Page 62 - Practical Control Engineering a Guide for Engineers, Managers, and Practitioners
P. 62

CHAPTER 3






                                    Basic Concepts in


                                      Process Analysis





                  ince the basic tenet of this book is to analyze the process before
                  one attempts to control it, we will have to develop some process
             S analysis  concepts.  Furthermore,  since  controlling  a  process
             inherently deals with transient behavior we will have to deal with
             process dynamics. Finally, since we need to keep the level of the mate-
             rial in this book reasonable, that is, attractive to a busy manager, we
             will start with the simplest of constructs-the first-order process. In
             fact,  we will beat it to  death. During the beating, the widely used
             proportional-integral (PI) control algorithm will be introduced. One
             of the sophisticated tools of control engineering, the Laplace trans-
             form, will also be introduced. For technical support, the reader may
             want  to  consult App. A  (introductory calculus),  App.  B (complex
             numbers),  App.  E  (first- and  second-order differential  equations),
             and App. F (Laplace transforms).


        3-1  The First-Order Process-an Introduction
             Let's go back to the tank of water introduced in Chap. 1 (Fig. 3-1). It
             will be our prototypical first-order process. The dynamic analysis of
             this tank often consists of studying the step response, which is shown
             in Fig. 3-2. Here the process input U, the valve, is given a step at time
             t = 9, from an initial value of zero to unity. The process output Y, the
             tank level, begins to rise and appears to line out at a value of 2.0. For
             convenience, we have chosen the initial value of the valve and the
             tank level to be zero. In general, these quantities could have almost
             any initial value but this graph would still apply if  the reader is will-
             ing to allow us to subtract these nonzero initial values, that is, nor-
             malizing the initial values of these quantities to zero.
                To proceed we need some nomenclature. First, let the change in
             the process input be signified as ~U.  The symbol~  usually signifies a
             change in the quantity following it (or upon which it operates). Sec-
             ond, let the resulting change in the tank level be signified as ~  Y.
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