本文選題：報(bào)警管理　切入點(diǎn)：小波分析　出處：《青島科技大學(xué)》2015年碩士論文　論文類型：學(xué)位論文

【摘要】：報(bào)警系統(tǒng)構(gòu)成了大型現(xiàn)代化工裝置操作界面的一個(gè)重要組成部分,在預(yù)防、控制和減輕異常情況方面具有重要的作用。因此,報(bào)警的優(yōu)化以及報(bào)警處理策略對(duì)化工裝置的正常運(yùn)行具有十分重要的意義。精餾塔是化工企業(yè)生產(chǎn)過程中應(yīng)用廣泛的傳質(zhì)設(shè)備,在化工行業(yè)有著很重要的地位。精餾塔的安全、平穩(wěn)運(yùn)行己經(jīng)成為了化工生產(chǎn)的重要環(huán)節(jié),也直接關(guān)系到化工企業(yè)的經(jīng)濟(jì)效益。本文針對(duì)精餾塔DCS報(bào)警信息冗余問題,進(jìn)行了報(bào)警優(yōu)化以及報(bào)警根原因分析研究。本文首先對(duì)報(bào)警系統(tǒng)關(guān)鍵性能指標(biāo)進(jìn)行了統(tǒng)計(jì)分析,并對(duì)報(bào)警系統(tǒng)的性能進(jìn)行了評(píng)估,為后續(xù)報(bào)警系統(tǒng)優(yōu)化做好了準(zhǔn)備。針對(duì)重復(fù)報(bào)警,在考慮死區(qū)的基礎(chǔ)上,引入了基于數(shù)據(jù)過濾的報(bào)警限優(yōu)化設(shè)計(jì)。數(shù)據(jù)過濾的引入有效地解決了過程數(shù)據(jù)受噪聲干擾的不足,增強(qiáng)了魯棒性。死區(qū)和數(shù)據(jù)過濾的結(jié)合,有效地解決了重復(fù)報(bào)警的問題。但是,僅根據(jù)測(cè)量信號(hào)進(jìn)行報(bào)警優(yōu)化是十分有限的,只有找到報(bào)警根源才能徹底解決報(bào)警的問題。故障診斷策略也是處理報(bào)警的一種有效方法,只要將故障消除,報(bào)警也會(huì)隨之消失。但是,直接將化工機(jī)理模型用于故障診斷還存在計(jì)算量大、收斂性不好的問題。因此,本文研究了基于雙層法模型的故障檢測(cè)和診斷方法。使用非線性模型監(jiān)控精餾過程和識(shí)別大的測(cè)量值偏差時(shí)的異常情況,通過基于線性模型的線性最小二乘法估計(jì)精餾塔內(nèi)部的故障參數(shù)。為了進(jìn)一步縮小模型計(jì)算范圍,還運(yùn)用希梅爾布勞算法對(duì)精餾系統(tǒng)進(jìn)行分解,將高維的、不易求解的問題分解成若干低維的子問題。然后對(duì)分解后的小系統(tǒng)采用基于中值濾波和提升小波分析去噪的方法對(duì)數(shù)據(jù)進(jìn)行去噪處理,增強(qiáng)了報(bào)警優(yōu)化的魯棒性。最后,將上述報(bào)警優(yōu)化策略應(yīng)用到TEP仿真流程的汽提塔中。案例研究結(jié)果表明,雙層診斷結(jié)構(gòu)有效地獲得了故障參數(shù)的變化情況,比單純的非線性模型結(jié)構(gòu)更有效。還給出了因物流C的壓差推動(dòng)力發(fā)生階躍下降導(dǎo)致的故障7時(shí)的塔底進(jìn)料損失參數(shù)的變化情況。結(jié)果表明,該方法不僅可以準(zhǔn)確地給出故障原因還可以大大縮短報(bào)警診斷的時(shí)間。
[Abstract]:The alarm system constitutes an important part of the operating interface of large-scale modern chemical plants and plays an important role in preventing, controlling and mitigating anomalies. The optimization of alarm and the strategy of alarm processing are very important to the normal operation of chemical plant. Distillation tower is a mass transfer equipment widely used in the production process of chemical enterprises and plays an important role in the chemical industry. Smooth operation has become an important part of chemical production, and also directly related to the economic benefits of chemical enterprises. This paper aims at the redundancy of DCS alarm information in distillation tower. The alarm optimization and the cause analysis of the alarm root are carried out. Firstly, the key performance indexes of the alarm system are statistically analyzed, and the performance of the alarm system is evaluated. For the repeated alarm, considering the dead zone, the optimal design of alarm limit based on data filtering is introduced. The introduction of data filtering can effectively solve the problem of process data being disturbed by noise. The combination of dead zone and data filtering can effectively solve the problem of repeated alarm. However, it is very limited to optimize the alarm only according to the measured signal. Only by finding the root cause of the alarm can the problem of alarm be solved completely. The fault diagnosis strategy is also an effective way to deal with the alarm. As long as the fault is eliminated, the alarm will disappear. However, The direct application of chemical mechanism model to fault diagnosis still has the problems of large computation and poor convergence. In this paper, the fault detection and diagnosis method based on the two-layer model is studied. The nonlinear model is used to monitor the distillation process and identify the abnormal situation of the large deviation of the measured value. The linear least square method based on the linear model is used to estimate the internal fault parameters of the distillation tower. In order to further reduce the calculation range of the model, the Simmel Braugh algorithm is also used to decompose the distillation system. The problem that is difficult to solve is decomposed into some sub-problems of low dimension. Then, the decomposed small system is de-noised based on median filter and lifting wavelet analysis, which enhances the robustness of alarm optimization. The above alarm optimization strategy is applied to the stripper of TEP simulation flow. The case study shows that the two-layer diagnosis structure can effectively obtain the variation of fault parameters. It is more effective than the simple nonlinear model structure. The variation of the parameters of the bottom feed loss caused by the step drop of the pressure differential driving force of the logistics C at 7:00 is also given. The results show that, This method can not only give the cause of fault accurately, but also shorten the time of alarm diagnosis.
【學(xué)位授予單位】：青島科技大學(xué)
【學(xué)位級(jí)別】：碩士
【學(xué)位授予年份】：2015
【分類號(hào)】：TQ053.5

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