Page 72 - Practical Control Engineering a Guide for Engineers, Managers, and Practitioners
P. 72

Basic  Concepts  in  Process  Analysis   47


                 1.4 r-----r---~---~-----r----r----....,
                 1.2               .       .       .       .
                  1              .................................
                                   0
                                           I
                                                   I
                                                           0
                                 .....................................
                                                   0
                                           0
                                                           •
                                   0
              ::::3  0.8
                                   0       I       I       0
                 0.6   •         •   0   •••  ••••••• •••   ••••••• :  0   ••••••• ·: •••••••
                                   •
                                           0
                                                           •
                 0.4  .    .     ............ ·: ........ : ........ ~ ....... .
                                           .
                                                   .
                                                           .
                 0.2                 . . . . . . . . . . . . . . . . . . . . . . . .  . . . . .
                  0~----~------~----~------~------~----~
                   0       5      10      15      20      25      30
                  1  .. ---- -:·- ---- -:----- -·.-----·- :-·---- -·-:-----·-
                           •       I       I       I       0
              V)  0.8              . .  . ..... : . ....... : ............. .
                                           .       .       .
              ]  0.6               . •.  :::::::~::::::::~:~::~:::::
              >- 0.4  •.
                 0.2
                  00
                           5      10      15      20      25      30
                                         Tl.Dle
             F1auRE 3-4  Proportional-only control.
             high values of k might cause large (and perhaps unacceptable)
             excursions in the controller output. Figure 3-4 shows the offset
             that results with proportional-only control.
                In case you want to do some simulation yourself, these results
             were derived from a process that had f  = 10, g = 2.5, and the pro-
             portional control gain was k = 1.1. The Matlab code that generates
             the results is given in the scripts mentioned in the preface.
               Question  3·2  Can you see that no matter how large  you make the value of
               the  proportional control gain k,  this idealized controlled system cannot go
               unstable?

               Answer  Let k increase without bound in Eq. (3-19). The result will be





               The controller output is proportional to the error and as the error decreases
               because of the controller action, so does the output. This, in turn, decreases the
               controller output. This ''backing off" of the control output leads to the offset.
               To obtain a zero error in the face of a step in the set point, we need a controller
               action that will "keep on going" until the error is removed, even after it stops
               changing. By the way, we could also have obtained the final value of Y by letting
               the derivative in Eq. (3-18) go to zero.
   67   68   69   70   71   72   73   74   75   76   77