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基于多控制器切换的过热汽温控制系统设计
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摘要
火电厂汽温控制是一个成熟而常新的研究领域。一方面,基于常规PID控制的DCS控制系统已经具有一套规范成熟的体系;另一方面,市场对电厂的供电质量、安全性能及价格体系提出了更高的要求,而且电厂中亚临界、起临界等大型机组的比重越来越大,因此具有大容量,多参数特点的大型机组带来更加复杂多变的热工特性,使得现有的控制策略难以满足新形势下的控制要求。因此,新的控制理论及控制策略的研究和应用对火电厂汽温控制具有迫切的现实意义。
     火电厂锅炉是一个非线性、强耦合、大滞后、多变量、工况范围广的复杂对象,本文以某火电厂#2锅炉600MW机组为研究对象,针对其控制品质差、易超温等问题,提出一种基于多控制器切换的过热汽温控制系统设计方法。由于过热汽温控制系统处于不同工况下的模型存在较大差异,本文针对每种不同的模型分别设计出与之相对应的控制器,并通过实时的监测其偏差值判断是否执行控制器的切换,当时滞在一定范围之内时,采用传统的数字PID对其控制;当时滞过大时,采用广义预测控制器进行控制。实验仿真结果表明,通过多控制的切换控制,锅炉过热汽温控制的动态特性明显得到了明显的改善。
Thermal power plant steam temperature control is a well-developed and frequentlyinnovated researching field.On the one hand, the DCS(distributed control system)based oncascade PID control strategy for power plant has been a normative and well-developedsystem. On the other hand,the more high criterions have been required for power plantspower supply quality, security performances and economy because of the market. Andsince the proportion of large units such as sub-vertical and super-critical growing unitshave been applied. Thermal complicated and variable thermal characteristics brought by alarge-capacity, multi-parameter characteristics have been made the existing controlstrategies not easy to meet the control request under the new situation. Therefore, a newresearch and application of control theory and strategies for thermal power plant steamtemperature control have urgent practical significance.
     The boiler of thermal power plants is a complex object of nonlinear, strong coupling,large delay, multi-variable, and a wide range of operating conditions. Based on the NO.2steam temperature of600MW a certain power plant which had the problems of bad controlquality and surpassing temperature easily, design method of super-heated steamtemperature control system is proposed based on the switching multi-controller.Correspondingly, the controller has been designed for each different model. And throughreal-time monitoring of its deviation determine, it is to switch the implementation of thecontroller or not. It is time to choose traditional digital PID control scheme when the timelag is in certain range. If the time lag is too large, the generalized predictive controller issuitable. Simulation results show that the dynamic characteristics of the superheated steamtemperature control of boiler have been significantly improved through the multi-controllerswitching method.
引文
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