相互作用耦合油箱系统FOPID控制器建模与性能分析

IF 1.2 Q3 ENGINEERING, MECHANICAL
Thelkar Ramesh, C. Bharatiraja, Muluken Teka, Mulugeta Gonfa, Tesfabirhan Shoga, A. Feyo, T. Mekonnen
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引用次数: 0

摘要

过程控制是现代交互的基础,因为它确保了周期的安全性和改进。此外,过程控制是实现生态战略和产品质量要求的重要手段。在企业中,控制系统的因素之一是液位,液位调节器是一个重要的问题和众所周知的相互作用,是设计技术的综合说明。液位耦合罐架可分为接触式和非关联式两种。这项工作主要围绕关联耦合罐控制框架,影响液位的许多问题,如框架的非线性,显示漏洞,以及复杂的调查,因此为了克服这些问题,需要不同的调节器来获得稳定的结果和快速的反应。在现代的控制设计中,液体必须被转移并保存在一个支架中。本文研究了一种局部请求比例积分微分(PID)调节器,用于控制油箱框架的液位。FOPID和TID控制器技术在耦合连接的油箱系统中进行了测试和演示,使用了几个部分请求调节器,包括命令鲁棒非整阶(CRONE)、倾斜积分导数(TID)和分数阶PID (FOPID)。在MATLAB®/Simulink®环境下直接对结果进行反应,检查框架的展示性。再现结果表明,在不加重连接耦合罐系统(CTS)控制的情况下,反应很大,但考虑到外界对后续罐的不安影响,除FOPID调节器外,调节器表现出微弱的反应。解释是FOPID调节器至少改变了两个边界,扩展了框架的活力。从试验的调节器来看,部分请求相对基本从属调节器(FOPID)与PID、TID和数字PID调节器相比具有很好的执行力。完成的演示,特别是FOPID调节器与其他列出的控制器相比,CTS具有更好的性能。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Modeling and performance analysis of FOPID controller for interacting coupled tank system
Process control is fundamental in modern interaction since it ensures security and improvement in a cycle. Furthermore, process control is a valuable apparatus to fulfill the ecological strategy and item quality necessities. In ventures, one of the controlling system factors is fluid level, the fluid level regulators are a critical concern and well-known interaction, and the aggregate illustrative additionally genuine world in designing techniques. Fluid-level coupled tank framework can be set up into two popular types of interfacing and non-associating structure. This work centers around associating coupled tank control frameworks, numerous issues impacting the fluid level like nonlinearity of the framework, displaying vulnerabilities, and complex investigation, so to conquer those issues, to acquire steady stable results and quick reactions different regulators are required. The liquid must be transferred and kept in a holder for control design in the modern day. The study of a partial request proportional-integralderivative (PID) regulator for controlling a fluid level of the tank framework is presented in this work. FOPID and TID controller techniques are tested and demonstrated for coupling connected tank systems using several partial request regulators, including Commande Robuste d'Ordre Non-Entire (CRONE), Tilt-Integral Derivative (TID), and Fractional order PID (FOPID). The result reaction is directed with the MATLAB®/Simulink® circumstance to check the exhibition of the framework. The reproduction results showed that by controlling connecting coupled tank system (CTS) without aggravation, the reaction is great, however remembering outside unsettling influence for the subsequent tank, the regulator shows a feeble reaction aside from the FOPID regulator. The explanation is FOPID regulator has at least two changed boundaries that expand the vigor of the framework. From the regulators tried in this work, the partial request relative basic subordinate regulator (FOPID) has great execution contrasted with PID, TID, and digital-PID regulators. The accomplished presentation particularly of the FOPID regulator is a better performance for CTS compared to the other listed controllers.
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来源期刊
FME Transactions
FME Transactions ENGINEERING, MECHANICAL-
CiteScore
3.60
自引率
31.20%
发文量
24
审稿时长
12 weeks
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