ISSN: 0256-1115 (print version) ISSN: 1975-7220 (electronic version)
Copyright © 2024 KICHE. All rights reserved

Articles & Issues

Language
English
Conflict of Interest
In relation to this article, we declare that there is no conflict of interest.
Publication history
Received April 23, 2011
Accepted September 15, 2011
articles 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.
Copyright © KIChE. All rights reserved.

All issues

Input/output linearization with a two-degree-of-freedom scheme for uncertain nonlinear processes

Center of Excellence for Petroleum, Petrochemicals, and Advanced Materials, Department of Chemical Engineering, Faculty of Engineering, Kasetsart University, Bangkok 10900, Thailand
fengcnp@ku.ac.th
Korean Journal of Chemical Engineering, June 2012, 29(6), 716-723(8), 10.1007/s11814-011-0243-x
downloadDownload PDF

Abstract

This work presents a new method to control processes with unmeasured input disturbance and random noise parametric uncertainty. The developed method takes advantage of a two-degree-of-freedom control structure in which setpoint regulation and load disturbance rejection are integrated in the controller synthesis. Input/output linearization is selected to provide the setpoint tracking ability. For disturbance rejection, the high-gain technique is used to compensate for the effect of the uncertainty. The control performance of the method is evaluated through numerical simulation of continuous stirred tank reactors with uncertainty. The simulation results show that both unmeasured disturbance and parametric uncertainty can be effectively compensated for by the proposed control method.

References

Tsai MH, Tung PC, J. Process Control, 20(6), 777 (2010)
Wu KL, Yu CC, Cheng YC, J. Process Control, 11(3), 311 (2001)
Tan W, ISA T., 49, 311 (2010)
Liu T, Zhang WD, Gu DY, J. Process Control, 15(5), 559 (2005)
Liu T, Zhang WD, Gao F, Ind. Eng. Chem. Res., 46(20), 6546 (2007)
Liu T, Gu DY, Zhang WD, J. Process Control, 15(2), 159 (2005)
Shamsuzzoha M, Moonyong Lee M, Korean J. Chem. Eng., 25(4), 637 (2008)
Chen J, Chou KT, Korean J. Chem. Eng., 26(6), 1512 (2009)
Wright RA, Kravaris C, Chem. Eng. Sci., 60(15), 4323 (2005)
Wright RA, Kravaris C, Chem. Eng. Sci., 61(14), 4676 (2006)
Slotine JJE, Li W, Applied nonlinear control, Prentice Hall, Englewood Cliffs, NJ (1991)
Henson MA, Seborg W, Nonlinear process control, Prentice Hall, Upper Saddle River, NJ (1996)
Aufderheide B, Bequette BW, Comput. Chem. Eng., 27(8-9), 1079 (2003)
Kanter JR, Soroush M, Seiders WD, Ind. Eng. Chem. Res., 40(9), 2069 (2001)
Wright RA, Kravaris C, Chem. Eng. Sci., 58(14), 3243 (2003)

The Korean Institute of Chemical Engineers. F5, 119, Anam-ro, Seongbuk-gu, 233 Spring Street Seoul 02856, South Korea.
Phone No. +82-2-458-3078FAX No. +82-507-804-0669E-mail : kiche@kiche.or.kr

Copyright (C) KICHE.all rights reserved.

- Korean Journal of Chemical Engineering 상단으로