精馏塔鲁棒分散控制系统的设计

IF 0.3 Q4 ENERGY & FUELS Problemele Energeticii Regionale Pub Date : 2022-05-01 DOI:10.52254/1857-0070.2022.2-54.04
A. Stopakevich, A. Stopakevich
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引用次数: 1

摘要

本文致力于开发一种具有改进鲁棒性的分散控制系统设计方法,适用于精馏塔控制问题。通过解决以下问题达到目的:选择具有代表性的立柱模型;开发一种有效的传递函数识别算法;开发了一种分散控制器设计算法,该算法考虑了交叉链路的影响;为选定的柱模型验证所开发的方法。最重要的结果是所开发的设计方法,该方法包括两种算法。第一种算法可以用于识别有效传递函数的简化模型。第二种算法使基于原始模型的对角线与有效传递函数之间的比率设计分散控制系统成为可能。采用了改进的PI控制器。实现蒸馏塔控制系统对模型参数的同步技术条件偏差的鲁棒性高达标称值的三百分之三是论文的重要结果。所设计的控制器的数字实现很简单。对文献的分析表明,以前提出的分散式自动控制系统的设计方法都没有解决这样的问题。使用已知的蒸馏塔动力学模型说明了所开发算法的效率。分析了该方法的局限性及其与最大对数调谐和H∞环路成形方法的显著差异。
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Design of Robust Decentralized Control Systems for Distillation Columns
This paper is devoted to the development of a decentralized control system design method with improved robustness, applicable to distillation columns control problem. The aim is attained by solving the following tasks: selection of representative models of columns; development of an effective transfer function identification algorithm; development of a decentralized controller design algorithm, which takes into account the cross-links impact; verification of the developed method for the selected models of columns. The most important result is the developed design method, which includes two algorithms. The first algorithm can be used to identify simplified models of the effective transfer functions. The second algorithm makes it possible to design a decentralized control system based on the ratio between the diagonals of the original model and effective transfer functions. Modified PI controller is used. The achievement of the distillation column control system robustness to the synchronous technologically conditioned deviation of the model parameters by up to three hundred percent of the nominal value is the paper significant result. The digital implementation of the designed controllers is simple. The analysis of the literature shows that none of the previously proposed methods for designing decentralized automatic control systems solved such a problem. The efficiency of the developed algorithms is illustrated using the known models of dynamics of distillation columns. The analysis of limitations of the method as well as its significant differences to the Biggest Log Tuning and H∞ loop shaping methods is presented.
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来源期刊
CiteScore
0.70
自引率
33.30%
发文量
38
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