Design of PI controller with input constraint: application on blending process

Because of their simplicity, reliability and effectiveness, proportional–integral–derivative (PID) controllers remain the most widely used controllers in the process industries. Actuator saturation is among the most common and significant problem in control systems design. Normal PID controller does...

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Main Authors: Chua, Bee Lin, Taip, Farah Saleena, Ab. Aziz, Norashikin, Choong, Thomas Shean Yaw
Format: Article
Language:English
Published: Wiley Periodicals 2010
Online Access:http://psasir.upm.edu.my/id/eprint/13917/1/Design%20of%20PI%20controller%20with%20input%20constraint%20application%20on%20blending%20process.pdf
http://psasir.upm.edu.my/id/eprint/13917/
https://onlinelibrary.wiley.com/doi/abs/10.1111/j.1745-4530.2009.00418.x
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Institution: Universiti Putra Malaysia
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spelling my.upm.eprints.139172018-08-14T08:53:18Z http://psasir.upm.edu.my/id/eprint/13917/ Design of PI controller with input constraint: application on blending process Chua, Bee Lin Taip, Farah Saleena Ab. Aziz, Norashikin Choong, Thomas Shean Yaw Because of their simplicity, reliability and effectiveness, proportional–integral–derivative (PID) controllers remain the most widely used controllers in the process industries. Actuator saturation is among the most common and significant problem in control systems design. Normal PID controller does not take this into consideration. Normally, an anti‐windup compensator is employed in the system to overcome the problem. In this contribution, a new set of controller tuning relations is developed to tune the PI controller when the system is under saturation. The blending process was described as first order plus time delay (FOPTD) process and an expression is developed for saturation level, U as a function of controller gain, Kc with the range of R 0.4–2 (ratio of time delay to time constant). The proposed tuning rule relate the parameters of the controller to the parameters of a FOPTD model of the plant to a step change in the set point. The proposed method was applied to PI controller and tested on the process of blending system of sweetened condensed milk. The performance of the controller with various tuning formulae incorporated with classical anti‐windup strategies has been compared. The simulation results showed that the proposed method could give satisfactory performance in controlling the process. Wiley Periodicals 2010 Article PeerReviewed text en http://psasir.upm.edu.my/id/eprint/13917/1/Design%20of%20PI%20controller%20with%20input%20constraint%20application%20on%20blending%20process.pdf Chua, Bee Lin and Taip, Farah Saleena and Ab. Aziz, Norashikin and Choong, Thomas Shean Yaw (2010) Design of PI controller with input constraint: application on blending process. Journal of Food Process Engineering, 33 (S1). pp. 284-297. ISSN 0145-8876; ESSN: 1745-4530 https://onlinelibrary.wiley.com/doi/abs/10.1111/j.1745-4530.2009.00418.x 10.1111/j.1745-4530.2009.00418.x
institution Universiti Putra Malaysia
building UPM Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Putra Malaysia
content_source UPM Institutional Repository
url_provider http://psasir.upm.edu.my/
language English
description Because of their simplicity, reliability and effectiveness, proportional–integral–derivative (PID) controllers remain the most widely used controllers in the process industries. Actuator saturation is among the most common and significant problem in control systems design. Normal PID controller does not take this into consideration. Normally, an anti‐windup compensator is employed in the system to overcome the problem. In this contribution, a new set of controller tuning relations is developed to tune the PI controller when the system is under saturation. The blending process was described as first order plus time delay (FOPTD) process and an expression is developed for saturation level, U as a function of controller gain, Kc with the range of R 0.4–2 (ratio of time delay to time constant). The proposed tuning rule relate the parameters of the controller to the parameters of a FOPTD model of the plant to a step change in the set point. The proposed method was applied to PI controller and tested on the process of blending system of sweetened condensed milk. The performance of the controller with various tuning formulae incorporated with classical anti‐windup strategies has been compared. The simulation results showed that the proposed method could give satisfactory performance in controlling the process.
format Article
author Chua, Bee Lin
Taip, Farah Saleena
Ab. Aziz, Norashikin
Choong, Thomas Shean Yaw
spellingShingle Chua, Bee Lin
Taip, Farah Saleena
Ab. Aziz, Norashikin
Choong, Thomas Shean Yaw
Design of PI controller with input constraint: application on blending process
author_facet Chua, Bee Lin
Taip, Farah Saleena
Ab. Aziz, Norashikin
Choong, Thomas Shean Yaw
author_sort Chua, Bee Lin
title Design of PI controller with input constraint: application on blending process
title_short Design of PI controller with input constraint: application on blending process
title_full Design of PI controller with input constraint: application on blending process
title_fullStr Design of PI controller with input constraint: application on blending process
title_full_unstemmed Design of PI controller with input constraint: application on blending process
title_sort design of pi controller with input constraint: application on blending process
publisher Wiley Periodicals
publishDate 2010
url http://psasir.upm.edu.my/id/eprint/13917/1/Design%20of%20PI%20controller%20with%20input%20constraint%20application%20on%20blending%20process.pdf
http://psasir.upm.edu.my/id/eprint/13917/
https://onlinelibrary.wiley.com/doi/abs/10.1111/j.1745-4530.2009.00418.x
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