Page 100 - Practical Control Engineering a Guide for Engineers, Managers, and Practitioners
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CHAPTER4



                                          A  New Domain


                                   and More Process


                                                       Models






                   hapter 3 introduced the reader to a  relatively sophisticated
                   tool,  the Laplace transform.  It was shown to be handy for
             Csolving the differential equations that describe model pro-
             cesses.  It appeared  to have  some other  features  that could  yield
             insight into a model's behavior without actually doing an inversion.
                In this chapter the Laplace transform will be used as a stepping
             stone to lead us to the frequency domain where we will learn more
             tools for gaining insight into dynamic behavior of processes and con-
             trolled systems.
                Chapter 3 also got us started with a simple process model, the
             first-order model that  behaved approximately as many real processes
             do. However, this model is not sufficient to cover the wide variety of
             industrial processes that the control engineer must deal with. So, to
             the first-order process model we will add a pure dead-time model
             which will subsequently be combined with the former to produce the
             first-order with dead-time or FOWDT model. For technical support
             the reader may want to read App. B (complex numbers), App. D (infi-
             nite series), App. E (first- and second-order differential equations),
             and App. F (Laplace transforms).
                As in previous chapters, each new process will be put under con-
             trol. In this chapter the new tool of  frequency domain analysis will  be
             used to augment time domain studies.

        4-1  Onward to the Frequency Domain


             4·1·1  Sinusoidally Disturbing the First-Order Process
             Instead of disturbing our tank of liquid with a  step change in the
             input flow rate, consider an input flow rate that varies as a sinusoid
             about some nominal value as shown in Fig. 4-1. The figure suggests

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