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Received November 11, 2013
Accepted August 19, 2014
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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A unified approach for proportional-integral-derivative controller design for time delay processes
Department of Chemical Engineering, King Fahd University of Petroleum and Minerals, Dhahran 31261, Saudi Arabia
mshams@kfupm.edu.sa
Korean Journal of Chemical Engineering, April 2015, 32(4), 583-596(14), 10.1007/s11814-014-0237-6
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Abstract
An analytical design method for PI/PID controller tuning is proposed for several types of processes with time delay. A single tuning formula gives enhanced disturbance rejection performance. The design method is based on the IMC approach, which has a single tuning parameter to adjust the performance and robustness of the controller. A simple tuning formula gives consistently better performance as compared to several well-known methods at the same_x000D_
degree of robustness for stable and integrating process. The performance of the unstable process has been compared with other recently published methods which also show significant improvement in the proposed method. Furthermore, the robustness of the controller is investigated by inserting a perturbation uncertainty in all parameters simultaneously, again showing comparable results with other methods. An analysis has been performed for the uncertainty margin in the different process parameters for the robust controller design. It gives the guidelines of the Ms setting for the PI controller design based on the process parameters uncertainty. For the selection of the closed-loop time constant, (τc), a guideline is provided over a broad range of θ/τ ratios on the basis of the peak of maximum uncertainty (Ms). A comparison of the IAE has been conducted for the wide range of θ/τ ratio for the first order time delay process. The proposed method shows minimum IAE in compared to SIMC, while Lee et al. shows poor disturbance rejection in the lag dominant process. In the simulation study, the controllers were tuned to have the same degree of robustness by measuring the Ms, to obtain a reasonable comparison.
Keywords
References
Desborough LD, Miller RM, Increasing customer value of industrial control performance monitoring.Honeywell’s experience, in Chemical Process Control .VI AIChE Symposium Series, Tuscon, Arizona, Jan. 2001, 2002. (2001)
Kano M, Ogawa M, J. Process Control, 20(9), 969 (2010)
Rivera D, Morari M, Skogestad S, Ind. Eng. Chem. Process Des. Dev., 25, 252 (1986)
Morari M, Zafiriou E, Robust Process Control, NJ: Prentice-Hall Englewood Cliffs, NJ (1989). (1989)
Horn IG, Arulandu JR, Gombas CJ, Vanantwerp JG, Braatz RD, Ind. Eng. Chem. Res., 35(10), 3437 (1996)
Lee Y, Park S, Lee M, Brosilow C, AIChE J., 44(1), 106 (1998)
Skogestad S, J. Process Control, 13(4), 291 (2003)
Chien IL, Fruehauf P, Chem. Eng. Prog., 86, 33 (1990)
Shamsuzzoha M, Lee M, Ind. Eng. Chem. Res., 46(7), 2077 (2007)
Seborg D, Edgar T, Mellichamp D, Process Dynamics and Control, New York, Wiley (2004). (2004)
Chen D, Seborg DE, Ind. Eng. Chem. Res., 41(19), 4807 (2002)
Lee Y, Lee J, Park S, Chem. Eng. Sci., 55(17), 3481 (2000)
Yang XP, Wang QG, Hang CC, Lin C, Ind. Eng. Chem. Res., 41(17), 4288 (2002)
Wang YG, Cai WJ, Ind. Eng. Chem. Res., 41(12), 2910 (2002)
Tan W, Marquez HJ, Chen TW, J. Process Control, 13(3), 203 (2003)
Liu T, Zhang WD, Gu DY, J. Process Control, 15(5), 559 (2005)
Jung CS, Song HK, Hyun CJ, J. Process Control, 9, 265 (1999)
Majhi S, Atherton DP, Automatica, 36(11), 1651 (2000)
Kwak HJ, Sung SW, Lee IB, Park JY, Ind. Eng. Chem. Res., 38(2), 405 (1999)
Zhang WD, Gu DY, Wang W, Xu XM, Ind. Eng. Chem. Res., 43(1), 56 (2004)
Tyreus BD, Luyben W, Ind. Eng. Chem. Res., 31, 2625 (1992)
Luyben WL, Ind. Eng. Chem. Res., 35(10), 3480 (1996)
Shamsuzzoha M, Moonyong Lee M, Korean J. Chem. Eng., 25(4), 637 (2008)
Shamsuzzoha M, Lee SH, Lee MY, Korean J. Chem. Eng., 26(3), 622 (2009)
Vu TNL, Lee M, Korean J. Chem. Eng., 30(3), 546 (2013)
Grimholt C, Skogestad S, Optimal PI control and verification of the SIMC tuning rule, in Proceedings of the IFAC Conference on Advances in PID Control PID’12, Brescia (Italy) (2012). (2012)
Skogestad S, Grimholt C, The SIMC Method for Smooth PID Controller, in PID Control in the Third Millennium, Advances in Industrial Control, Springer, 147 (2012). (2012)
Ziegler JG, Nichols NB, Trans. ASME, 64, 759 (1942)
Shamsuzzoha M, Skogestad S, J. Process Control, 20(10), 1220 (2010)
Hu W, Xiao G, Ind. Eng. Chem. Res., 2011, 2461 (2011)
Haugen F, Modeling, Identification Control, 31, 79 (2010)
Seki H, Shigemasa T, J. Process Control, 20(1), 217 (2010)
Veronesi M, Visioli A, J. Process Control, 20(3), 261 (2010)
Alcantara S, Vilanova R, Pedret C, J. Process Control, 23(4), 527 (2013)
Alcantara S, Pedret C, Vilanova R, J. Process Control, 20(5), 596 (2010)
Alcantara S, Zhang WD, Pedret C, Vilanova R, Skogestad S, J. Process Control, 21(6), 976 (2011)
Alcantara S, Vilanova R, Pedret C, Skogestad S, A look into robustness/performance and servo/regulation issues in PI tuning, in Proceedings of the IFAC Conference on Advances in PID Control PID’12, Brescia, Italy (2012). (2012)
Lee J, Cho W, Edgar TF, Ind. Eng. Chem. Res., 52, 12973 (2013)
Torrico BC, Cavalcante MU, Braga APS, Normey-Rico JE, Albuquerque AAM, Ind. Eng. Chem. Res., 52(33), 11646 (2013)
Shamsuzzoha M, Ind. Eng. Chem. Res., 52, 12973 (2013)
Alfaro VM, Vilanova R, Optimal robust tuning for 1DoF PI/PID control unifying FOPDT/SOPDT models, in IFAC Conference on Advances in PID Control PID’12, Brescia (Italy), March 28-30 (2012). (2012)
Isaksson AJ, Graebe SF, IEE Proc.-Control Theory Appl., 149(1), 41 (2002)
Visioli A, Practical PID Control, London (UK), Springer (2006). (2006)
Shamsuzzoha M, Skliar M, Lee M, Asia-Pacific J. Chem. Eng., 7, 93 (2012)
Kano M, Ogawa M, J. Process Control, 20(9), 969 (2010)
Rivera D, Morari M, Skogestad S, Ind. Eng. Chem. Process Des. Dev., 25, 252 (1986)
Morari M, Zafiriou E, Robust Process Control, NJ: Prentice-Hall Englewood Cliffs, NJ (1989). (1989)
Horn IG, Arulandu JR, Gombas CJ, Vanantwerp JG, Braatz RD, Ind. Eng. Chem. Res., 35(10), 3437 (1996)
Lee Y, Park S, Lee M, Brosilow C, AIChE J., 44(1), 106 (1998)
Skogestad S, J. Process Control, 13(4), 291 (2003)
Chien IL, Fruehauf P, Chem. Eng. Prog., 86, 33 (1990)
Shamsuzzoha M, Lee M, Ind. Eng. Chem. Res., 46(7), 2077 (2007)
Seborg D, Edgar T, Mellichamp D, Process Dynamics and Control, New York, Wiley (2004). (2004)
Chen D, Seborg DE, Ind. Eng. Chem. Res., 41(19), 4807 (2002)
Lee Y, Lee J, Park S, Chem. Eng. Sci., 55(17), 3481 (2000)
Yang XP, Wang QG, Hang CC, Lin C, Ind. Eng. Chem. Res., 41(17), 4288 (2002)
Wang YG, Cai WJ, Ind. Eng. Chem. Res., 41(12), 2910 (2002)
Tan W, Marquez HJ, Chen TW, J. Process Control, 13(3), 203 (2003)
Liu T, Zhang WD, Gu DY, J. Process Control, 15(5), 559 (2005)
Jung CS, Song HK, Hyun CJ, J. Process Control, 9, 265 (1999)
Majhi S, Atherton DP, Automatica, 36(11), 1651 (2000)
Kwak HJ, Sung SW, Lee IB, Park JY, Ind. Eng. Chem. Res., 38(2), 405 (1999)
Zhang WD, Gu DY, Wang W, Xu XM, Ind. Eng. Chem. Res., 43(1), 56 (2004)
Tyreus BD, Luyben W, Ind. Eng. Chem. Res., 31, 2625 (1992)
Luyben WL, Ind. Eng. Chem. Res., 35(10), 3480 (1996)
Shamsuzzoha M, Moonyong Lee M, Korean J. Chem. Eng., 25(4), 637 (2008)
Shamsuzzoha M, Lee SH, Lee MY, Korean J. Chem. Eng., 26(3), 622 (2009)
Vu TNL, Lee M, Korean J. Chem. Eng., 30(3), 546 (2013)
Grimholt C, Skogestad S, Optimal PI control and verification of the SIMC tuning rule, in Proceedings of the IFAC Conference on Advances in PID Control PID’12, Brescia (Italy) (2012). (2012)
Skogestad S, Grimholt C, The SIMC Method for Smooth PID Controller, in PID Control in the Third Millennium, Advances in Industrial Control, Springer, 147 (2012). (2012)
Ziegler JG, Nichols NB, Trans. ASME, 64, 759 (1942)
Shamsuzzoha M, Skogestad S, J. Process Control, 20(10), 1220 (2010)
Hu W, Xiao G, Ind. Eng. Chem. Res., 2011, 2461 (2011)
Haugen F, Modeling, Identification Control, 31, 79 (2010)
Seki H, Shigemasa T, J. Process Control, 20(1), 217 (2010)
Veronesi M, Visioli A, J. Process Control, 20(3), 261 (2010)
Alcantara S, Vilanova R, Pedret C, J. Process Control, 23(4), 527 (2013)
Alcantara S, Pedret C, Vilanova R, J. Process Control, 20(5), 596 (2010)
Alcantara S, Zhang WD, Pedret C, Vilanova R, Skogestad S, J. Process Control, 21(6), 976 (2011)
Alcantara S, Vilanova R, Pedret C, Skogestad S, A look into robustness/performance and servo/regulation issues in PI tuning, in Proceedings of the IFAC Conference on Advances in PID Control PID’12, Brescia, Italy (2012). (2012)
Lee J, Cho W, Edgar TF, Ind. Eng. Chem. Res., 52, 12973 (2013)
Torrico BC, Cavalcante MU, Braga APS, Normey-Rico JE, Albuquerque AAM, Ind. Eng. Chem. Res., 52(33), 11646 (2013)
Shamsuzzoha M, Ind. Eng. Chem. Res., 52, 12973 (2013)
Alfaro VM, Vilanova R, Optimal robust tuning for 1DoF PI/PID control unifying FOPDT/SOPDT models, in IFAC Conference on Advances in PID Control PID’12, Brescia (Italy), March 28-30 (2012). (2012)
Isaksson AJ, Graebe SF, IEE Proc.-Control Theory Appl., 149(1), 41 (2002)
Visioli A, Practical PID Control, London (UK), Springer (2006). (2006)
Shamsuzzoha M, Skliar M, Lee M, Asia-Pacific J. Chem. Eng., 7, 93 (2012)