Abstract
The industrial PID has many options, tools, and parameters for dealing with the wide spectrum of difficulties and opportunities in manufacturing plants. Some of the options such as “dynamic reset limit” have existed for decades but the full value and applicability has not been realized. Also, the possibilities extend considerably beyond the original intent into improving process efficiency, operability, and compliance for sustainable manufacturing. A sustainable plant is defined as plant that is safe, clean, efficient, profitable, and compliant (Studebaker in Sustainable plant. PutmanMedia http://www.sustainableplant.com/ 2011). An enhanced PID developed for wireless measurements has been found to play an important role in providing a sustainable plant by inherently eliminating oscillations from a wide variety of sources including discontinuous and delayed responses in the automation system and interactions between loops when used with a threshold sensitivity setting and the dynamic reset limit. The advancements in new techniques and a greater understanding of existing capabilities enable the PID to not only improve loop performance but to individually optimize unit operations.
This is a preview of subscription content, log in via an institution.
Buying options
Tax calculation will be finalised at checkout
Purchases are for personal use only
Learn about institutional subscriptionsReferences
Astrom, K., Hagglund, T.: Advanced PID Control. ISA, Research Triangle Park (2006)
Blevins, T., McMillan, G., Wojsznis, W., Brown, M.: Advanced Control Unleashed. ISA, Research Triangle Park (2003)
Bohl, A., McAvoy, T.: Linear feedback vs. time optimal control. II. The regulator problem. Ind. Eng. Chem. Process Des. Dev. 15(1) (1976)
Boudreau, M., McMillan, G.: New Directions in Bioprocess Modeling and Control. ISA, Research Triangle Park (2008)
Harriott, P.: Process Control. McGraw Hill, New York (1964)
McMillan, G.: Tuning and Control Loop Performance. ISA, Research Triangle Park (1994)
McMillan, G.: Advanced pH Measurement and Control. ISA, Research Triangle Park (2003)
McMillan, G.: Models Unleashed. ISA, Research Triangle Park (2004)
McMillan, G.: What is your flow control valve telling you. Control Design, May 2004
McMillan, G., Sowell, M., Wojsznis, P.: The next generation—adaptive control takes a leap forward. Chemical Processing, Sept. 2004
McMillan, G.: Good Tuning: A Pocket Guide. ISA, Research Triangle Park (2005)
McMillan, G.: Life’s a batch. Control, May 2005
McMillan, G.: Full throttle batch and startup response. Control, May 2006
McMillan, G.: Improve control loop performance. Chemical Processing, October 2007
McMillan, G.: Effect of sample delay on standard PID tuning and loop performance. Advanced Application Note 5, Emerson, Austin (2008). http://www.modelingandcontrol.com/repository/AdvancedApplicationNote005.pdf
McMillan, G.: Unlocking the secret profiles of batch reactors. Control, July 2008
McMillan, G.: Is wireless control ready for prime time? Control, July 2009
McMillan, G.: Essentials of Modern Measurements and Final Elements in the Process Industry, 2nd edn. ISA, Research Triangle Park (2010)
McMillan, G.: Centrifugal and Axial Compressor Control. Momentum Press, New York (2010)
McMillan, G.: Wireless—Overcoming challenges of PID control & analyzer applications. InTech, July–August 2010
McMillan, G.: DeltaV v11 PID enhancements for wireless. Emerson white paper, Austin, August 2010
McMillan, G.: How to get the most out of your PID. In: ISA Automation Week, Houston, October 2010
McMillan, G.: Deminar #10 Deadtime compensator myth buster. Emerson website entry and screencast recording, Austin, October 2010. http://www.modelingandcontrol.com/2010/10/review_of_deminar_10_-_deadtim.html
McMillan, G.: Exceptional opportunities in process control. ISA short course, Saint Louis, 8 December 2010. http://www.modelingandcontrol.com/2010/12/exceptional_opportunities_in_p_18.html
McMillan, G.: Measurement and valve errors—Sources and impact. Emerson website entry, Austin, 9 December 2010. http://www.modelingandcontrol.com/2010/12/measurement_and_valve_errors_-.html
McMillan, G.: Star performers in minimizing life cycle costs. Emerson website entry, Austin, 16 December 2010. http://www.modelingandcontrol.com/2010/12/star_performers_in_minimizing.html
McMillan, G.: Advanced Temperature Measurement and Control. ISA, Research Triangle Park (2011)
McMillan, G., Baril, R.: pH measurement and control. Chemical Engineering, August 2010
McMillan, G., Dasani, S., Jagadeesan, P.: Adaptive level control. Control, February 2010
Shinksey, F.: The effect of scan period on digital control loops. InTech, June 1993
Shinskey, F.: Feedback Control for Industrial Processes. McGraw Hill, New York (1994)
Shinskey, F.: Process Control Systems. McGraw Hill, New York (1996)
Shinskey, F.: The power of external reset-feedback. Control, May 2006
Shinskey, F.: Maximizing control-loop performance. Control, May 2010
Studebaker, P.: Sustainable plant. PutmanMedia (2011). http://www.sustainableplant.com/
Wojsznis, W., Blevins, T., Wojsznis, P.: Adaptive feedback/feedforward PID controller. In: ISA Conference, Houston (2003)
Author information
Authors and Affiliations
Corresponding author
Editor information
Editors and Affiliations
Rights and permissions
Copyright information
© 2012 Springer-Verlag London Limited
About this chapter
Cite this chapter
McMillan, G.K. (2012). Industrial Applications of PID Control. In: Vilanova, R., Visioli, A. (eds) PID Control in the Third Millennium. Advances in Industrial Control. Springer, London. https://doi.org/10.1007/978-1-4471-2425-2_14
Download citation
DOI: https://doi.org/10.1007/978-1-4471-2425-2_14
Publisher Name: Springer, London
Print ISBN: 978-1-4471-2424-5
Online ISBN: 978-1-4471-2425-2
eBook Packages: EngineeringEngineering (R0)