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102  Cha11ter  Fonr


             4-4·1  Proportional-Only Control of a Pure Dead-nme
                    Process
             Based on Chap. 3, we can guess that there will be an offset between the
             set point and the process output. The open-loop transfer function is




             where k  is the proportional control gain that we wish to estimate.
             When s is replaced by jro, the open-loop transfer function becomes

                             GpGc(jro) = e-it»Dk = 1Giei 6
                                  IGI=k                         (4-14)
                                   6=-roD

                The Bode plot for k = 1 and D = 8 is the same as that in Fig. 4-24.
             Find  the  point  where  the  phase  lag  reaches  180°.  The  amplitude
             remains unity at all frequencies so a control gain of unity will cause
             problems. When the control gain k is decreased to 0.7 the whole ampli-
             tude line  is shifted down to a  value of 0.7  and the phase margin
             requirement is satisfied. Using this control gain, a simulation in the
             time domain shows the response to a step in the set point (Fig. 4-26).


                 1.5
                   1                             ... ""· ............. .
                                                    .
                                                              .
                                                         .
              :::s  0.5
                                           •
                                                              0
                                                •
                                                         0
                                                    0
                   0                  ·.· .. · ..... :  .... · ... ·.· ... ·.·  ..
                --0.5
                    0
                 1.5
                   1
              V)
              1   0.5
              >-
                   0
                --0.5 0
                        10   20   30   40   50   60   70   80   90   100
                                         Time
             F1auRE 4-28  Proportionak>nly control of pure dead-time process, k = 0. 7.
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