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基于非平稳敏感协整分析的化工过程故障检测。

Fault detection for chemical processes based on non-stationarity sensitive cointegration analysis.

机构信息

Key Laboratory of Knowledge Automation for Industrial Processes of Ministry of Education, School of Automation and Electrical Engineering, University of Science and Technology Beijing, Beijing 100083, China.

Key Laboratory of Knowledge Automation for Industrial Processes of Ministry of Education, School of Automation and Electrical Engineering, University of Science and Technology Beijing, Beijing 100083, China.

出版信息

ISA Trans. 2022 Oct;129(Pt B):321-333. doi: 10.1016/j.isatra.2022.02.010. Epub 2022 Feb 10.

Abstract

Due to the time-varying operation conditions, chemical processes are characterized by non-stationary characteristics, which makes it a great challenge for conventional process monitoring methods to capture the non-stationary variations In the non-stationary processes, the abnormality would cause the stationary variables to be non-stationary. In this article, a non-stationarity sensitive cointegration analysis monitoring method is proposed to explore potential non-stationary variations. First, the essential non-stationary variables are distinguished using Augmented Dickey-Fuller test to eliminate the influence of essential non-stationary under normal conditions. Then by further analyzing the faulty data, the variables which are sensitive to the non-stationary variations are selected. On this basis, cointegration analysis models are established for both the essential non-stationary variables and non-stationarity sensitive variables to explore long-term dynamic equilibrium relationship, respectively. With the selection of non-stationarity sensitive variables, the potential faulty information is emphasized in the process monitoring model, which makes the model capable to handle the non-stationary variations. Finally, the monitoring results are combined through Bayesian inference criterion. The proposed method is applied on the Tennessee Eastman process and a vinyl acetate monomer plant model, and the feasibility and performance are demonstrated.

摘要

由于操作条件随时间变化,化学过程的特点是非平稳特性,这使得传统的过程监测方法难以捕捉到非平稳过程中的非平稳变化。在非平稳过程中,异常会导致平稳变量变得非平稳。本文提出了一种对非平稳性敏感的协整分析监测方法,以探索潜在的非平稳变化。首先,使用增广迪基-富勒检验来区分基本非平稳变量,以消除正常条件下基本非平稳的影响。然后,通过进一步分析故障数据,选择对非平稳变化敏感的变量。在此基础上,分别为基本非平稳变量和非平稳敏感变量建立协整分析模型,以分别探索长期动态平衡关系。通过选择非平稳敏感变量,在过程监测模型中强调了潜在的故障信息,从而使模型能够处理非平稳变化。最后,通过贝叶斯推断准则结合监测结果。该方法应用于田纳西伊斯曼过程和醋酸乙烯单体工厂模型,验证了其可行性和性能。

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