Consider the PCM furnace module of Appendix E. Assume that hydrocarbon temperature T HC is the CV,
Question:
(a) Design a PID controller based on the IMC tuning relations and a reasonable choice for Ïc.
(b) Design a PID controller based on the relay auto-tuning feature of the PCM, and the Z-N settings.
(c) Simulate each controller for a sudden change in an unmeasured disturbance, the hydrocarbon flow rate FHC, at t = 10 min, from 0.035 to 0.040 m 3 /min. Which controller is superior?
(d) Attempt to obtain improved control system performance by fine tuning your better controller for part (c). For the performance criteria, consider maximum deviation from set point and settling time.
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Process Dynamics And Control
ISBN: 1602
4th Edition
Authors: Dale E. Seborg, Thomas F. Edgar, Duncan A. Mellichamp, Francis J. Doyle
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