文献翻译-单容水箱液位模糊控制系统设计
单容水箱液位控制系统设计计算机课设
辽宁工业大学微型计算机控制技术课程设计(论文)题目:单容水箱液位控制系统设计院(系):电气工程学院专业班级:自动化074学号:*********学生姓名:***指导教师:(签字)起止时间:2010.12.15—2010.12.24课程设计(论文)任务及评语院(系):电气工程学院教研室:自动化摘要本文根据液位系统过程机理,建立了单容水箱的数学模型。
介绍了PID控制的基本原理及数字PID算法,并根据算法的比较选择了增量式PID算法。
建立了基于单片机编程语言的PID液位控制模拟界面和算法程序,进行了系统仿真,并通过整定PID 参数,利用MATLAB应用软件对系统进行仿真得到图线。
系统由进出水阀门,单片机,A/D转换器,D/A转换器,传感器,显示电路和键盘电路等组成。
整个过程保持进水阀的开度比例不变,由传感器检测电路连续不断地相应液位值,送入A/D转换器中处理,输出的数字量送给单片机,控制显示电路实时显示实际液位值,由键盘输入设定值,控制器比较其值控制出水阀门的开度比例,以保持液位稳定在要求范围内。
关键词:水箱建模,液位控制,PID算法,增量式PID目录第1章绪论 (1)第2章课程设计的方案 (2)2.1概述 (2)2.2系统组成总体结构 (2)第3章硬件设计 (3)3.1单片机最小系统设计 (3)3.2传感器模块 (3)3.3A/D转换和D/A转换模块 (3)3.4键盘模块 (3)3.5显示模块 (4)第4章软件设计 (5)4.1PID算法 (5)4.2位置式PID控制系统 (6)4.3增量型PID控制算法 (8)4.4PID计算 (10)4.5主程序控制流程 (11)4.6显示部分 (12)第5章系统测试与分析/实验数据及分析 (14)5.1MATLAB程序 (14)5.2MATLAB成象曲线 (14)第6章课程设计总结 (15)参考文献 (16)附录:系统硬件原理图 (17)第1章绪论过程控制是自动技术的重要应用领域,它是指对液位、温度、流量等过程变量进行控制,在冶金、机械、化工、电力等方面得到了广泛应用。
标准格式的水箱液位控制系统的中文引用文献
标准格式的水箱液位控制系统的中文引用文献【引言】水箱液位控制系统在许多实际应用中起着至关重要的作用。
通过准确控制液位的高低,我们可以实现流体的自动调节和流量的控制。
在水资源紧缺的情况下,有效的液位控制系统可以节约水资源,提高生产效率。
然而,要设计一个稳定可靠的水箱液位控制系统并非易事。
为了更好地理解和应用这一技术,我们需要深入了解并参考相关的文献和研究成果。
在本文中,我将为您介绍一些中文引用文献,以帮助您更全面地了解标准格式的水箱液位控制系统。
【主体】一、《液位控制的最优方案研究》在该论文中,研究者提出了一种利用PID控制算法实现液位控制的最优方案。
该方案通过系统建模和理论分析,得出了一组最佳的PID参数,以实现液位的精确控制。
论文中详细介绍了PID控制算法的原理及其在液位控制中的应用,为我们理解和应用液位控制系统提供了宝贵的参考。
二、《基于模糊控制的水箱液位控制系统研究》这篇论文主要研究了基于模糊控制的水箱液位控制系统。
模糊控制是一种具有鲁棒性和适应性的控制方法,可以有效处理实际应用中涉及到的不确定性和模糊性。
论文中详细介绍了模糊控制系统的原理与设计,并通过实验验证了该控制系统在水箱液位控制中的有效性。
三、《基于神经网络模型的水箱液位控制系统研究》该论文提出了一种基于神经网络模型的水箱液位控制系统。
神经网络模型具有强大的非线性建模和泛化能力,可以很好地适应复杂的控制环境。
论文详细介绍了神经网络的结构和训练方法,并通过实验验证了该模型在水箱液位控制中的高性能。
四、《水箱液位控制系统的设计与实现》这篇论文从工程实际出发,详细介绍了一个水箱液位控制系统的设计与实现过程。
论文中包括了系统的硬件和软件设计,以及控制算法的选择和调试方法。
通过实验数据的分析和结果的验证,论文提供了一种实用的水箱液位控制系统设计方案。
【结论】通过对以上中文引用文献的介绍,我们可以得出一些有关标准格式的水箱液位控制系统的重要结论。
文献总结报告
最优控制与智能控制基础文献总结报告基于模糊控制的单容水箱液位控制系统学生姓名:班级学号:3134110任课教师:段洪君提交日期:2016.06.22成绩:1 研究背景及意义液位是过程控制中的一个重要参数,它对生产的影响不容忽视。
为保证生产的安全和高效,有必要进行先进的液位控制方法和策略的研究与开发[2]。
为了保证安全生产以及产品的质量,对液位进行及时有效地控制是非常必要的。
水箱液位控制是液位控制中的一个主要问题,它在工业过程中普遍存在,具有代表性且非常实用[3]。
液位控制的策略对液位精度有着重要的影响,因此,根据不同的需要选择适当的控制算法极为重要[4]。
模糊控制作为一种典型的智能控制方法,因其不依赖于过程模型、鲁棒性好、抗干扰能力强等优点而备受关注。
目前模糊控制的理论研究较为深入,但模糊控制的应用尚不成熟。
本文将模糊控制理论应用于过程控制装置的单容水箱液位控制系统的设计中,实现对单容水箱的液位模糊控制。
2 液位模糊控制的研究现状2.1研究现状我们的过程控制实验装置是基于工业过程物理模拟对象,集自动化仪表技术、计算机技术、通信技术、自动控制技术为一体的多功能实验装置,包括流量、温度、液位、压力等热工参数。
过程控制系统的被控对象包括上位水箱、中位水箱、下位水箱,控制装置有传感器、调节阀、交流变频器、流量传感器、调节器等。
本文所论述的液位模糊控制系统构造如下:①被控对象为上单容水箱;②采用液位传感器扩散硅压力变送器感测上位水箱和中位水箱液位,仪表变送器通电预热后分别在零压力和满量程压力下检查输出电流值。
在零压力下调整零点电位器,使输出电流为4mA,在满量程压力下调整量程电位器,使输出电流为20mA。
传感器精度为0.5 级。
因为二线制,故工作时需提供24V 直流电源;③采用电/气动调节阀作为执行机构,其输入信号气动为(0.02 ~ 0.1)MPa,电动为0 ~ 10、4 ~ 20mA(带电/ 气阀门定位器);2.2水箱水位模糊控制器的建立本章利用模糊数学工具及模糊控制理论知识,建立一个水箱水位模糊控制器,水位模糊控制器可以设计为二维控制器,即输入量是水位误差和误差变化率,输出量是阀门控制量,但由于过程计算量大,计算复杂所以此章仅采用一维系统,即单输入——单输出统,较复杂的二维系统将在下一章里利用MUTLAB软件构建,并仿真。
智能控制及MATLAB实现—水箱液位模糊控制仿真设计
智能控制及MATLAB实现—水箱液位模糊控制仿真设计智能控制是一种利用先进的智能技术和算法来实现自动控制的方法。
在智能控制中,模糊控制是一种常见且有效的方法之一、模糊控制通过将模糊逻辑应用于控制系统中的输入和输出,根据模糊规则来进行决策和控制。
水箱液位控制是一个典型的控制问题,常常用于工业和民用领域中的自动化系统。
在许多控制应用中,水箱液位的控制是一个关键的问题,因为它需要根据系统的液位情况来实现稳定的控制。
在模糊控制中,首先需要建立一套模糊规则系统,该系统包括模糊化、模糊推理和解模糊化这三个步骤。
模糊化是将实际输入转换为模糊集合的过程。
在水箱液位控制中,可以将液位分为低、中和高三个模糊集合。
通过将实际液位值映射到这些模糊集合中的一个,来表示液位状态。
模糊推理是根据一组模糊规则,将模糊输入转换为模糊输出的过程。
通过将输入和规则进行匹配,确定输出的模糊集合。
在水箱液位控制中,可以使用如下规则:如果液位低且液位变化小,则控制信号为增大水流量;如果液位高且液位变化大,则控制信号为减小水流量;如果液位中等且液位变化适中,则控制信号为不变。
解模糊化是将模糊输出转换为实际的控制信号的过程。
在水箱液位控制中,可以使用模糊加权平均值的方法来进行解模糊化。
通过将模糊集合和其对应的权重进行加权平均计算,得到最终的控制信号。
在MATLAB中,可以使用Fuzzy Logic Toolbox来实现水箱液位模糊控制仿真设计。
首先需要建立输入和输出的模糊化和解模糊化函数,然后根据实际的模糊规则,构建模糊系统。
最后通过设定输入的模糊值,使用模糊系统进行推理和解模糊,得到最终的控制信号。
总结起来,智能控制及MATLAB实现水箱液位模糊控制仿真设计包括建立模糊规则系统,进行模糊化、模糊推理和解模糊化三个步骤,通过Fuzzy Logic Toolbox来实现模糊控制系统的构建和仿真。
通过利用模糊控制的方法,可以实现水箱液位的自动稳定控制,并提高了控制系统的鲁棒性和适应性。
智能控制及MATLAB实现—水箱液位模糊控制仿真设计
水箱水位模糊控制系统设计一.在MATLAB命令窗口中输入sltank,便可打开如图所示的模型窗口。
图1 sltank仿真图(1)打开MATLAB,输入指令fuzzy,打开模糊逻辑工具箱的图形用户界面窗口,新建一个Mamdani模糊推理系统。
(2)增加一个输入变量,将输入变量命名为水位误差、误差变化,将输出变量命名为阀门开关速度。
这样就建立了一个两输入单输出的模糊推理系统,保存为shuiwei1。
图2 增加一个输入变量(3)设计模糊化模块;设水位误差level的论域为[2、95 3、05],误差变化率rate的论域为[-0、2 0、2];两个输入量的模糊集为level设为为7个,rate设为5个:其中水位误差level定为NB、NM、NS、ZE、PS、PM、PB;参数分别为[0、01 2、95]、[0、01 2、97],[0、01 2、99]、[0、01 3]、[0、01 3、01]、[0、01 3、03]、[0、01 3、05],隶属度均为高斯函数;图3 输入量level的参数设定误差变化率rate分别为负大,负小,不变,正小,正大。
参数分别为,[0、03 -0、2]、[0、03 -0、1]、[0、03 0]、[0、03 0、1]、[0、03 -0、2],隶属度函数均为高斯函数。
图4 误差变化率rate的参数设定阀门的开关速度设为七个等级:快关,中关,慢关,不动,慢开,中开,快开,其论域为[2、95 3、05]。
参数分别为;[2、94 2、95 2、96]、[2、965 2、97 2、975]、[2、99 2、99 2、995]、[2、999 3 3、001]、[3、005 3、01 3、015]、[3、02 3、03 3、035]、[3、04 3、05 3、06],隶属函数为三角形函数。
图5 输出量valve的参数设定(4)设计模糊规则打开Ruel Editor窗口,通过选择添加模糊规则;1)If (level is NB) and (rate is 负大) then (valve is 快关) (1)2)If (level is NB) and (rate is 负小) then (valve is 快关) (1) 3)If (level is NB) and (rate is 不变) then (valve is 快关) (1) 4)If (level is NB) and (rate is 正小) then (valve is 中关) (1)5)If (level is NB) and (rate is 正大) then (valve is 不动) (1) 6)If (level is NM) and (rate is 负大) then (valve is 快关) (1) 7)If (level is NM) and (rate is 负小) then (valve is 快关) (1) 8)If (level is NM) and (rate is 不变) then (valve is 快关) (1) 9)If (level is NM) and (rate is 正小) then (valve is 中关) (1)10)If (level is NM) and (rate is 正大) then (valve is 不动) (1) 11)If (level is NS) and (rate is 负大) then (valve is 中关) (1) 12)If (level is NS) and (rate is 负小) then (valve is 中关) (1) 13)If (level is NS) and (rate is 不变) then (valve is 中关) (1) 14)If (level is NS) and (rate is 正小) then (valve is 不动) (1) 15)If (level is NS) and (rate is 正大) then (valve is 慢开) (1) 16)If (level is ZE) and (rate is 负大) then (valve is 中关) (1) 17)If (level is ZE) and (rate is 负小) then (valve is 慢关) (1) 18)If (level is ZE) and (rate is 不变) then (valve is 不动) (1)19)If (level is ZE) and (rate is 正小) then (valve is 慢开) (1) 20)If (level is ZE) and (rate is 正大) then (valve is 中开) (1) 21)If (level is PS) and (rate is 负大) then (valve is 慢关) (1) 22)If (level is PS) and (rate is 负小) then (valve is 不动) (1) 23)If (level is PS) and (rate is 不变) then (valve is 中开) (1) 24)If (level is PS) and (rate is 正小) then (valve is 中开) (1) 25)If (level is PS) and (rate is 正大) then (valve is 中开) (1) 26)If (level is PM) and (rate is 负大) then (valve is 不动) (1) 27)If (level is PM) and (rate is 负小) then (valve is 中开) (1) 28)If (level is PM) and (rate is 不变) then (valve is 快开) (1) 29)If (level is PM) and (rate is 正小) then (valve is 快开) (1) 30)If (level is PM) and (rate is 正大) then (valve is 快开) (1) 31)If (level is PB) and (rate is 负大) then (valve is 不动) (1) 32)If (level is PB) and (rate is 负小) then (valve is 中开) (1) 33)If (level is PB) and (rate is 不变) then (valve is 快开) (1) 34)If (level is PB) and (rate is 正小) then (valve is 快开) (1) 35)If (level is PB) and (rate is 正大) then (valve is 快开) (1) 这35条模糊控制规则的权重都为1、图6 模糊控制规则的设定(5)利用编辑器的 to Workspace, 将当前的模糊推理系统,以shuiwei1保存到工作空间中。
单容水箱液位控制系统设计
单容水箱液位控制系统设计分类号密级UDC过程控制系统设计作业单容水箱液位控制系统设计学生姓名 xxxxxx 学号xxxxxxxxxxxx任课教师 xxxx院、系、中心工程学院自动化及测控系专业年级 xxxx级自动化提交日期 10 月日中国海洋大学文档历史单容水箱液位控制系统设计摘要本论文以单容水箱为被控对象,给出了单闭环控制系统、串级控制系统和前馈反馈控制系统的设计方案,实现对水箱液位的控制。
本论文还针对每种控制系统,在Matlab的Simulink中建立仿真模型进行仿真,得到仿真曲线,而且利用仿真曲线分析控制系统的性能,例如最大动态偏差、调节时间、衰减率和积分性能指标IAE等。
单闭环控制系统的设计包括P、I、PI和PID的设计。
本文分别经过衰减频率特性法(理论整定法)和衰减曲线法(工程整定法)对控制器参数进行了整定。
本论文还经过比较各控制系统的仿真曲线和系统性能指标,对各种控制系统设计方案进行了比较,发现串级控制和前馈反馈控制可提高系统性能。
关键词: PID;串级;前馈反馈;参数整定;SimulinkDesign on Water Level Control in a TankAbstractThis thesis provides design methods of single closed-loop control system, cascade control system and feed forward control system about the controlled object asingle water tank , and it achieves the goal of controlling level. For every kind of control system, simulation model is established by using simulation tool Matlab, simulation curves can analysis the performance of control system, such as the maximum percent overshoot, settling time, attenuation rate and IAE. The design of single closed-loop control system includes designs of P, I, PI and PID. The controller parameter is tuned by frequency response of attenuation rate and the attenuation curve .All the control design methods included are compared by simulation curves and performance indexes and we finally find that cascade control and feed forward control are able to improve system’s performance.Keywords:PID;Cascade;Feedforward- feedback;Parameter tuning;Simulink。
单容水箱液位控制系统设计
单容水箱液位控制系统设计一、引言单容水箱液位控制系统是一种常见的工业自动化控制系统。
它主要用于监测和控制水箱的液位,确保水箱中的液位保持在特定的范围内。
本文将介绍单容水箱液位控制系统的设计原理、硬件电路设计、软件设计以及系统测试和实施。
二、设计原理1.传感器模块传感器模块用于监测水箱中的液位。
一种常用的传感器是浮球传感器,它随着液位的变化而移动,从而输出不同的电信号。
传感器模块将传感器输出的信号转换为数字信号,并传送给控制器模块进行处理。
2.控制器模块控制器模块是整个系统的核心,它接收传感器模块传来的信号,并根据预设的液位范围进行判断和控制。
控制器模块通常使用单片机或者嵌入式系统来实现。
它可以通过开关控制执行器模块的工作状态,以调节水箱的液位。
3.执行器模块执行器模块用于控制水箱的进水和排水。
在液位过低时,执行器模块打开水泵,使水箱进水;在液位过高时,执行器模块关闭水泵,使水箱排水。
执行器模块可以采用继电器、驱动电机等元件来实现。
三、硬件电路设计1.传感器模块传感器模块将传感器的信号转换为数字信号。
可以使用模拟到数字转换器(ADC)将传感器输出的模拟电压转换为数字信号,然后通过串口等方式传送给控制器模块。
2.控制器模块控制器模块可以使用单片机或者嵌入式系统来实现。
它需要包括输入接口、控制逻辑和输出接口。
输入接口负责接收传感器模块传来的信号,控制逻辑通过判断液位范围来控制执行器模块的工作状态,输出接口负责向执行器模块发送控制信号。
3.执行器模块执行器模块根据控制器模块的信号控制水箱的进水和排水。
可以使用继电器或驱动电机等元件来实现。
进水时,可以通过开启水泵或开启电磁阀等方式;排水时,可以通过关闭水泵或关闭电磁阀等方式。
四、软件设计软件设计主要包括控制器模块的程序设计。
程序需要实时监测传感器模块的信号,并根据预设的液位范围进行判断和控制。
可以使用状态机或者PID控制算法来实现。
1.状态机状态机通过定义不同的状态和状态转移条件来实现控制逻辑。
水箱水位恒定的模糊PID控制
学校代码 10126 学号 00824032 分类号 TP273+.4 密级本科毕业论文(设计)学院、系电子信息工程学院自动化系专业名称自动化年级 08 级学生姓名指导教师2012年05月30日摘要论文设计了一个参数自整定的模糊PID控制器来完成对单容水箱水位恒定的控制,并对其进行了SIMULINK仿真,与常规PID控制的仿真结果进行了对比与分析。
它的原理是在PID算法的基础上,以误差e及误差的变化率ec作为输入,利用模糊规则进行模糊推理,在运行中不断检测e和ec,并以PID参数的修正值ΔKp、ΔKi、ΔKd为输出,以满足不同时刻偏差和偏差变化率变化对PID参数整定的要求。
最终得到PID控制器的三个参数, Kp= Kp′+ΔKp ,Ki= Ki′+ΔKi ,Kd= Kd′+ΔKd,其中Kp′,Ki′,Kd′为预整定值。
仿真结果表明,参数自整定PID控制系统的动态性能得到高。
关键词:水位控制,模糊PID,SIMULINKAbstractAuthor:Tutor: This paper designes a parameter self-setting fuzzy PID controller to keep the level of water tank as a constant , and analyses the SIMULINK, and compared with conventional PID control ler’s simulation results . It’s principle is based on PID algorithm and it take s error e and error rate ec as inputs. Using the fuzzy rules for fuzzy reasoning, and constantly testing e and ec, then export PID parameters (ΔKp, ΔKi, ΔKd) to meet error and error rate’s requirements at PID parameters. Finally achieved the PID controller’s three parameters, Kp = Kp '+Δ Kp, Ki = Ki' + ΔKi, Kd = Kd '+ ΔKd, Among them ,Kp', Ki', Kd' is the initial value of PID controller.The simulation results show that the parameter self-setting PID control system dynamic performance is improved.Key words:water level control, fuzzy PID, SIMULINK目录第1章绪论 (1)1.1课题的研究背景及意义 (1)1.2 PID控制的特点 (1)1.3模糊控制技术的特点及展望 (2)第2章被控对象的分析与建模 (4)第3章模糊控制理论 (6)3.1模糊集合定义 (6)3.2 模糊语言 (6)3.3模糊变量的隶属函数 (7)3.5论域、量化因子、比例因子的选择 (7)3.5.1论域及基本论域 (7)3.5.2量化因子及比例因子 (8)第4章参数自整定模糊PID控制器的设计内容 (10)4.1参数自整定模糊PID控制原理 (10)4.2模糊控制器的结构设计及模糊变量的论域设计 (10)4.2.1模糊控制器的结构设计 (10)4.2.2 模糊控制器模糊变量的论域设计 (11)4.3 模糊集选择及隶属函数设计 ....................................................... 错误!未定义书签。
单容水箱液位控制系统实验设计
单容水箱液位控制系统实验设计【摘要】通过对单容水箱液位控制系统特性的测试掌握单容水箱阶跃响应测试方法,并记录相应液位的响应曲线。
根据实验得到的液位阶跃响应曲线,用相关的方法确定被测对象的特征参数T和传递函数。
【关键词】单容水箱;液位控制;数字模型1.单容水箱液位控制系统组成本实验装置由被控对象和上位控制系统两部分组成。
系统动力支路分两路:一路由三相(380V交流)磁力驱动泵、气动调节阀、直流电磁阀、PA电磁流量计及手动调节阀组成;另一路由变频器、三相磁力驱动泵(220V变频)、涡轮流量计及手动调节阀组成。
1.1被控对象被控对象由不锈钢储水箱、圆筒形有机玻璃水箱和敷塑不锈钢管路组成。
水箱:包括上水箱和储水箱。
上水箱采用淡蓝色圆筒型有机玻璃,不但坚实耐用,而且透明度高,便于学生直能接观察到液位的变化和记录结果。
分别是缓冲槽,工作槽,出水槽。
管道:整个系统管道采用敷塑不锈钢管组成,所有的水阀采用优质球阀,彻底避免了管道系统生锈的可能性。
有效提高了实验装置的使用年限。
其中储水箱底有一个出水阀,当水箱需要更换水时,将球阀打开让水直接排出。
1.2检测装置压力传感器、变送器:采用SIEMENS带PROFIBUS-PA通讯协议的压力传感器和工业用的扩散硅压力变送器,扩散硅压力变送器含不锈钢隔离膜片,同时采用信号隔离技术,对传感器温度漂移跟随补偿。
1.3执行机构调节阀:采用SIEMENS带PROFIBUS-PA通讯协议的气动调节阀,用来进行控制回路流量的调节。
它具有精度高、体积小、重量轻、推动力大、耗气量少、可靠性高、操作方便等。
水泵:本装置采用磁力驱动泵,型号为16CQ-8P,流量为32升/分,扬程为8米,功率为180W。
泵体完全采用不锈钢材料,以防止生锈,使用寿命长。
可移相SCR调压装置:采用可控硅移相触发装置,输入控制信号为4~20mA标准电流信号。
输出电压用来控制加热器加热,从而控制锅炉的温度。
电磁阀:在本装置中作为气动调节阀的旁路,起到阶跃干扰的作用。
单容液位控制系统设计
目录1系统设计认识 (1)1.1前言 (1)2系统方案确定、系统建模和原理介绍 (1)2.1控制方案确定 (1)2.2控制系统建模 (1)2.2.1被控对象 (1)2.2.2系统建模 (2)3系统构成 (4)3.1控制系统结构 (4)3.2控制系统方框图 (4)4系统各环节分析 (5)4.1调节器PID控制 (5)4.2执行器分析 (6)4.3检测变送环节分析 (6)4.4被控对象分析 (6)5系统仿真 (7)5.1系统结构图以及参数整定 (7)6仪器仪表选型 (10)6.1 PID调节器选择 (10)6.2执行器选择 (11)6.2.1变频器的选择 (11)6.2.2电机的选择 (11)6.2.3泵的选择 (12)6.3差压变送器的选择 (12)7课程设计结束语 (14)参考文献 (15)一、系统设计认识1.1前言过程控制早已在矿业、冶金、机械、化工、电力等方面得到了广泛应用。
在液位控制方面,比如:水塔供水、工矿企业排给水、锅炉汽包液位控制、精馏塔液位控制等更是发挥着重要作用。
在这些生产领域里,基本上都是劳动强度大或者操作有一定危险性的工作,极易出现操作失误引起事故,造成厂家的经济损失。
可见,在实际生产中,液位控制的准确程度和控制效果直接影响着工厂的生产成本、经济效益以及设备的安全系数。
所以,为了保证安全条件、方便操作,就必须研究开发先进的液位控制方法和策略。
本设计以单容水箱的液位控制系统为研究对象。
由于单回路反馈控制系统结构简单、投资少、操作方便,且能满足一般的生产过程要求,在液位控制中得到了广泛的应用,所以本设计单容水箱的液位控制系统采用的就是单回路反馈控制。
它的控制任务就是使水箱液位保持在给定值所要求的高度,并且减少或消除来自系统内部和外部扰动的影响。
通过系统方案的选择,完成系统的工艺流程图设计和方框图的确定,各环节仪表仪器的选型,控制算法的选取,系统的仿真以及控制参数的整定等工作。
二、系统方案确定、系统建模和原理介绍2.1控制方案确定如前言所介绍,由于单回路反馈控制系统结构简单、投资少、操作方便,且能满足一般的生产过程要求,在液位控制中得到了广泛的应用,故采用单回路反馈控制。
单容水箱液位控制系统设计
单容水箱液位控制系统设计一、引言水箱是常见的储水设备,广泛应用于家庭、工业和农业等领域。
为了保证水箱的水位稳定和安全,需要设计一种液位控制系统来监测和控制水箱的液位。
本文将介绍一个单容水箱液位控制系统的设计思路和实现方法。
二、系统设计思路1.系统功能要求2.系统组成液位传感器用于检测水箱的液位,并将检测到的液位信号传输给控制器。
控制器根据液位传感器的信号以及设定范围来判断蓄水或排水的需求,并通过控制阀门的开闭来实现液位的控制。
执行器是用于控制阀门开闭的装置,可以是电磁阀、电动阀或脚踏阀等。
人机界面用于显示水箱的液位信息和设置控制参数,可以是液晶显示屏或者计算机控制界面。
3.系统工作原理水箱液位控制系统的工作原理如下:当水箱液位低于设定范围的下限时,控制器会发送信号给执行器,使其打开阀门,进水进入水箱。
当水箱液位达到设定范围的上限时,控制器会发送信号给执行器,使其关闭阀门,停止进水进入水箱。
当水箱液位高于设定范围的上限时,控制器会发送信号给执行器,使其打开阀门,排水排出水箱。
当水箱液位低于设定范围的下限时,控制器会发送信号给执行器,使其关闭阀门,停止排水排出水箱。
三、系统实现方法1.液位传感器的选择与安装在单容水箱液位控制系统中,可以使用浮球式液位传感器或者压力式液位传感器。
浮球式液位传感器安装在水箱内部,通过浮球的上下运动来检测液位变化。
压力式液位传感器安装在水箱外部,通过测量水箱外部水压来间接推算液位变化。
2.控制器的设计与实现控制器可以使用微控制器或者可编程逻辑控制器(PLC)来实现。
控制器需要实现以下功能:(1)接收液位传感器的信号,并进行信号处理和滤波;(2)判断水箱液位是否低于设定范围的下限或高于设定范围的上限;(3)根据判断结果控制执行器的开闭。
3.执行器的选择与控制执行器可以根据具体需求选择合适的类型,如电磁阀、电动阀或脚踏阀。
执行器控制的开闭可以通过控制信号来实现。
4.人机界面的设计与实现人机界面可以使用液晶显示屏或者计算机控制界面来显示水箱的液位信息和设置控制参数。
单容水箱液位控制系统设计
过程控制系统设计作业单容水箱液位控制系统设计学生姓名文强学号2212130任课教师陶珑院、系、中心专科部专业生产过程自动化提交日期2015年10 月日太原科技大学单容水箱液位控制系统设计摘要本论文以单容水箱为被控对象,给出了单闭环控制系统、串级控制系统和前馈反馈控制系统的设计方案,实现对水箱液位的控制。
本论文还针对每种控制系统,在Matlab的Simulink中建立仿真模型进行仿真,得到仿真曲线,并且利用仿真曲线分析控制系统的性能,例如最大动态偏差、调节时间、衰减率和积分性能指标IAE 等。
单闭环控制系统的设计包括P、I、PI和PID的设计。
本文分别通过衰减频率特性法(理论整定法)和衰减曲线法(工程整定法)对控制器参数进行了整定。
本论文还通过比较各控制系统的仿真曲线和系统性能指标,对各种控制系统设计方案进行了比较,发现串级控制和前馈反馈控制可提高系统性能。
关键词: PID;串级;前馈反馈;参数整定;SimulinkDesign on Water Level Control in a TankAbstractThis thesis provides design methods of single closed-loop control system, cascade control system and feed forward control system about the controlled object asingle water tank , and it achieves the goal of controlling level. For every kind of control system, simulation model is established by using simulation tool Matlab, simulation curves can analysis the performance of control system, such as the maximum percent overshoot, settling time, attenuation rate and IAE. The design of single closed-loop control system includes designs of P, I, PI and PID. The controller parameter is tuned by frequency response of attenuation rate and the attenuation curve .All the control design methods included are compared by simulation curves and performance indexes and we finally find that cascade control and feed forward control are able to improve system’s performance.Keywords:PID;Cascade;Feedforward- feedback;Parameter tuning;Simulink目录摘要 (I)ABSTRACT ............................................................................................................................ I I 1设计要求及内容 (1)2单容水箱系统建模 (3)3单闭环控制系统设计 (5)3.1比例控制系统设计 (5)3.2积分控制系统设计 (7)3.3比例-积分控制系统设计 (9)3.4比例-积分-微分控制系统设计 (12)4串级控制控制方案设计 (16)5前馈控制方案设计 (18)6实验室水箱实验报告 (19)6.1压力单闭环实验 (19)6.2液位单闭环实验 (20)6.3上水箱液位和流量组成串级实验 (22)6.4前馈反馈控制实验 (24)7总结 (26)参考文献 (27)附录 (28)1设计要求及内容图1 单容水箱液位控制系统单容水箱液位控制系统如题图1所示。
课程设计-单容水箱液位控制-MCGS
综合实验报告综合实验名称自动控制系统综合实验题目单容水箱液位定值控制系统指导教师设计起止日期2013年1月7日~1月18日系别自动化学院控制工程系专业自动化学生姓名班级学号自控成绩目录目录 (2)正文 (3)设计内容 (4)应用MCGS组态软件 (4)构建实时数据库 (8)设备窗口 (11)策略及脚本 (15)综合测试 (20)实验结果 (21)总结 (23)参考文献 (23)正文第一部分一、课题单容水箱液位定值控制系统二、设计目的课程设计旨在使学生在深入消化课堂教学内容的基础上,综合应用所学课程的基本原理与方法,解决实际设计与应用问题,提高学生分析问题与解决问题的能力,并在设计工作中,学会查阅资料、系统设计、调试与分析、撰写报告等,达到综合能力培养的目的。
1.根据自动控制系统的设计要求,学会方案比较和论证,初步掌握工程设计的基本方法;2.掌握各种变送器以及自动化仪表的工作原理和调校;3.掌握自动控制系统集成技术;4.掌握控制系统的通信技术,学会PCI数据采集卡或远程数据采集模块的应用;5.应用MCGS软件,学会控制算法的设计和调试;6.熟悉MCGS组态软件,学会监控界面、通信驱动程序等的设计;7.提高总结归纳、撰写设计报告的能力,应当规范、有条理、充分、清楚地论述设计内容和调试成果。
三、课设设备TH PCAT-2型现场总线控制系统实验装置(常规仪表侧),双容水箱;AT-1挂件,智能仪表,485通信线缆一根(或者如果用数据采集卡做,AT-4 挂件,PCL通讯线一根)四、课设所需软件MCGS组态软件五、设计内容课设原理说明单容水箱液位定值控制系统如下:图2—1 上水箱单容液位定值控制系统(a)结构图(b)方框图本实验系统结构图和方框图如图所示。
被控量为左上水箱(也可采用右上水箱或者下水箱)的液位高度,实验要求它的液位稳定在给定值。
将压力传感器LT1检测到的左上水箱液位信号作为反馈信号,在与给定量比较后的差值通过调节器控制气动调节阀的开度,以达到控水箱液位的目的。
液位控制系统中英文对照外文翻译文献
液位控制系统中英⽂对照外⽂翻译⽂献中英⽂对照翻译The liquid level control system based ondde\matlab\simulinkProcess control is an important application field of automatic technology, it is to point to the level, temperature, flow control process variables, such as in metallurgy, machinery, chemical, electric power, etc can be widely used. Especially liquid level control technology in real life, played an important role in production, for example, the water supply, civil water tower if low water levels, can affect people's lives in water; Industrial enterprises with water, if the drainage water drainage or controlled properly or not, in relation to the workshop of condition; Boiler drum, if the control level boiler is too low, can make level boiler overheating, possible accident; Jing flow, liquid level control tower control accuracy and level of the craft can influence the quality of the products and the cost, etc. In these production field, are basically labor strength or the operation has certain risk nature of work, extremely prone to accidents caused by operating error, the losses, killing manufacturer. Visible, in actual production, liquid level control accuracy and control effects directly affect the factory production cost and economic benefit of safety coefficient. Even equipment So, in order to ensure safety, convenient operation, you have to research the development of a d v a n c e d l e v e l c o n t r o l m e t h o d s a n d s t r a t e g i e s.The graduation design topic is the liquid level control system based on dde\matlab\simulink\force control, Among them was controlled object for tank level, Communication mode for DDE communications , Matlab is mainly used in the simulation test ,And force control software used for modeling, This system mainly through combination of hardware and software device to achieve precise control of liquid level , In modern industry level control of important component, it influence upon production not allow to ignore, in order to ensure safety in production and the product quality and quantity, the level and perform effective control is very necessary, The following is a description of all aspects:⼀PID controllerA proportional–integral–derivative controller (PID controller) is a generic .control loop feedback mechanism widely used in industrial control systems.A PID controller attempts to correct the error between a measured process variable and a desired set point by calculating and then outputting a corrective action that can adjust the process accordingly.The PID controller calculation (algorithm) involves three separate parameters; the Proportional, the Integral and Derivative values. The Proportional value determines the reaction to the current error, the Integral determines the reaction based on the sum of recent errors and the Derivative determines the reaction to the rate at which the error has been changing. The weighted sum of these three actions is used to adjust the process via a control element such as the position of a control valve or the power supply of a heating element. By "tuning" the three constants in the PID controller algorithm the PID can provide control action designed for specific process requirements. The response of the controller can be described in terms of the responsiveness of the controller to an error, the degree to which the controller overshoots the set point and the degree of system oscillation. Note that the use of the PID algorithm for control does not guarantee optimal control of the system or system stability.Some applications may require using only one or two modes to provide the appropriate system control. This is achieved by setting the gain of undesired control outputs to zero. A PID controller will be called a PI, PD, P or I controller in the absence of the respective control actions. PI controllers are particularly common, since derivative action is very sensitive to measurement noise, and the absence of an integral value may prevent the system from reaching its target value due to the control action.1.Control loop basicsA familiar example of a control loop is the action taken to keep one's shower water at the ideal temperature, which typically involves the mixing of two process streams, cold and hot water. The person feels the water to estimate its temperature. Based on this measurement they perform a control action: use the cold water tap to adjust the process. The person would repeat this input-output control loop, adjusting the hot water flow until the process temperature stabilized at the desired value.Feeling the water temperature is taking a measurement of the process value or process variable (PV). The desired temperature is called the set point (SP). The output from the controller and input to the process (the tap position) is called the manipulated variable (MV). The difference between the measurement and the set point is the error (e), too hot or too cold and by how much. As a controller, one decides roughly how much to change the tap position (MV) after one determines the temperature (PV), and therefore the error. This first estimate is the equivalent of the proportional action of a PID controller. The integral action of a PID controller can be thought of as gradually adjusting the temperature when it is almost right.Derivative action can be thought of as noticing the water temperature is getting hotter or colder, and how fast, and taking that into account when deciding how to adjust the tap,Making a change that is too large when the error is small is equivalent to a high gain controller and will lead to overshoot. If the controller were to repeatedly make changes that were too large and repeatedly overshoot the target, this control loop would be termed unstable and the output would oscillate around the set point in either a constant, growing, or decaying sinusoid. A human would not do this because we are adaptive controllers, learning from the process history, but PID controllers do not have the ability to learn and must be set up correctly. Selecting the correct gains for effective control is known as tuning the controller.If a controller starts from a stable state at zero error (PV = SP), then further changes by the controller will be in response to changes in other measured or unmeasured inputs to the process that impact on the process, and hence on the PV. Variables that impact on the process other than the MV are known as disturbances and generally controllers are used to reject disturbances and/or implement set point changes. Changes in feed water temperature constitute a disturbance to the shower process.In theory, a controller can be used to control any process which has a measurable output (PV), a known ideal value for that output (SP) and an input to the process (MV) that will affect the relevant PV. Controllers are used in industry to regulate temperature, pressure, flow rate, chemical composition, speed and practically every other variable for which a measurement exists. Automobile cruise control is an example of a process which utilizes automated control.Due to their long history, simplicity, well grounded theory and simple setup and maintenance requirements, PID controllers are the controllers of choice for many ofthese applications.2.PID controller theoryNote: This section describes the ideal parallel or non-interacting form of the PID controller. For other forms please see the Section "Alternative notation and PID forms".The PID control scheme is named after its three correcting terms, whose sum constitutes the manipulated variable (MV). Hence:where Pout, Iout, and Dout are the contributions to the output from the PID controller from each of the three terms, as defined below.2.1. Proportional termThe proportional term makes a change to the output that is proportional to the current error value. The proportional response can be adjusted by multiplying the error by a constant Kp, called the proportional gain.The proportional term is given by:WherePout: Proportional outputKp: Proportional Gain, a tuning parametere: Error = SP ? PVt: Time or instantaneous time (the present)Change of response for varying KpA high proportional gain results in a large change in the output for a given change in the error. If the proportional gain is too high, the system can become unstable (See the section on Loop Tuning). In contrast, a small gain results in a small output response to a large input error, and a less responsive (or sensitive) controller. If the proportional gain is too low, the control action may be too small when responding to system disturbances.In the absence of disturbances, pure proportional control will not settle at its target value, but will retain a steady state error that is a function of the proportional gain and the process gain. Despite the steady-state offset, both tuning theory and industrial practice indicate that it is the proportional term that should contribute the bulk of the output change.2.2.Integral termThe contribution from the integral term is proportional to both the magnitude of the error and the duration of the error. Summing the instantaneous error over time (integrating the error) gives the accumulated offset that should have been corrected previously. The accumulated error is then multiplied by the integral gain and added to the controller output. The magnitude of the contribution of the integral term to the overall control action is determined by the integral gain, Ki.The integral term is given by:Iout: Integral outputKi: Integral Gain, a tuning parametere: Error = SP ? PVτ: Time in the past contributing to the integral responseThe integral term (when added to the proportional term) accelerates the movement of the process towards set point and eliminates the residual steady-state error that occurs with a proportional only controller. However, since the integral term is responding to accumulated errors from the past, it can cause the present value to overshoot the set point value (cross over the set point and then create a deviation in the other direction). For further notes regarding integral gain tuning and controller stability, see the section on loop tuning.2.3 Derivative termThe rate of change of the process error is calculated by determining the slope of the error over time (i.e. its first derivative with respect to time) and multiplying this rate of change by the derivative gain Kd. The magnitude of the contribution of the derivative term to the overall control action is termed the derivative gain, Kd.The derivative term is given by:Dout: Derivative outputKd: Derivative Gain, a tuning parametere: Error = SP ? PVt: Time or instantaneous time (the present)The derivative term slows the rate of change of the controller output and this effect is most noticeable close to the controller setpoint. Hence, derivative control isused to reduce the magnitude of the overshoot produced by the integral component and improve the combined controller-process stability. However, differentiation of a signal amplifies noise and thus this term in the controller is highly sensitive to noise in the error term, and can cause a process to become unstable if the noise and the derivative gain are sufficiently large.2.4 SummaryThe output from the three terms, the proportional, the integral and the derivative terms are summed to calculate the output of the PID controller. Defining u(t) as the controller output, the final form of the PID algorithm is:and the tuning parameters areKp: Proportional Gain - Larger Kp typically means faster response since thelarger the error, the larger the Proportional term compensation. An excessively large proportional gain will lead to process instability and oscillation.Ki: Integral Gain - Larger Ki implies steady state errors are eliminated quicker. The trade-off is larger overshoot: any negative error integrated during transient response must be integrated away by positive error before we reach steady state.Kd: Derivative Gain - Larger Kd decreases overshoot, but slows down transient response and may lead to instability due to signal noise amplification in the differentiation of the error.⼆Matlab IntroductionThe MATLAB? environment is well suited to rapid prototyping and application development. The interactive programming environment, built-in math functions, toolboxes, editing and debugging tools, and deployment options all contribute to reducing your overall development time.By using the built-in math functions and the many specialized functions contained within our toolboxes, MATLAB can significantly reduce the time it takes you to develop prototypes. In addition to integrated editing and debugging tools, MATLAB provides a performance profiler to help you further optimize your code when programming in MATLAB.Building applications around complex algorithms and graphics is easier than everwith the GUI builder, GUIDE. GUIDE was redesigned in MATLAB 6 to save you time. It offers all the drag and drop interface options you would expect, such as text boxes, radio buttons, check boxes, listboxes, sliders, pop-up menus, frames and more.When you're ready to deploy your application, the MathWorks offers a number of different options that allow you to either convert or interface your MATLAB application to other environments including C/C++ and the Web. MATLAB is the most productive development environment for creating scientific and engineering applications because it offers powerful tools for every step in the process to reduce your overall development time.MATLAB is a high-performance language for technical computing. It integrates computation, visualization, and programming in an easy-to-use environment where problems and solutions are expressed in familiar mathematical notation. Typical uses includeMath and computationAlgorithm developmentData acquisitionModeling, sim ulation, and prototypingData analysis, exploration, and visualizationScientific and engineering graphicsApplication development, including graphical user interface building三DDE IntroductionDynamic data exchange (DDE, Dynamic data exchange) is real-time exchange data between applications, it is the effective method between different applications to share data a agreement. DDE agreement is a kind of open, and language unrelated, based on protocol, it allows multiple applications to any human agreed format data exchange or command. It is application through Shared memory process of the communication between a form, also need not user intervention of good data exchange method.DDE applications can be divided into four types: client and server and client/server and the monitor. Conversation is a basic concept of DDE. DDE conversation happened in client applications and server application between. Customer is responsible for initializing and attendant session and control conversation flow, from the server application request data or services; The server applicationresponse client applications of data or service request. Client/server applications is both client applications and server application request, it can be and can provide information. Monitor application for debugging purposes. DDE applications can have multiple burst conversation, a service applications can also have multiple client applications, a client applications can to multiple requests data service applications, and an application can also act as client applications and services applications, when don't need the service application data or service, the customer will terminate session. DDE agreement must be synchronous control the news session, but in different application can switch between asynchronous session. DDE Application using the three layer identification system: Application name apply), theme name (from) and project name (Item). Application name (also called service name) is located at the top of the hierarchical structure, the service application registration for pointed out that particular DDE server application name, customer the application wants to establish session with the server application must be specified application name when this string marks; Name in every conversation topics is one and to identify logical data connection string, is the total classification, data it defines a server application conversation theme content, the server application can support one or more theme name; Project name identifies exchange unit of data string, furthermore confirm the conversation of detailed information, every theme name may have one or more project name.Example: for a database interface applications, will it supports database name as a theme name, and will all sorts of SQL commands as project name, because the server application can support one or more theme, and each theme name name may have one or more project name; So, when to change or reconstruct a conversation, just changing the subject name or project name can.四force control IntroductionForce control is Beijing SANWEI force control technology and "soft" control strategy software, real-time database and its management system, Web portal of tools and other products. These products are not isolated, and the force control is an application scale can free the system structure, the whole expansion force control system and its various products are made from some components procedures according to certain combinations and become. So this guide is not specifically targeted specific products separately describes the use of method, but the common use of all products introduced method. Force control configuration software is a can run on Windows 98/2000 / NT environment, and can run on Windows CE, DOS embedded environment control fu- nctions such as software modules. It USES function diagram way for users provide interface, possess and real-time database, graphical interface system and communication function.Force charged with monitoring configuration software is to the field production data acquisition and process control of specialized software, the biggest characteristic is to flexible "configuration mode" instead of programming approach to system integration, and it provides a good user interface and simple engineering development, as long as the realization method of software module of pre-settings simple "configuration", it can easily realization and complete monitoring layer each function, shorten the automation engineer system integration time, greatly improve the efficiency of integration.Force charged with monitoring configuration software is in the automatic control system monitoring layer level software platform, it can also and the domestic and foreign various industrial control network communication equipment manufacturer, it is ok with high reliable industrial controlling computer and network system integration, can achieve the purpose of the centralized management and monitoring, and can also be convenient to control layer and management for software and hardware to implement all the interface, with "third party" hardware and software systems for integration.The control strategy in the force control, an application in generator may have a lot of control strategy, but only one main strategy. The Lord, the Lord was first execution strategy calls. Other strategies strategy Strategy nested grade 4, namely for most 0 ~ 3 level, in this category 4, grade 3 0 level supreme, the lowest. Senior strategy can call low-level strategy, and low-level strategy can't call senior strategy. In addition to tier 3 most can have 127 strategy outside, other three grades maximum respectively are 255 strategy. Control strategy of by some basic function blocks, a function blocks represent an operation, algorithm or variables. Function blocks basic execution element is strategy, similar to an integrated circuit blocks, have several input and output, each input and output tube feet all have the only name.Force control control strategy is in control strategy, edited generated generators in automatic control strategy for strategies when inventory compiled, and check grammar mistakes, compile can also manually. Control strategy, and you can also call between if A strategy was B strategy calls, says A is B son strategy. A functional block can be repeated calls, each calls are automa- tically entitled to a name by. The executive order and function block in the position of screen on the upper left, position relevant function block, according to priority execution left after the first order under implementation.Force control control strategy of basic function blocks generator was divided into five categories: variable function blocks, mathematical operation function blocks, program control function blocks, logic function blocks function block and control algorithm.基于matlab\dde\simulink\⼒控的液位控制系统过程控制是⾃动技术的重要应⽤领域,它是指对液位、温度、流量等过程变量进⾏控制,在冶⾦、机械、化⼯、电⼒等⽅⾯得到了⼴泛应⽤。
基于MATLAB的水箱水位模糊控制系统的设计
Abstract: This paper designs a suit of water lever fuzzy controller system in the water tank using the fuzzy control theory, and gives
us a system design project which is validated by the MATLAB. The final result shows that the project obtains an excellent anticipant
技
术
图 3 采用模糊-PID 控制的水位实时趋势曲线图Ⅰ
创 上图所示为整个系统运行初始阶段的水位实时曲线图。而 要对控制器的控制效果进行分析、比较,还需要有系统稳定运行
新 阶段的实时Leabharlann 线图,如图 4。图 4 采用模糊-PID 控制的水位实时趋势曲线图Ⅱ
4 结论
由上面的两幅曲线图可以看出, 水箱水位可以较快的上升 到设定的高度,即具有较小的上升时间;水位第一次超过设定水 位较小,即系统的最大动态误差较小;水位能够稳定在给定值附 近,即此系统的稳态误差较小。综上,从以上三个方面和实际的 水位曲线来看,说明了采用此模糊-PID 控制器可以起到很好的 控制效果,是一种比较理想的控制方案。
(收稿日期:2010.03.19)(修稿日期:2010.06.19)
(上接第 17 页) 距离走动的优点,还能够同时消除距离弯曲对成像的影响;并且 由于引入了双通道处理机制,在大大消除杂波的影响的同时,利 用增加的系统自由度,提高参数估计能力,从而实现对运动目标 的精确测速、定位和成像。该方法不改变传统的 SAR 成像流程, 易于在已有的系统上进行更新,具有一定的应用价值。
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英文翻译系别自动化系专业自动化班级学生姓名学号指导教师Single tank water level fuzzy control system designIn industrial process control, the amount usually charged with the following four kinds, namely, level, pressure, flow and temperature. Where in the liquid is not only common in industrial process parameters, and for direct observation, easy to measure. Level control is a common industrial process control, impact on production can not be ignored. For level control system, although the conventional PID control parameters fixed, it is difficult to ensure the control parameters of the system to adapt to changes and changes in working conditions, it is difficult to get the desired effect; fuzzy control parameters have not sensitive and robust and strong features . Single-tank liquid level control system with linearity, hysteresis, coupling characteristics, this paper for the study of the level system, the application of fuzzy control theory to control research.Single tank water system structureTank level control system consists of a single tank water system ontology and AD / DA data acquisition card and other components, allows the computer to set the level value by controlling the regulator, at the entrance of a regulator valve to control and maintain the water level does not change; valve at the outlet of the receiver D-A converter output signal directly controlled tank. Valves on the inlet and discharge control rely on typical self-balancing system.Fuzzy ControlFuzzy logic control referred to fuzzy control, based on fuzzy set theory, fuzzy linguistic variables and fuzzy logic of a computer-based digital control technology. In 1965, the United States LAZadeh founded the fuzzy set theory; 1973 he gives definitions and theorems related to fuzzy logic control. In 1974, the British EHMamdani first statement in accordance with the composition of fuzzy control fuzzy controller, and apply it to the control of boilers and steam engines, get the lab's success. This pioneering work marked the birth of fuzzy control theory.Birth control is fuzzy and the development of social science and technology and the need inseparable. With the rapid development of science and technology in all areas of the automatic control system to control the precision required response speed, system stability and the ability to adapt to increasingly high, the studied systems are increasingly complex. However, due to a number of reasons, such as the charged object or process nonlinear, time-varying, multi-parameter strong coupling between the larger random noise, the intricate mechanism of the process, a variety of uncertainties and imperfect means of in situ measurements, difficult to establish the mathematical model of controlled object. While conventional adaptive control techniques can solve some problems, but the scope is limited. Good manual control for complex effects that are difficult to establish the mathematical model of the controlled object, using the traditional control methods, including methods of modern control theory based control is often better than a practical experience of operating personnel carried out. Because one of the important features of the human brain is the ability to identify and fuzzy things, judgment, fuzzy means can often seem imprecise achieve precise purpose.Contains five main parts, namely: the definition of variables , fuzzy , knowledge , logic and anti- blur . Define a variable that is the situation and determine the procedures to be observed considering control actions, such as the general control problem , the input variables and output error E output error rate of change EC, and fuzzy control variables as inputs U will control the next state . Wherein E, EC, U collectively referred to as fuzzy variables . Fuzzy input value to an appropriate ratio value domain conversion , using colloquial process variables to describe the physical quantity measured , to find the value of the membership degree according to the relative value of the appropriate language , the colloquial variable called fuzzy subset . Including database and rule base knowledge of two parts, one related to the definition of fuzzy database provides data processing ; while the rule base is controlled by agroup of language rules describe the control objectives and strategies. Imitating fuzzy logic judgment under the concept of human beings, the use of fuzzy logic and fuzzy inference inference method to obtain fuzzy control signals. This part is the essence of the fuzzy controller . Defuzzification : Convert fuzzy inference value obtained for the explicit control signals as input value system.Fuzzy controller designFuzzy controller input and error rate of change of the error, the error e = r-y, the rate of change of error ec = de / dt, where, r and y are respectively the level setpoint and measured value. The exact value of the error and error rate of change in the amount of blur blur becomes E and EC, the further you can get E and EC fuzzy language collections. E and EC by the vague language subsets and fuzzy relationship matrix, decision-making based on fuzzy inference rules synthesis, controlled amount of U, the U de vague, converted to the exact amount u, the D-A converter control valve actuators generate action.Fuzzy controller, the input signal quantization error e is 8 level (NB, NM, NS, NO, O, PS, PM, PB); the rate of change of error ec and the output variable u is 7 quantization level (NB , NM, NS, O, PS, PM, PB); error e, and the error rate of change of the output variable u ec domain of [-6,6]. The error e, error change rate ec and output variables membership functions chosen triangular membership functions. Fuzzy control rules are based on fuzzy reasoning, in the design of fuzzy control rules, you should consider the completeness of the control rules, cross and consistency, should ensure that for any given input has a corresponding control rules work. If the error is negative big change, but also for the negative rate of change of the error is large, it is necessary to adjust the control amount being small, in order to ensure the expected systematic development. On the basis of summing up experiences and basic professional knowledge, get control rules (see Table 1), designed a total of 49 (7 × 7) of the Rules.ece NB NM NS O PS PM PB NB PS PS PS PS PM PB PB NM NS PS PS PS PM PM PB NS NM NS O O PS PM PM O NB NM NS O PS PM PM PS NB NM NS O O PS PM PM NB NB NM NS NS PS PS PB NB NB NM NS NS NS NSCommonly used methods of reasoning fuzzy control system CRI reasoning table method, CRI reasoning analytical method, Mamdani inference method and the consequent direct function method. This selection is a direct Mamdani inference method, first find the fuzzy relation R, then the amount calculated according to the input control and clarity. This selection of 49 (7 × 7) of control rules, the fuzzy rule table of conditional statements can be described, for example, if e = NB and ec = NB then u = PS. Corresponding fuzzy relationship: R1 = A1 × B1 × C1, where, A1 is a fuzzy set of E, B1 is a fuzzy set of EC, C1 is a fuzzy set of U; fuzzy matrix R can be integrated according to R.Fuzzy control, simplify the complexity of system design, especially for nonlinear, time-varying lag model does not fully control systems; does not depend on accurate mathematical model of the controlled object; take advantage of the system control law to describe the relationship between variables; no value but with fuzzy variables to describe the language type system, the fuzzy controller does not have to establish a complete mathematical model of the controlled object; fuzzy controller is an easy to control and master the ideal nonlinear controller has better robustness, flexibility, robustness and better fault tolerance.单容水箱液位模糊控制系统设计在工业过程控制中,被控量通常有以下4种,即液位、压力、流量和温度。