PID中英文對照翻譯

1、中英文互譯PID ControlIntroductionThe PID controller is the most common form of feedback. It was an essential element of early governors and it became the standard tool when process control emerged in the 1940s. In process control today, more than 95% of the control loops are of PID type, most loops are a

2、ctually PI control. PID controllers are today found in all areas where control is used. The controllers come in many different forms. There are standalone systems in boxes for one or a few loops, which are manufactured by the hundred thousands yearly. PID control is an important ingredient of a dist

3、ributed control system. The controllers are also embedded in many special purpose control systems. PID control is often combined with logic, sequential functions, selectors, and simple function blocks to build the complicated automation systems used for energy production, transportation, and manufac

4、turing. Many sophisticated control strategies, such as model predictive control, are also organized hierarchically. PID control is used at the lowest level; the multivariable controller gives the set points to the controllers at the lower level. The PID controller can thus be said to be the “bread a

5、nd butter of control engineering. It is an important component in every control engineers tool box.PID controllers have survived many changes in technology, from mechanics and pneumatics to microprocessors via electronic tubes, transistors, integrated circuits. The microprocessor has had a dramatic

6、influence the PID controller. Practically all PID controllers made today are based on microprocessors. This has given opportunities to provide additional features like automatic tuning, gain scheduling, and continuous adaptation.6.2 The AlgorithmWe will start by summarizing the key features of the P

7、ID controller. The “textbook” version of the PID algorithm is described by: 6.1where y is the measured process variable, r the reference variable, u is the control signal and e is the control error（e = y）. The reference variable is often called the set point. The control signal is thus a sum of thre

8、e terms: the P-term （which is proportional to the error）, the I-term （which is proportional to the integral of the error）, and the D-term （which is proportional to the derivative of the error）. The controller parameters are proportional gain K, integral time Ti, and derivative time Td. The integral,

9、 proportional and derivative part can be interpreted as control actions based on the past, the present and the future as is illustrated in Figure 2.2. The derivative part can also be interpreted as prediction by linear extrapolation as is illustrated in Figure 2.2. The action of the different terms

10、can be illustrated by the following figures which show the response to step changes in the reference value in a typical case.Effects of Proportional, Integral and Derivative ActionProportional control is illustrated in Figure 6.1. The controller is given by D6.1E with Ti = and Td=0. The figure shows

11、 that there is always a steady state error in proportional control. The error will decrease with increasing gain, but the tendency towards oscillation will also increase.Figure 6.2 illustrates the effects of adding integral. It follows from D6.1E that the strength of integral action increases with d

12、ecreasing integral time Ti. The figure shows that the steady state error disappears when integral action is used. Compare with the discussion of the “magic of integral action” in Section 2.2. The tendency for oscillation also increases with decreasing Ti. The properties of derivative action are illu

13、strated in Figure 6.3.Figure 6.3 illustrates the effects of adding derivative action. The parameters K and Ti are chosen so that the closed loop system is oscillatory. Damping increases with increasing derivative time, but decreases again when derivative time becomes too large. Recall that derivativ

14、e action can be interpreted as providing prediction by linear extrapolation over the time Td. Using this interpretation it is easy to understand that derivative action does not help if the prediction time Td is too large. In Figure 6.3 the period of oscillation is about 6 s for the system without de

15、rivative Chapter 6. PID ControlFigure 6.1Figure 6.2 Derivative actions cease to be effective when Td is larger than a 1 s (one sixth of the period). Also notice that the period of oscillation increases when derivative time is increased.A PerspectiveThere is much more to PID than is revealed by （6.1）

16、. A faithful implementation of the equation will actually not result in a good controller. To obtain a good PID controller it is also necessary to consider。Figure 6.3· Noise filtering and high frequency roll off· Set point weighting and 2 DOF· Windup· Tuning· Computer implem

17、entationIn the case of the PID controller these issues emerged organically as the technology developed but they are actually important in the implementation of all controllers. Many of these questions are closely related to fundamental properties of feedback, some of them have been discussed earlier

18、 in the book.6.3 Filtering and Set Point WeightingDifferentiation is always sensitive to noise. This is clearly seen from the transfer function G(s) =s of a differentiator which goes to infinity for large s. The following example is also illuminating.where the noise is sinusoidal noise with frequenc

19、y w. The derivative of the signal isThe signal to noise ratio for the original signal is 1/an but the signal to noise ratio of the differentiated signal is w/an. This ratio can be arbitrarily high if w is large.In a practical controller with derivative action it is there for necessary to limit the h

20、igh frequency gain of the derivative term. This can be done by implementing the derivative term as 6.2instead of D=sTdY. The approximation given by (6.2) can be interpreted as the ideal derivative sTd filtered by a first-order system with the time constant Td/N. The approximation acts as a derivativ

21、e for low-frequency signal components. The gain, however, is limited to KN. This means that high-frequency measurement noise is amplified at most by a factor KN. Typical values of N are 8 to 20.Further limitation of the high-frequency gainThe transfer function from measurement y to controller output

22、 u of a PID controller with the approximate derivative isThis controller has constant gainat high frequencies. It follows from the discussion on robustness against process variations in Section 5.5 that it is highly desirable to roll off the controller gain at high frequencies. This can be achieved

23、by additionallow pass filtering of the control signal bywhere Tf is the filter time constant and n is the order of the filter. The choice of Tf is a compromise between filtering capacity and performance. The value of T f can be coupled to the controller time constants in the same way as for the deri

24、vative filter above. If the derivative time is used, T f= Td/N is a suitable choice. If the controller is only PI, T f =Ti/N may be suitable.The controller can also be implemented as 6.3This structure has the advantage that we can develop the design methods for an ideal PID controller and use an ite

25、rative design procedure. The controller is first designed for the process P(s). The design gives the controller parameter Td. An ideal controller for the process P(s)/(1+sTd/N)2 is then designed giving a new value of Td etc. Such a procedure will also give a clear picture of the tradeoff between per

26、formance and filtering.Set Point WeightingWhen using the control law given by （6.1） it follows that a step change in the reference signal will result in an impulse in the control signal. This is often highly undesirable there for derivative action is frequently not applied to the reference signal. T

27、his problem can be avoided by filtering the reference value before feeding it to the controller. Another possibility is to let proportional action act only on part of the reference signal. This is called set point weighting. A PID controller given by （6.1） then becomes 6.4where b and c are additiona

28、l parameter. The integral term must be based on error feedback to ensure the desired steady state. The controller given by D6.4E has a structure with two degrees of freedom because the signal path from y to u is different from that from r to u. The transfer function from r to u is 6.5 Time tFigure 6

29、.4 Response to a step in the reference for systems with different set point weights b= 0 dashed, b = 0.5 full and b=1.0 dash dotted. The process has the transfer function P（s）=1/（s+1）3 and the controller parameters are k = 3, ki = 1.5 and kd = 1.5.and the transfer function from y to u is 6.6Set poin

30、t weighting is thus a special case of controllers having two degrees of freedom.The system obtained with the controller （6.4） respond to load disturbances and measurement noise in the same way as the controller （6.1） . The response to reference values can be modified by the parameters b and c. This

31、is illustrated in Figure 6.4, which shows the response of a PID controller to set-point changes, load disturbances, and measurement errors for different values of b. The figure shows clearly the effect of changing b. The overshoot for set-point changes is smallest for b = 0, which is the case where

32、the reference is only introduced in the integral term, and increases with increasing b.The parameter c is normally zero to avoid large transients in the control signal due to sudden changes in the set-point.6.4 Different ParameterizationsThe PID algorithm given by Equation（6.1）can be represented by

33、the transfer function 6.7 6.8 6.9 An interacting controller of the form Equation D6.8E that corresponds to a non-interacting controller can be found only ifThe parameters are then given by 6.10The non-interacting controller given by Equation （6.7） is more general, and we will use that in the future.

34、 It is, however, sometimes claimed that the interacting controller is easier to tune manually.It is important to keep in mind that different controllers may have different structures when working with PID controllers. If a controller is replaced by another type of controller, the controller paramete

35、rs may have to be changed. The interacting and the non-interacting forms differ only when both I and the D parts of the controller are used. If we only use the controller as a P, PI, or PD controller, the two forms are equivalent. Yet another representation of the PID algorithm is given by 6.11The p

36、arameters are related to the parameters of standard form through The representation Equation （6.11） is equivalent to the standard form, but the parameter values are quite different. This may cause great difficulties for anyone who is not aware of the differences, particularly if parameter 1/ki is ca

37、lled integral time and kd derivative time. It is even more confusing if ki is called integration time. The form given by Equation （6.11） is often useful in analytical calculations because the parameters appear linearly. The representation also has the advantage that it is possible to obtain pure pro

38、portional, integral, or derivative action by finite values of the parameters.PID控制6.1 介紹PID控制器是反饋控制的最常見形式。因為早在40年代它就成為了過程控制的標準工具。在今天的過程控制業(yè)中, 超過95%的控制回路是PID類型, 多數實際上是PI 控制。PID控制是分布控制系統(tǒng)的一種重要組成部分。控制器被隱藏在許多其他控制系統(tǒng)下面。PID 控制與邏輯控制經常結合在一起,連續(xù)作用、選擇器, 和簡單的功能模塊一起構成復雜自動化系統(tǒng)，可以應用在發(fā)電, 運輸，以及制造業(yè)。許多經典的控制策略, 譬如模型有預測性的控制

39、。PID控制是使用在要求水平較低的場合；PID控制器應用在底層。PID控制器在每個控制工程師的應用實例里都能經常見到。近年來PID控制器在技術生產上也產生了許多變化, 從機械到微處理器控制由電子管, 晶體管,組合電路組成的控制系統(tǒng)。 微處理器對PID控制器有著強烈的影響。實際上今天制作的所有PID控制器都是建立在微處理器的基礎上的。這就有機會擴展其他的特點：像自動定調, 獲取預定, 和連續(xù)的適應。6.2 算法我們開始講解PID控制器的主要特點。 PID算法的描述: 6.1這里 y 是被測量的處理可變量, r 參考可變量, u 是控制信號，e是控制誤差 。參考變量經常可以被稱為是固定的點?？刂菩?/p>

40、號包含三個量，P-term，I-term，D-term，控制器的參數包括比例系數K，整體時間Ti，和Td。以過去，現在和未來為基礎的控制軌跡可解釋整體，比例項和輸出部份的關系。圖中舉例。在不同時間的運動可以表示輸出部分的一個典型的例子。在參數值方面作一下改變，即可預測下一時間的走向問題。PID的作用圖6.1說明的是典型的比例控制. 控制器給定Ti=，Td=0。表示在比例控制中總存在有一種穩(wěn)定狀態(tài)誤差。獲取值增加誤差將減少, 但系統(tǒng)穩(wěn)定性將受到影響。圖 6.2 說明增加積分式的作用。它跟隨圖6.1而來增加時間Ti.當積分式運行使用。穩(wěn)定狀態(tài)誤差將逐漸的消失。相比較，說明在圖6.3減少Ti，波動繼

41、續(xù)增大.圖 6.3 舉例說明增加輸出的方法的效果。 參數 K 和 Ti 被選定以便閉環(huán)系統(tǒng)是振動的。當輸出時間過長時，導出時間將被阻值再一次增加，減少也是一樣。當在時間Td作線形補償取消輸出可以得到預測的結果。用簡單的方法解釋，如果預測時間Td太大，導出將沒有影響。在圖6.3中，振蕩的周期是沒有引出的，大約是6S。圖6.1圖6.2.當Td比1S（六分之一的周期時間）大的時候，輸出的作用停止是有效的。也要注意當輸出時間增加的時候，振蕩的周期也將增加。圖6.1說明有許多比 PID更好的系統(tǒng)，但是，實際上一個好控制器，必需得有一個好的PID控制器。而獲得一個好的PID控制器，也需要認真地考慮一下。圖

42、6.3.· 噪聲過濾和高頻率關閉· 凝固點衡量和2 DOF· 終結· 調諧· 計算機執(zhí)行在使用PID 控制器的時候，有些問題就會涌現出來，但他們實際上最重要的是在所有控制中的實施。許多問題與反饋本身是緊密地聯系在一起的。其中，有些在早期的一些資料中就已經被研究過。6.3 過濾和凝固點的衡量微分對噪聲總是敏感的。像G(s) = s 的微分器。以下的例子可以有力的說明。例子6.1-DIFFERENTIATION 放大高頻率噪音，參考信號這里的噪聲是正弦信號，頻率為w 。信號的導數是針對噪音的信號比率為原始的信號是1倍，但噪音的信號比率是被區(qū)分的。如果w 是足夠大的這個比率是可能任意提高的。從一種積分作用控制器來看，是有必要限制積分范圍的，以得到高頻率。這可以由做積分