Greg: I had the pleasure of interviewing Jacques Smuts on improving control loops,. a subject near and dear to my heart. Jacques is the president of OptiControls Inc and the author of the book Process Control for Practitioners that provides a very understandable and practical approach to control loop optimization.
Stan: What do you do for plants?
Jacques: I do process control consulting and training to improve the performance of control loops. You would think after 20 years it would become old hat, but I am constantly surprised at how key fundamentals are not understood by people responsible for tuning.
Greg: In the midst of teaching a course on opportunities in process control at a plant I used to work at outside New Orleans, I realized the veterans were hanging on each word, but the young engineers were pretty much blowing me off. I found out most of their job was paper work in a Six Sigma program, and none had spent any time trying to tune or improve loops. As I lead the ISA Mentor Program, I am astonished how little time my protégés have to work on control loops.
Jacques: I am lucky that I can focus on tuning loops. This has unfortunately been reduced to a small fraction of what practitioners at plants are responsible for today. Tuning is a skill that requires practice. Many don't appreciate how much you really have to know beyond the basic tuning relationships. You need to know if the valve works properly. You need understand if a process needs to be tuned fast or slow and whether you need to schedule tuning. I enjoy the depth of the field. We lose sight of what the user needs to know and what the user does know. Increasingly, the user has more responsibility and less time for tuning and learning.
Greg: I was impressed with your chapter on valve problems where you describe tests for the various sources of limit cycling. Most other books don't make a distinction between dead band and stiction or the importance of valve problems in general. In university textbooks, the valve is perfect, and the whole emphasis is on a process time constant and gain and a setpoint response, reducing the loop to a servo problem. This may work for aerospace, but not for industrial processes with sloppy valves, slow measurements, analyzer sample and cycle times, large and variable dead time, interactions, unmeasured disturbances and non-self-regulating responses.
Stan: What has been the impact of digital positioners?
Jacques: Nowadays I find a lot less dead band, but also some erratic behavior from weird positioner tuning. I am amazed at how many tuning settings are on a modern positioner. Each manufacturer has a proprietary algorithm and tuning parameters. Tuning guidelines are slim to none. It helps to know the positioner is a closed loop controller that could have overshoot and limit cycles. Also, be aware that the response time depends on step size. I have seen a response time increase from 2 sec for a 2% change to 30 sec for 0.5% change. I look at past history to see the size of increments in the PID output to determine what the controller will have to deal with. I have also seen a positioner develop a limit cycle with a flow loop in manual.