Page 9 - Practical Control Engineering a Guide for Engineers, Managers, and Practitioners
P. 9

Contents     ix


                    4-5  A First-Order with Dead-Tune (FOWDT)
                         Process  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .  107
                         4-5-1  The Concept of Minimum Phase     109
                         4-5-2  Proportional-Dnly Control   . . . . . . . .  109
                         4-5-3  Proportional-Integral Control of the
                               FOWDT Process  . . . . . . . . . . . . . . . . .  111
                    4-6  A Few Comments about Simulating
                         Processes with Variable Dead Tunes  . . . . . . .  114
                    4-7  Partial Summary and a Slight Modification
                         of the Rule of Thumb   . . . . . . . . . . . . . . . . . . .  116
                    4-8  Summary    . . . . . . . . . . . . . . . . . . . . . . . . . . . . .  118

               5  Matrices and Higher-Order Process Models       121
                    5-1  Third-Order Process without
                         Backflow  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .  121
                    5-2  Third-Order Process with
                         Backflow  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .  129
                    5-3  Control of Three-Tank System with No
                         Backflow  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .  133
                    5-4  Critical Values and Finding the Poles   139
                    5-5  Multitank Processes   . . . . . . . . . . . . . . . . . . . .  140
                    5-6  Summary    . . . . . . . . . . . . . . . . . . . . . . . . . . . . .  143

               6  An Underdamped Process  . . . . . . . . . . . . . . . . . . . • .  145
                    6-1  The Dynamics of the Mass/Spring/
                         Dashpot Process  . . . . . . . . . . . . . . . . . . . . . . . .  145
                    6-2  Solutions in Four Domains   . . . . . . . . . . . . . .  149
                         6-2-1  Tune Domain  . . . . . . . . . . . . . . . . . . . .  149
                         6-2-2  Laplace Domain Solution   . . . . . . . . .  149
                         6-2-3  Frequency Domain  . . . . . . . . . . . . . . .  150
                         6-2-4  State-Space Representation  . . . . . . . .  151
                         6-2-5  Scaling and Round-Off Error      152
                    6-3  PI Control of the Mass/Spring/Dashpot
                         Process  . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .  153
                    6-4  Derivative Control (PID)   . . . . . . . . . . . . . . . .  156
                         6-4-1  Complete Cancellation  . . . . . . . . . . . .  161
                         6-4-2  Adding Sensor Noise  . . . . . . . . . . . . .  161
                         6-4-3  Filtering the Derivative  . . . . . . . . . . .  163
                    6-5  Compensation before Control-The Transfer
                         Function Approach  . . . . . . . . . . . . . . . . . . . . .  165
                    6-6  Compensation before Control-The State-Space
                         Approach   . . . . . . . . . . . . . . . . . . . . . . . . . . . . .  171
                    6-7  An Electrical Analog to the Mass/Dashpot/
                         Spring Process   . . . . . . . . . . . . . . . . . . . . . . . . .  174
                    6-8  Summary    . . . . . . . . . . . . . . . . . . . . . . . . . . . . .  176
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