Review Paper on Comparison of various PID Controllers Tuning Methodologies for Heat Exchanger Model

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Review Paper on Comparison of various PID Controllers Tuning Methodologies for Heat Exchanger Model Sumit 1, Ms. Kajal 2 1 Student, Department of Electrical Engineering, R.N College of Engineering, Rohtak, India 2 Assistant Professor, Department of Electrical Engineering, R.N College of Engineering, Rohtak ABSTRACT First-Order plus Delay-Time (FOPDT) model approximation can be carried out through either a kind of model reduction approach or a kind of system identification approach. In industrial applications heat exchanger plays a very vital role. In heat exchanger model controlling temperature range and achieving a desired temperature is a very complicated process. We can use different controlling techniques to achieve desired temperature. In this paper comparison of step response of Ziegler-Nichols PID controller (Method II), Cohen-Coon Method and Fuzzy logic controller has been developed for a heat exchanger model. A First- Order plus time delay system is very common in modern industry. For this particular model MATLAB simulations are carried out and responses are obtained for PID and Fuzzy Logic Controller. Key Words: PID controller, Ziegler-Nichols technique, Cohen-Coon, Tyreus-Luyben, AMIGO. I. INTRODUCTION Any control system when involves the movement of material or information it encounters time delay. Many industrial processes have the time delay effect introduced due to measurement delay. This delay causes unnecessary instability in whole system. There are a number of ways through which nonlinearity can be present in the system. The presence of time-delay thus complicates the whole system. Since most physical, chemical, mechanical systems are affected by temperature, so it is most often measured quantity. PID controllers [1] are very commonly used in control industry. There are a number of controlling techniques used to enhance the performance of controllers. In this paper the first part comprises of heat exchanger model and its First-Order plus Delay-time (FOPDT) approximation. The middle part consists of simulation of various techniques Ziegler-Nichols (oscillations method), Cohen-Coon Method Fuzzy logic controller. In the end part various results are compared qualitatively. Fig 1. Heat Exchanger Model 77

II. SYSTEM MODELING A chemical process for heating consists of chemical reactors and a heat exchanger system. The heat exchanger [4] heats up the fluid to a desired value by using superheated steam. Different assumptions have been considered regarding this process. First assumption is that, fluid level remains constant. The second assumption is that, heat storage capacity of the insulating wall is negligible. The above model can be expressed as First Order plus Time Delay (FOPDT) System. The first order plus time delay system has the following form of mathematical model: Where is time delay, T is Time constant and K is represents gain of the system. From the experimental data the transfer function [4] of the process model [4] is given by III. CONTROLLER DESIGN Different types of controller tuning techniques that can be applied to temperature control process are listed below: A. Ziegler-Nichols (method II) PID tuning B. Cohen-Coon Method C. Fuzzy Logic controller A. Ziegler-Nichols (method II) PID tuning PID controllers are integral part of the control industry. Earlier trial and error tuning was used to tune these PID controllers until Ziegler and Nichols published a paper in 1942 where they described two methods for tuning the parameters of P-, PI- and PID controllers. These two methods are the Ziegler-Nichols closed loop method [5] [6] and the Ziegler-Nichols open loop method. The present paper describes the closed-loop method. The tuning procedure is as follows: Step I: Find out the sign of process gain. Step II: Introduce proportional control. Step III: Raise proportional gain until sustained periodic oscillation occurs. Step IV: Note down ultimate gain Ku (gain at which oscillation occurs) and ultimate period Pu (distance between two consecutive crests) Step V:Calculate control parameters as prescribed by Ziegler and Nichols. Table 1 : Ziegler Nichols parameter for PID controller 78

On simulation Z-N PID gives following values Ku=2.9521, Pu=48.2 Therefore, by calculation using above table we get Kp=1.77, Ki=0.0735,Kd=10.672 Since, we know that PID controller is represented by Kp + Kp/Ti +Kp*Td Where Kp/Ti =Ki and Kp*Td=Kd B. Cohen-Coon Method A decade after Ziegler-Nichols published a paper based upon PID tuning Cohen-coon developed another tuning method. The Cohen-Coon method [7] is a more complex version of the Ziegler-Nichols method. The method is similar to the Ziegler- Nichols method but the difference comes with the fact that Cohen-Coon provides the faster rise time. Table 2- Cohen-Coon parameters On calculation C-C PID gives following values Kp=2.207 Ki=0.0757, Kd=10.672 C. Fuzzy Logic Controller The concept of Fuzzy Logic was conceived by LotfiZadeh, a professor at the University of California at Berkley, and presented not as a control methodology, but as a way of processing data by allowing partial set membership rather than crisp set membership or non-membership. This approach to set theory was not applied to control systems until the 70's due to insufficient small-computer capability prior to that time. Usually fuzzy logic controller performs better than PID controllers [10] for system exhibiting time delays in thermal models [11]. Fuzzy logic controllers based on human approach. This method is very frequent in European countries. A rule-based system [8] [9] is characterized by a set of rules that were defined by antecedents and consequents. Inference rules were made by a simple logic. A fuzzy logic controller has four main components as shown in Figure: a) Fuzzification b) Inference engine c) Rule base d) Defuzzification 79

Fig. 2- Rule base for fuzzy logic controller E represents error and CE represents change in error in the rule base table. In the above table NL- Negative Large, NM- Negative Medium, NS- Negative Small, Z- Zero, PS- Positive Small, PM- Positive Medium, PL- Positive Large. Further VL stands for Very Low, L- Low, MED- Medium, MOD- Moderate, H- High, VH- Very High, F- Full. Fuzzification [12] is a process in which,crisp variables are converted into linguistic variables. The membership functions are divided into a range. Rule base plays a very important role. They are in form of IF-THEN statements. Consider a rule If (temperature is cold ) than (heater is high ) Defuzzification generates a crisp numeric value. The defuzzified output is fed to the plant. 80

Fig. 3- Comparison diagram of Ziegler-Nichols, Cohen-Coon and Fuzzy logic controller 81

Fig. 4- Comparison of Z-N, C-C and Fuzzy logic controller Table for Comparison of Various Parameters for Different Controllers CONCLUSION In this paper the response of First-order plus Time-delay (FOPTD) process is compared using Ziegler-Nichols (method II), Cohen-Coon Method and fuzzy logic controller. According to the calculations, if system requires faster transient response Cohen-Coon method is better,and in case of Ziegler-Nichols response is faster but there is an overshoot of slightly more than 30 percent, but if system is sensitive to any kind of overshoot than fuzzy logic gives better response. REFERENCES [1]. Yingjian Xu, Dept. of Automation, Shanghai Jiao Tong Univ., Shanghai, China; A simple PID controller tuning strategy for first order plus dead time model electronics, Communications and Control(ICECC), 2011. [2]. AndriMirzal, Stability Analysis and Compensation of Time Delays in Analog Control Systems International Journal of Control and Automation Vol. 5, No. 4, December, 2012 [3]. Xinye Wang, Generalized exergy for finite-time heat transfer Processes, Transportation, Mechanical, and Electrical Engineering (TMEE), 2011 International Conference on 16-18 Dec. 2011, Page(s):1036 1039 [4]. Matlab: Control System Toolbox / Temperature Control in a Heat Exchanger. [5]. Susmita Das, Ayan Chakraborty, Jayanta Kumar Ray, Study on Different Tuning Approach with Incorporation of Simulation Aspect for Z-N (Ziegler-Nichols) Rules, International Journal of Scientific and Research Publications, Volume 2, Issue 8, August 2012 1 ISSN 2250-31537. 82

[6]. Bhaskar Lodh Simulink Based Model for Analysing the Ziegler Nichols Tuning Algorithm as applied on Speed Control of DC Motor International Journal of Advanced Research in Electrical, Electronics and Instrumentation [7]. N. Gireesh, Dr. G. Sreenivasulu, Comparison of PI Controller Performances for a Conical Tank Process using different tuning Published in: Advances in Electrical Engineering (ICAEE), 2014 International Conference on Date of Conference: 9-11 Jan. 2014 Page(s):1 4 INSPEC Accession Number: 14384490 DOI:10.1109/ICAEE.2014.6838426 Publisher:IEEE [8]. Tyreus B D W I Luyben, Tuning of PI controllers for integrator/dead time processes, ind.eng.chem. Res., 31, 2625-2628(1992). [9]. K.J. _Astrom, T. Hagglund, Revisiting the Ziegler Nichols step response method for PID control Journal of Process Control 14 (2004) 635 650. [10]. Vila Nova, PID Controller Tuning Rules for Robust step response of First-Order-Plus-Dead-Time models, American Control Conference, 2006 on 14-16 June 2006, Minneapolis, MN [11]. Khan, S. (2014). Modelling and temperature control of heat exchanger process. International Journal for Research in applied science and engineering technology. [12]. P. Ramanathan, Fuzzy logic controller of temperature regulation process Middle-East Journal of Scientific Research 20 (11): 1524-1528, 2014. 83