coupled-Tank plant through variable manipulation of water pump in the first tank. This project presents the ability of controlling the liquid level of a coupled tank system that used Programmable Logic Controller (PLC) as a main controller hardware. A PID controller has been developed and designed via ladder programme of CXprogrammer. A mathematical model of the couple tank system was derived by refering to the experimental manual and verified by using MATLAB software. The controller parameters derived from the simulation and design process using MATLAB as well. The project is based on Single Input Single Output (SISO) system which mean the liquid will entering the tank 1 (pump 1) in couple tank while the level control is in tank 2 in the condition of pump 2 is set OFF. The aim of the project is to design controller that can maintain the level and minimize the error (SPCV) value at any of given set point(SP). It is to show that PID controller could produce appropriate control signal to the coupled-tank system and minimize the error value for the system. A series of tracking performance tests conducted to evaluate the controller performance in comparison to other controller such are fuzzy controller, DMRAC controller or other controller that used by other reearcher before. . The outcome of the project reveals that PID controller could carry a small error rate when the appropriate value of Kp, Ki, and K are applied. The framework of this project is generic enough to have an overview of the possible outcome before implementing the PID controller in real-time system in the future.
机译:石油化工,造纸,废物管理等行业是液位和流量控制必不可少的重要行业。液体将在储罐中通过化学处理或混合处理进行处理,但是必须始终控制储罐中的液位,并且必须在存在非线性和不精确的工厂模型描述的情况下调节储罐之间的流量。该项目研究了比例积分微分(PID)控制器在耦合罐设备第二个罐中通过对第一个罐中的水泵进行可变操作来控制液位的用法。该项目展示了控制使用可编程逻辑控制器(PLC)作为主控制器硬件的耦合储罐系统的液位的能力。通过CXprogrammer的梯形图程序已开发和设计了PID控制器。参考实验手册推导了耦合罐系统的数学模型,并使用MATLAB软件进行了验证。控制器参数也来自使用MATLAB进行的仿真和设计过程。该项目基于单输入单输出(SISO)系统,这意味着当泵2处于关闭状态时,液位控制在罐2中时,液体将进入耦合罐中的罐1(泵1)。该项目的目的是设计一种控制器,该控制器可以在给定的任何设定点(SP)保持水平并最小化误差(SPCV)值。这表明PID控制器可以向耦合储罐系统产生适当的控制信号,并使系统的误差值最小。与其他控制器(例如模糊控制器,DMRAC控制器或以前由其他挖土机使用的其他控制器)相比,进行了一系列跟踪性能测试以评估控制器性能。 。该项目的结果表明,当应用适当的Kp,Ki和K值时,PID控制器的误差率很小。该项目的框架足够通用,可以在将来在实时系统中实施PID控制器之前对可能的结果进行概述。

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    Salman Razeni;

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  • 年度 2009
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