Modern Control Engineering

(Chris Devlin) #1
118 Chapter 4 / Mathematical Modeling of Fluid Systems and Thermal Systems

whereX(s)=l[x]and If qi, the change in flow through the pneumatic


actuating valve, is proportional to x, the change in the valve-stem displacement, then


whereQi(s)=lCqiDandKqis a constant. The transfer function between qiand


becomes


whereKvis a constant.


The standard control pressure for this kind of a pneumatic actuating valve is between


3 and 15 psig. The valve-stem displacement is limited by the allowable stroke of the


diaphragm and is only a few inches. If a longer stroke is needed, a piston–spring


combination may be employed.


In pneumatic actuating valves, the static-friction force must be limited to a low value


so that excessive hysteresis does not result. Because of the compressibility of air, the


control action may not be positive; that is, an error may exist in the valve-stem position.


The use of a valve positioner results in improvements in the performance of a pneu-


matic actuating valve.


Basic Principle for Obtaining Derivative Control Action. We shall now present


methods for obtaining derivative control action. We shall again place the emphasis on


the principle and not on the details of the actual mechanisms.


The basic principle for generating a desired control action is to insert the inverse of


the desired transfer function in the feedback path. For the system shown in Figure 4–12,


the closed-loop transfer function is


If@G(s)H(s)@1, then C(s)/R(s)can be modified to


Thus, if proportional-plus-derivative control action is desired, we insert an element


having the transfer function 1/(Ts+1)in the feedback path.


C(s)


R(s)


=


1


H(s)


C(s)


R(s)


=


G(s)


1 +G(s)H(s)


Qi(s)


Pc(s)


=Kc Kq=Kv


pc


Qi(s)


X(s)


=Kq


Pc(s)=lCpcD.


R(s) C(s)
G(s)

H(s)

+–

Figure 4–12
Control system.

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