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Welcome to the official blog of the International Society of Automation (ISA).

This blog covers numerous topics on industrial automation such as operations & management, continuous & batch processing, connectivity, manufacturing & machine control, and Industry 4.0.

The material and information contained on this website is for general information purposes only. ISA blog posts may be authored by ISA staff and guest authors from the automation community. Views and opinions expressed by a guest author are solely their own, and do not necessarily represent those of ISA. Posts made by guest authors have been subject to peer review.

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Is a VFD or Valve Faster?

This guest post is authored by Greg McMillan.

In the ISA Automation Week Mentor Program, I am providing guidance for extremely talented individuals from Argentina, Brazil, Malaysia, Mexico, Saudi Arabia, and the USA. We will be sharing a question and the answers each week. If you would like to provide additional answers, please send them to Susan Colwell at ISA. The nineteenth question is from Muhammad Khalifah in Saudi Arabia:

"How fast is a VFD if compared to a control valve and does this vary from application to application?"

Greg Shinskey in his study “Flow and Pressure Control Using Variable Speed Drives” (Control Conference, Chicago, 1980, pages 161-167), found that the VFD deadtime was essentially zero and the response time was much faster than for a control valve.

If the drive and motor have a generous amount of torque compared to the inertia of the impeller and rotor, a velocity limit (rate of change of speed limit) or deadband is not unnecessarily introduced, and speed and torque control is done in the VFD, the only deadtime in a flow or pressure response is due to PID scan and execution time and measurement lag and update time. For liquid or polymer pressure control or incinerator pressure control, the use of a VFD and a fast sensor can be essential for tight control creating a scenario where analog control is needed to eliminate digital delays as discussed in “Analog Control Holdouts.”

However, many times velocity limiting and deadband are introduced in the drive setup making the VFD slower than a control valve because the VFD supplier doesn’t understand the effect of dynamics on control loop performance. Also, to realize the benefit of a faster final control , the user must increase the gain and reduce the reset time per Equation 1 in the resource file Effect of PID Execution Time and Equation 2 in the InTech online article “PID tuning rules.” Often users are not accustomed to the much faster tuning settings and operations is concerned  that things are happening much faster. If the loop output limits are not judiciously set, the loop can get into a lot of trouble very quickly. If the PID has a dynamic reset limit option (external reset feedback), directional setpoint velocity limits can be added in the analog output block to provide an easily adjustable slower approach to undesirable speeds without retuning.

The excerpt Essential Book Excerpt VFD Performance from the ISA book Essentials of Modern Measurements and Final Elements in the Process Industries provides on pages 377-379 a more detailed answer to the question “Which Is Faster: A Valve or a VSD?”

 

Greg McMillan
Greg McMillan
Greg McMillan has more than 50 years of experience in industrial process automation, with an emphasis on the synergy of dynamic modeling and process control. He retired as a Senior Fellow from Solutia and a senior principal software engineer from Emerson Process Systems and Solutions. He was also an adjunct professor in the Washington University Saint Louis Chemical Engineering department from 2001 to 2004. Greg is the author of numerous ISA books and columns on process control, and he has been the monthly Control Talk columnist for Control magazine since 2002. He is the leader of the monthly ISA “Ask the Automation Pros” Q&A posts that began as a series of Mentor Program Q&A posts in 2014. He started and guided the ISA Standards and Practices committee on ISA-TR5.9-2023, PID Algorithms and Performance Technical Report, and he wrote “Annex A - Valve Response and Control Loop Performance, Sources, Consequences, Fixes, and Specifications” in ISA-TR75.25.02-2000 (R2023), Control Valve Response Measurement from Step Inputs. Greg’s achievements include the ISA Kermit Fischer Environmental Award for pH control in 1991, appointment to ISA Fellow in 1991, the Control magazine Engineer of the Year Award for the Process Industry in 1994, induction into the Control magazine Process Automation Hall of Fame in 2001, selection as one of InTech magazine’s 50 Most Influential Innovators in 2003, several ISA Raymond D. Molloy awards for bestselling books of the year, the ISA Life Achievement Award in 2010, the ISA Mentoring Excellence award in 2020, and the ISA Standards Achievement Award in 2023. He has a BS in engineering physics from Kansas University and an MS in control theory from Missouri University of Science and Technology, both with emphasis on industrial processes.

Books:

Advances in Reactor Measurement and Control
Good Tuning: A Pocket Guide, Fourth Edition
New Directions in Bioprocess Modeling and Control: Maximizing Process Analytical Technology Benefits, Second Edition
Essentials of Modern Measurements and Final Elements in the Process Industry: A Guide to Design, Configuration, Installation, and Maintenance
101 Tips for a Successful Automation Career
Advanced pH Measurement and Control: Digital Twin Synergy and Advances in Technology, Fourth Edition
The Funnier Side of Retirement for Engineers and People of the Technical Persuasion
The Life and Times of an Automation Professional - An Illustrated Guide
Advanced Temperature Measurement and Control, Second Edition
Models Unleashed: Virtual Plant and Model Predictive Control Applications

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