A fractional order PID-based sliding mode controller approach for chemical processes

Q3 Mathematics
Oscar Camacho , Sebastian Vega , Marco Herrera , Antonio Di Teodoro , Juan J. Gude
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引用次数: 0

Abstract

This paper proposes a novel control strategy for chemical processes by integrating fractional-order PID (FOPID) controllers with sliding mode control (SMC). Through the use of the enhanced flexibility and superior tuning capabilities of FOPID controllers over traditional PID schemes, the method replaces the classical discontinuous switching mechanism of SMC with a smooth fractional-order control action. The proposed hybrid approach is evaluated through simulations in two nonlinear systems, a mixing tank with variable time delay and a pH neutralization process, and experimentally validated using the TCLab device. Throughout three case studies, the method demonstrates improvements in performance and response between 40% and 10% compared to the other two SMC alternatives. Furthermore, the approach effectively reduces chattering, improves convergence speed, and improves robustness to measurement noise, contributing to extended actuator lifespan. This makes the proposed methodology particularly attractive for chemical process applications, offering a practical and accessible solution for plant operators by enabling the utilization of robust control techniques without requiring deep expertise in nonlinear control design.
基于分数阶pid的化工过程滑模控制器方法
将分数阶PID (FOPID)控制器与滑模控制(SMC)相结合,提出了一种新的化工过程控制策略。该方法利用FOPID控制器相对于传统PID方案增强的灵活性和优越的整定能力,以平滑的分数阶控制动作取代SMC的经典不连续切换机制。通过在两个非线性系统、变时延混合槽和pH中和过程中进行仿真,对所提出的混合方法进行了评估,并使用TCLab装置进行了实验验证。在三个案例研究中,与其他两种SMC替代方案相比,该方法的性能和响应提高了40%到10%。此外,该方法有效地减少了抖振,提高了收敛速度,提高了对测量噪声的鲁棒性,有助于延长执行器的使用寿命。这使得所提出的方法对化学过程应用特别有吸引力,通过启用鲁棒控制技术的利用,为工厂操作员提供了实用且易于访问的解决方案,而无需在非线性控制设计方面拥有深厚的专业知识。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Results in Control and Optimization
Results in Control and Optimization Mathematics-Control and Optimization
CiteScore
3.00
自引率
0.00%
发文量
51
审稿时长
91 days
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