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CONTROLLER TUNING AND CONTROL LOOP PERFORMANCE, A PRIMERSubtitled: PID WITHOUT THE MATHBy David W. St. Clair (Retired DuPont Engineer)$25 Includes Free Shipping 33,850 Copies Sold Through August 2024 100 Pages, 8 1/2" x 11", with 43 Figures |
This PID tuning or controller tuning booklet describes the basics needed to understand PID control. Companion controller tuning software is available, which illustrates the basic points made in the booklet, and a demonstration version is available for downloading.
May you enjoy learning about PID control!
Table of Contents |
CHAPTER 1, GETTING STARTED: Science or Art, History, The Language of Control, Terminology for and Description of Controller Settings, Proportional Action, Integral Action, Reset Windup, Derivative Action, Filter Time, Filter Time and Derivative Action.
CHAPTER 2, TUNING RULES AND PROCEDURES: Preparation, Closed-loop Tuning: What to Do, Closed-loop Tuning: How to Do It, Open-loop Tuning: What to Do, Open-loop Tuning: How to Do It, Comparison of Testing Methods, When to Not Tune by the Rules, Tuning Rules Overview.
CHAPTER 3, TUNING OBJECTIVES AND EXPECTED LOOP PERFORMANCE: Response to Cyclic Upsets, Factors Affecting the Natural Period.
CHAPTER 4, LAGS AND GAINS, BUT MOSTLY LAGS: Dead Time, Integrator, First Order Lag, Combining Building Blocks, Gains.
CHAPTER 5, EXAMPLES OF ACTUAL LAGS: Dead Time, Controllers, Pneumatic Transmission Lags, Valves, Transmitters, Temperature Measurement, Tanks (Liquid Flow Lag), Tanks (Compositional Lag), Thermal Process Lags, Typical Natural Periods.
CHAPTER 6, CASCADE CONTROL
CHAPTER 7, DERIVATIVE ACTION
CHAPTER 8, INTERACTIONS AND NONLINEARITIES: Interactions, Nonlinearities, Process, Hardware (Continuous Nonlinearities), Hardware (Discontinuous Nonlinearities), Velocity Limiting, Dead Band, Valves at Limits, Integral (Reset) Windup.
CHAPTER 9, POTPOURRI: Digital Control Algorithms, Sampling Frequency and Loop Performance, Load Changes /Upsets / Disturbances, Dampening Noisy Measurements.
IMPROVING CONTROL UNIFORMITY
SUMMARY
GLOSSARY
APPENDIX: Pure Dead Time Process, Process with Dead Time and Integration, Derivative Frequency Response.
Background |
The booklet was originally issued in 1983
as an internal report in the DuPont Company, to help engineers and technicians,
who have no special training in feedback control, understand the basic
considerations and limitations. It handily broke all records at the DuPont
Company for number of requested copies (over 1200) when issued. That report
was released to the public and published in 1990. It subsequently sold almost
17,000 copies. In 1992 it was expanded for DuPont to about twice the size.
This report also broke distribution records in the Company, with over 2500
copies requested when issued. The part unique to DuPont was deleted and more
was added to make the Second Edition, which was published in Dec., 1993.
SECOND EDITION
The second edition of "Controller Tuning and Control Loop Performance" has
been extended in both directions from the first. Sections have been added
for the very beginner and for the somewhat more experienced. It is about
twice the size. Sections have been added on the what-to-do and how-to-do-it
of tuning, to help the person who may have never done it before. Then
interspersed throughout are paragraphs that extend some of the non-math concepts
to the realm of math, or at least algebra. These sections explaining concepts
in math (sometimes frequency response terms) are clearly identified to make
them easy to skip. This Second Edition still stands on its own, of explaining
the essence of feedback control, without referring to math. I hope these
new references will help any reader who wants to bridge the gap from the
nonmath to the math. I have tried to make this second edition appeal to readers
whose background may not be the chemical processing industries. I know I
can only partly succeed in this broadened scope, for all of my 40 years in
the automatic control business were in that industry. I hope this booklet
meets what I perceive as a need for more information on the beginning end
of training on the subject of controller tuning and control loop
performance.
Summary |
This booklet on controller tuning and control
loop performance stops where most books and courses on the subject begin.
Too often this subject is introduced with math unfamiliar to the reader.
That does not have to be - there are simple concepts to help those unschooled
in the math to know and understand the basics of control system tuning, to
appreciate the limitations and to know what can be expected.
TUNING CONTROLLERS IS MOSTLY SCIENCE. It consists of fitting the time
and amount parameters of the controller to the time and amount parameters
of the process. An open-loop test of the process yields the needed parameters,
and simple tuning rules based on these parameters have proven to apply well
to a large portion of industrial control loops. Tuning parameters can also
be determined from a closed-loop test, though the test is not as thorough.
For a large family of loops it is possible to predict what is likely to happen
to performance when the process changes or when the tuning adjustments are
set differently.
ALL CONTROL LOOPS WILL CYCLE IF THE CONTROLLER GAIN IS HIGH ENOUGH.
The period of this cycle is called the natural period, and it largely determines
the potential performance of the loop. The shorter the period the better.
The natural period in turn is closely linked to the apparent (or real) dead
time in the loop. It is paradoxical that the natural period is not determined
by the largest lags in the loop, but rather by the dead time and the smaller
lags. The potential performance of a loop is limited by certain lags in the
loop, and trying to eke out better performance through tuning is often an
exercise in futility.
TUNING RULES ARE DESIGNED TO GIVE REASONABLY TIGHT CONTROL. This may
not always be the objective. Many, and perhaps most, loops do not need to
be tuned tightly. However all loops need to be tuned as part of the process
of putting the controller into operation. Most loops respond to changes in
tuning parameters much like the response curves given in chapter 2. Consideration
should be given, when contemplating retuning a loop, to what the justification
for the effort is, and whether the desired improvement can reasonably be
expected from tuning.
THERE ARE A FEW TYPICAL GREMLINS WHICH CAUSE LOOPS TO NOT BEHAVE IN THE
TYPICAL FASHION. It is important to recognize these, for failure to do
so can result in detuning a loop, not to mention a loss of faith in the
scientific approach. You will not have to tune many loops before you run
into one of these gremlins.
BE PATIENT IN LEARNING THE METHODS WHICH ARE NEW TO YOU. They do work,
and the method of understanding loop performance will allow you to converse
with others on a common ground, sharing your experiences. Otherwise tuning
is just one isolated hit-or-miss experience after another.
About the Author |
The author retired after 40 years of practice in the field of instrumentation and control in the process industries (8 years with Eastman Kodak and 32 years with DuPont). He took, in 1947, what he understood to be the first college course offered in the theory of feedback control, a chance event at MIT that started his career in the field. He arguably has applied the scientific method to solving control problems in the process industries longer than anyone, or at least that was probably true when he retired in 1987. He had been explaining the concepts to the non-specialist for most of that time. He relishes this opportunity to spread the word to a larger audience.
Links Which May Be of Interest |
- PID tuning, process control consulting and training is available from Paul S. Fruehauf. His website is Frue-engg-svcs.com.. You may e-mail him at fruehaufps@frue-engg-svcs.com, phone (302) 690 1929.
- A Spanish translation of the first edition is available through Tiempo Real S. A. in Barcelona, phone (93) 410 17 49. fax (93) 419 06 32, amable@tiemporeal.es. They also carry the Second Edition (in English) as well as the companion software.
- There is an interactive simulation of a temperature control system available on the web. It is part of a document called Feedback & Control by Charles Williams at the University of Exeter in the UK.
- John Gerry has a site which describes his ExperTune software. PID Tuning Software makes it easy to analyze and tune PID loops in any industrial controller.
- Potential customers for the booklet in Australasia may get them from the Institute of Instrumentation, Control & Automation Aust Inc (IICA). You may e-mail Cathie Tynan at the IICA in Patterson Lakes, Victoria, phone (03) 9772 0944, fax (03) 9772 0133 for quicker delivery and typically a lower price, because of lower mailing costs.