共查询到18条相似文献,搜索用时 109 毫秒
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针对汽包锅炉过热汽温的特点,设计了自适应模糊控制器,即采用了一种模糊控制的遗传算法将控制器的隶属参数进行优化。理论分析和仿真结果都表明该方案对解决汽包锅炉过热汽温热工过程的非线性和大时滞有显著效果,具有快速的实时性和很强的鲁棒性。 相似文献
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基于混沌理论的过热汽温最优预测控制策略 总被引:3,自引:0,他引:3
由于非线性混沌时间序列内部确定的规律性,其重构相空间具有高精度短期预测性。因此,为实现锅炉过热汽温的非线性、大时滞系统的自适应控制,根据具有混沌特性的过热汽温时间序列重构相空间,计算相空间饱和嵌入维数、最大Lyapunov指数和系统的可预报尺度,并以此为指导,建立神经网络预测模型对过热汽温系统作高精度的短期预测,在此基础上,通过反馈校正,将校正误差和控制增量引入性能函数,寻优得最优控制策略,实现了对过热汽温的非线性、大时滞系统高精度的自适应预测控制。仿真表明了控制的有效性、快速性和鲁棒性。 相似文献
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过热汽温多模型预测函数控制策略的研究 总被引:9,自引:1,他引:9
过热汽温系统是典型的大时延、大惯性对象,尤其当机组负荷变化时,参数表现出明显的时变特性,大大降低了传统PID串级控制的品质。基于此点,提出先进的多模型切换的过热汽温预测函数控制策略。使用带有Smith预估补偿思想的一阶时滞对象预测函数控制算法,来有效克服对象的大时延、大惯性;并通过建立若干典型工况的固定模型,在线计算其模型匹配度确定控制权重,从而得到控制器的输出的方法,能适应参数的时变。与PID串级控制和单一模型控制的仿真结果对比,证实了本控制策略的有效性。图3表1参8 相似文献
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针对过热汽温对象特征参数在负荷范围内变化较大的特点,提出一种基于插值和拟合技术的过热汽温非线性自适应控制方法,通过调节控制器参数使其随负荷自动变化来保证系统的鲁棒性。首先简单介绍了过热汽温串级控制和采用插值与拟合技术获取控制器参数的方法,然后提出一种连续变速积分不完全微分数字比例、积分、微分(PID)控制算法。基于典型工况下的PID参数和插值及拟合技术建立了过热汽温全工况下的自适应控制器,并对某超临界600 MW直流锅炉过热汽温对象进行了仿真。分析了不同插值和拟合方法下自适应PID控制的控制效果,证明了本文方法的有效性。 相似文献
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考虑超临界锅炉过热汽温系统的非线性、大惯性、大时延等特性,建立了过热汽温喷水减温系统的非线性动态神经网络逆模型,运用机组的历史运行数据对模型进行训练与校验。以训练好的模型为基础,构建了具有PID补偿环节的神经网络逆控制器,在MATLAB平台编制了实时控制程序。借助600 MW超临界机组全仿真系统,对过热汽温进行设定值扰动、大范围变工况扰动等仿真试验。结果表明:具有PID补偿的神经网络逆控制方案可有效降低动态变负荷过程中过热汽温的控制偏差,缩短汽温控制的稳定时间,与机组原控制方案相比具有更好的控制效果。 相似文献
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为了增强过热汽温控制系统的负荷适应能力,以一个600MW机组的过热汽温系统为研究对象,设计了由4组局部控制器组成的负荷调度控制系统,并以主蒸汽流量作为系统的调度变量。每一组局部控制器对应一种典型工况,采用串级内模原理进行设计和整定,其中,高阶的外回路控制器通过Taylor级数展开的方法简化为实际PID形式。控制系统各局部控制器之间的跟踪与无扰切换通过Hanus方法实现。系统保留了传统串级控制系统克服内回路扰动、提高系统工作频率的优点。在不同负荷下的仿真试验以及大范围变工况试验均表明,该系统具有良好的负荷适应能力。图5表3参3 相似文献
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LI Xu 《Frontiers in Energy》2008,2(1):25
A simple way of calculating the dynamic behavior of a superheater is presented. A comparison of the measured data with the calculated result verifies the accuracy of this simple method. It is the first time that a phase compensation for real roots, i.e., the twin lead/lag loop which is facile for engineering applications, is used in superheated steam temperature control. Numerous simulation results show that both the response time lapse and maximal dynamic deviation are greatly reduced. Moreover, a formula to calculate the setting parameters is presented, together with a practical example of its engineering application in superheated steam temperature control with single-stage attemperation in a power plant boiler. This method can remarkably improve the control performance of superheated steam temperature and makes it possible for one stage attemperation to be sufficient for the superheater of power plant boilers, thus simplifying the superheater system and reducing investment. Because the control performance is remarkably raised, the set values of the steam temperature control system can be raised above rated values and also the operational economy, without impairing the operation safety. 相似文献
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过热汽温的动态特性与控制 总被引:4,自引:0,他引:4
给出了过热器动态特性的简便计算方法.按过热器的结构和热力参数计算出单级和多级过热汽温的传递函数.与实测数据相比较,证实这种方法准确而且简便.首次提出在过热气温控制中,采用取实根的相位补偿,即2个串联的超前/滞后环节,在工程中实现很方便.经大量仿真试验证实,其过渡过程时间缩短1半左右,最大动态偏差缩减2-3倍.还给出整定计算公式及多种整定计算数据的取法,以及在一级喷水过热汽温控制的工程应用实例.该方法极大地改善了过热汽温控制品质,电站锅炉过热器可采用一级喷水减温,使过热器系统结构简化,设备投资减少.由于汽温控制品质大大提高,可把汽温控制系统的设定值定在稍高于额定值.在不影响机组运行安全性的同时,提高机组运行的经济性. 相似文献
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Xu LI 《Frontiers of Energy and Power Engineering in China》2008,2(1):25-30
A simple way of calculating the dynamic behavior of a superheater is presented. A comparison of the measured data with the
calculated result verifies the accuracy of this simple method. It is the first time that a phase compensation for real roots,
i.e., the twin lead/lag loop which is facile for engineering applications, is used in superheated steam temperature control.
Numerous simulation results show that both the response time lapse and maximal dynamic deviation are greatly reduced. Moreover,
a formula to calculate the setting parameters is presented, together with a practical example of its engineering application
in superheated steam temperature control with single-stage attemperation in a power plant boiler. This method can remarkably
improve the control performance of superheated steam temperature and makes it possible for one stage attemperation to be sufficient
for the superheater of power plant boilers, thus simplifying the superheater system and reducing investment. Because the control
performance is remarkably raised, the set values of the steam temperature control system can be raised above rated values
and also the operational economy, without impairing the operation safety.
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Translated from Journal of Power Engineering, 2007, 27(2): 199–203 [译自: 动力工程] 相似文献
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针对目前常用串级PID系统在电厂过热蒸汽温度控制过程中存在的问题,提出采用带约束预测的控制算法予以解决.采用这种有约束预测控制后,可抬高控制设定值,从而提高机组运行效率,提高经济效益.采用现场试验数据,通过面积法辨识过程模型并利用Matlab设计预测控制器,进行了控制过热蒸汽温度模型的仿真试验,结果表明:有约束预测控制可改善系统的动态特性和抗干扰能力,并使过热蒸汽温度控制品质得到有效提升. 相似文献
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To address the characteristics of the large delay and uncertainty of superheated temperature, a new cascade control system is presented based on control’s history. Based on the analysis of the control objects’ dynamic characteristics, historical control information (substituting for the deviation change rate) is used as the basis for decision-making of the fuzzy control. Therefore, the changing trend of the controlled variable can be accurately reflected. Furthermore, a proportional component is introduced, the advantages of PID and fuzzy controllers are integrated, and the structure weaknesses of conventional fuzzy controllers are overcome. Simulation shows that this control method can effectively reduce the adverse impact of the delay on control effects and, therefore, exhibit strong adaptability by comparing the superheated temperature control system by this controller with PID and conventional fuzzy controllers. 相似文献
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针对发电厂的过热汽温控制系统中锅炉过热器出口温度的非线性、时变性、滞后性等特点,文中提出了一种模糊PID控制在过热汽温控制系统中的应用。该控制系统能够很好地克服非线性和时变性,使过热汽温控制系统具有较强的鲁棒性,从而提高了控制系统的控制品质,提高了过热器的生产效率。 相似文献