D. Krishnaa, K. Suryanarayanab, G. Aparnab, and R. Padma Sreeb,*

Department of Chemical Engineering, M.V.G.R. College of Engineering, Vizianagaram, India
Department of Chemical Engineering, Andhra University College of Engineering (A) Visakha-patnam, India


Download Citation: |
Download PDF


ABSTRACT


Tuning Proportional Integral and Derivative (PID) controllers for unstable Second Order Plus Time Delay systems with a Zero (SOPTDZ), based on internal model control (IMC) and stability analysis (SA) principles is proposed. The controllers designed by the proposed methods are used to control unstable jacketed Continuous Stirred Tank Reactors (CSTR), carry-ing out irreversible first order reaction. The performance of proposed controllers is compared with the synthesis method. Simulation results on nonlinear unstable continuous stirred tank re-actors and transfer function models are presented to the show the efficiency of the proposed con-trollers.


Keywords: Internal model control; stability analysis method; synthesis method; CSTR; PID controller; Unstable systems; Second Order Plus Time Delay system with a Zero (SOPTDZ).


Share this article with your colleagues

 


REFERENCES


  1. [1] Bequette, B. W. 2003. “Process control, Modeling, design and simulation”. Pren-tice Hall India. New Delhi.

  2. [2] Jacobsen, E. W. 1999. On the dynamics of integrated plants Non-minimum phase behavior. J Process Control, 9: 439-451.

  3. [3] Padmasree, R. and Chidambaram, M. 2006. “Control of unstable systems”. Narosa publishers. New Delhi.

  4. [4] Kausthubh, S. M. and Chidambaram, M. 2000. Control of Isothermal Crystallizers, Proc. CHEMCON, Calcutta., December 18th to 21st .2000.

  5. [5] Lee, Y., Lee, J., and Park, S. 2000. PIDcontroller tuning for integrating and unstableprocesses with time delay. Chemical Engineering Science, 55:3481-3493.

  6. [6] Wang, L.W. and Hwang, S. H. 2005. Identification and control for unstable processes of three dynamics, Chemical Engineering Science, 192: 34-61.

  7. [7] Wright, R. A. and Kravaris, C. 2006. Two degree of freedom output feedback controllers for discrete time nonlinear systems. Chemical Engineering Science, 61: 4676-4688.

  8. [8] Feng, L., Wang, J. L., and Poh, E. K. 2007. Improved robust model predictive control with structured uncertainty. J Process Control, 17: 683-688.


ARTICLE INFORMATION


Received: 2011-05-24
Revised: 2011-07-02
Accepted: 2011-09-29
Available Online: 2012-03-01


Cite this article:

Krishna, D., Suryanarayana, K., Aparna, G., Sree, R.P. 2012. Tuning of PID controllers for unstable continuous stirred tank reactors. International Journal of Applied Science and Engineering, 10, 1–18. https://doi.org/10.6703/IJASE.2012.10(1).1