Trends in Fractional Order Controllers

International Journal of Emerging Technology and Advanced Engineering Website: www.ijetae.com (ISSN 2250-2459, Volume 2, Issue 3, March 2012) Trends ...
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International Journal of Emerging Technology and Advanced Engineering Website: www.ijetae.com (ISSN 2250-2459, Volume 2, Issue 3, March 2012)

Trends in Fractional Order Controllers Karanjkar D. S.1,, Chatterji. S.2, Venkateswaran P.R.3 1

Head, Instrumentation Engineering Department, Institute of Petrochemical Engineering, Lonere, Raigad, Maharastra, India. 2 Professor & Head, Electrical Engineering Department, National Institute of Technical Teachers’ Training and Research, Chandigarh, India. 3 Senior Development Engineer, Bharat Heavy Electricals Limited, Tiruchirappalli, India. 1

[email protected]

II. INTRODUCTION TO FRACTIONAL CALCULUS

Abstract— Use of fractional order integral and derivative operators became very popular among many research areas during the last decade. This paper reviews the trends in fractional order controller and ongoing research on tuning of its parameters. Using n integer toolbox with MATLAB/SIMULINK, series and parallel connected fractional order PID controllers have designed for first-order system and simulation results have been compared. The application of fractional order calculus in controller design introduces superior performance than a conventional controller.

The concept of fractional calculus (calculus of integrals and derivatives of any arbitrary real or complex order) was raised in year 1695 by Marquis de L‘Hopital to Gottfried Wilhelm Leibniz regarding solution of non-integer order derivative. On September 30th 1695, Leibniz replied to L‘ Hopital ―This is an apparent paradox from which one day, useful consequences will be drawn‖. Between 1695 and 1819 several mathematicians (Euler in 1730, Lagrange in 1772, Laplace in 1812, and so on..) mentioned it. The question raised in 1695 was only partly answered 124 years later! [1] in 1819, by S. F. Lacroix. The real journey of development of fractional calculus started in 1974 when the first monograph on fractional calculus was published by academic press [2]. Since then many books were published until now [3-12]. Fractional calculus is presently being applied in the field of mathematics, physics, engineering, chemistry, computer science, mechanics, pharmacology, material science, neuroscience and neurology. Percentage utilization of fractional calculus in mathematics is around 25 percentage followed by that of in physics around 20 percentage while in engineering field it is around 14 percentage [13]. Fractional calculus will perhaps be the calculus of twenty-first century. The fractional-order differentiator can be denoted by a general fundamental

Keywords— Fractional order controllers, PID, ninteger toolbox.

I. INTRODUCTION Fractional order integral and derivative operators have found several applications in large areas of research during the last decade. Application of fractional order calculus to conventional controller design extends the opportunity of improved performance. Outline of the paper is as follows. Section two discusses the introduction and development of fractional calculus. Third section deals with applications of the fractional calculus in control systems and introduction of four types of fractional controller and tuning of fractional PID controller have been discussed. In fifth section the design of series and parallel FOPID controllers are presented using ‗ninteger‘ toolbox. Conclusions and future scope of work are discussed in the sixth section.

operator a Dtq as a generalization of the differential and integral operators, which is defined as follows [14]:

383

International Journal of Emerging Technology and Advanced Engineering Website: www.ijetae.com (ISSN 2250-2459, Volume 2, Issue 3, March 2012)  q d  dt q  q a Dt  1 t  ( d )  q  a

, R(q)  0

III. APPLICATIONS OF FRACTIONAL CALCULUS IN CONTROL

, R(q)  0



Classification of dynamic systems according to the order of the plant and the controller can be done as: i) integer order system - integer order controller ii) integer order system - fractional order controller iii) fractional order system - integer order controller and iv) fractional order system - fractional order controller. In fractional order controller given by, Gc(s) = Kp + Ki s-λ + Kd sµ (where Kp, Ki and Kd are proportional, integral and derivative gains respectively) more parameters need to be tuned. It‘s unfair but, theoretically, always better than integer order controller.

, R(q)  0

(1) where, q is the fractional order which can be a complex number, the constant a is related to the initial conditions. There are two commonly used definitions for the general fractional differentiation and integration, i.e., the Grünwald–Letnikov (GL) and the Riemann Liouville (RL). The GL definition is as mentioned below:

q a Dt

f (t )  lim

h 0

1 h

 (t  q ) h 

q

 (1)  j  f (t  jh) j

q

λ

PI

PID

PI

PID

λ=1

λ =1

j 0

λ

(2) P

where, . is a flooring-operator. On the other hand, the RL (3)

definition is given by:

q a Dt f (t ) 

1 dn (n  q) dt n

0

t

d , for (n  1  q  n) q  n 1

a

where, ( x) is the well known Euler‘s Gamma function. Their is another definition of fractional differintegral introduced by Caputo in [15] which can be written as: t

q a Dt

1 f (t )   ( q  n)

f ( n) ( )

 (t  )

q  n 1

d ,

P

µ 0 µ=1 λ λ µ Fig.1 PI D controller: from points to plane µ=1

PD

µ λ

Many control objects are fractional-order ones, so that the fractional approach for control of the fractional-order systems becomes a meaningful work. This approach (as shown in fig.1) has changed the point based control scheme to plane based scheme. Achieving something better is always the major concern from control engineering point of view. Existing evidences have confirmed that the best fractional order controller outperforms the best integer order controller. It has also been answered in the literature why to consider fractional order control even when integer order control works comparatively quite well [17]. Since integer-order PID control dominates the industry, it can be believed that fractional order-PID control will gain increasing impact and wide acceptance. The use of fractional-order calculus in dynamic system control was initiated in year 1960 [18]. Since then application of fractional calculus was extended to distributed control system[19], to linear feedback control [20], for linear approximation of transfer function [21] and to process control strategy with fractional derivatives through recursivity [22]. In year 1990 patent was registered for robust fractional controller (CRONE-Contrˆole Robuste d‘Ordre Non Entier) approach [23].

f ( )

 (t  )

PD

n  1  q  n (4)

a

The stability of fractional order differential equations can be supposed to be as equal as that of their integer orders counterparts, this is because; systems with memory are typically more stable as compared to their memory-less alternatives [16]. 384

International Journal of Emerging Technology and Advanced Engineering Website: www.ijetae.com (ISSN 2250-2459, Volume 2, Issue 3, March 2012) Quantitative Feedback Theory (QFT) and evolutionary algorithms have been used for tuning of a fractional PID controller.[42-46]. A paper [47] presents a different method for parameter adjustment scheme to improve the robustness of fractional fuzzy adaptive sliding-mode control by the use of an ANFIS architecture for two degree of freedom robot. The paper [48] describes an application of PSO to the problem of designing a fractional-order PID controller based on ITAE. A fractional high-gain adaptive controller for a class of linear systems was presented in the paper [49]. The paper [50] deals with the design of FO-PI for a coupled tank system. A global search optimization method with bacterial foraging technique oriented by particle swarm optimization was applied for optimizing five parameters of fractional controllers in the year 2009 [51]. The self-tuning regulators form an important sub-class of conventional adaptive controllers. Design of a fractional order selftuning regulator has been presented in [52]. The particle swarm optimization algorithm has been utilized for the online identification of parameters of the dynamic fractional order process while the tuning of the controller parameters has been performed by differential evolution. The paper [53] presents adaptive genetic algorithm (AGA) for the multi-objective optimization design of a fractional PID controller. The article [54] describes an application of differential evolution (DE) to the design of fractional-order controller. The paper [55] presents a robust adaptive control using fractional order systems as parallel feedforward in the adaptation loop based on the ―Almost Strictly Positive Realness (ASPR) property‖ of the plant. In paper [56] the tuning of FOPID controller of electromagnetic actuator (EMA) system for aerofin control (AFC) using particle swarm optimization (PSO) has been presented. Another method for tuning of fractional controller based on the relay feedback technique has been presented in [57]. Paper [58] reports about the design of FOPID using multi-objective optimization based genetic algorithm. Another work [59] published in the year 2010, on fractional PIλDμ controller tuning, explains the process of tuning by internal model control (IMC) based method with process described by fractional transfer function. A graphical tuning method of PIλDµ controllers for fractionalorder processes with time-delay has been presented in [60]. In this work a random search optimization method has been introduced for fractional order model reduction and the parameters of fractional order controllers have been tuned by internal model control (IMC) based method. Fractional order sliding mode control has been presented in [61].

Robust regulators with fractional structure and fractional order state equations for the control of visco-elastic damped structures was presented in year 1991 [24, 25]. The concept of tilt-integral-derivative (TID) (refer fig. 2) was presented and patent was registered in 1994 [26]. The first practical application of CRONE (refer to CRONE Group‘s introduction and the demo of MATLAB CRONE Toolbox) control was presented in year 1995 [27]. Fractional order lead-lag compensator was presented in year 2000 [28]. Application of fractional calculus in control theory was accelerated after year 2002. In the year 2002 a special issue on fractional order calculus and its applications was published in an international journal of Nonlinear Dynamics and Chaos in Engineering Systems [29]. A tutorial Workshop in IEEE International Conference on Fractional Order Calculus in Control and Robotics was organized in Las Vegas in the year 2002 [30]. Tuning of PIλDμ controllers is a new research subject during last few years. Some important articles on design and parameter optimization of fractional controllers are presented here. I

Ref

±

T

1/S

I/S(1/n)

D

+

Plant

s

Fig. 2. Tilt-integral-derivative controller P

Ref

±

I

D

1 I/S

+

Plant

s

Fig.3. FO-PID (PIλDμ) controller (where, 0 ≤ λ ≤ 1 & 0 ≤ µ ≤ 1)

Articles [31-36] present various methodologies to design and optimize the fractional order controller viz. PSO, GA, minimization of ISE etc. Many tuning techniques for obtaining the parameters of controllers were introduced since inception of PID controller. The most well known tuning rules for classical controllers are given by Ziegler-Nichols [37] and Åström-Hägglund [38] which have been the milestones for developments of many other methods.Several tuning rules similar to Ziegler and Nichols for integer PID, were presented [39,40,41] in the year 2006. 385

International Journal of Emerging Technology and Advanced Engineering Website: www.ijetae.com (ISSN 2250-2459, Volume 2, Issue 3, March 2012) The control objectives have been achieved by adopting the reaching law approach of sliding mode control. In a similar work published in the year 2010 [62], an optimal fractional order controller has been designed and the optimal values of FOPID controller parameters for minimizing the cost function have been tuned using an evolutionary algorithm. Design of FOPD for motion control and minimum integral squared error (ISE) criterion approach is presented in [63,64]. In another paper [65] a servo control strategy for tuning of fractional order PI controllers is presented for fractional order system models with and without time delays. Recent article of the year 2011 [66], presents the design of internal model controller (IMC) based fractional order two-degrees of freedom controller with robust control. The features of the IMC based PID controller have been combined with fractional order controller. Tuning of FOPID controller using Taylor series expansion of desired closed-loop and actual closedloop transfer functions has been presented in [67]. This literature survey reveals that the fractional controller gives better results as compared to the conventional PID controller. Tuning of FOPID controller is difficult as five tuning parameters need to be tuned and theoretically infinite memory is essential for its digital implementation. In next section simulation example of FOPID is presented.

In this section, series and parallel configuration of fractional order PID is designed in MATLAB/ SIMULINK using ‗nid‘ block of ‗ninteger‘ toolbox, which uses ‗crone‘ formula with ‗mcltime‘ expansion for fractional operator implementation. Simulink model (Fig.4) is designed for implementation of conventional (parallel) PID, parallelFOPID and series- FOPID controllers for first order system with transfer function s/(s+1). Parameters of conventional PID have been optimized using SIMULINK control design as shown in Table.1. Design of parallel and series-FOPID is done according to the parameters shown in table 2.

IV. SIMULATION RESULTS Three types of PID configurations have been mostly used in industrial applications- parallel, series and ideal. Parallel configuration is commonly used in process control applications. The response of the conventional PID with parallel configuration can be represented as: KP .e(s) + KC .(1/TI.s).e(s)+KD. TD.s.e(s) (5) Where, KP, KC, and KD are proportional, integral and derivative gains respectively, T I and TD are integral and derivative time, and e(s) is error between measured variable and set-point. Transfer function of fractional order PID (series configuration) can be represented by: KPKC [1+(1/Ti.salpha)]KD.sbeta

Fig.4. Simulink implementation of series, parallel and conventional PID for first order system. TABLE I OPTIMIZED PARAMETERS FOR PARALLEL PID WITH MINIMUM ERROR CRITERIA FOR FIRST ORDER SYSTEM

(6)

Where, ‗alpha‘ and ‗beta‘ are the fractional powers of integral and derivative terms respectively. Response of Fractional order PID (parallel configuration) can be represented by: KP .e(s) + KC .(1/Ti.salpha).e(s)+KD. TD.sbeta.e(s)

(7) 386

KP

TI

TD

1.3185

2.2306

-0.2735

International Journal of Emerging Technology and Advanced Engineering Website: www.ijetae.com (ISSN 2250-2459, Volume 2, Issue 3, March 2012) TABLE III PARAMETERS FOR PARALLEL AND SERIES FO-PID FOR FIRST ORDER SYSTEM KP

KI

KD

alpha

beta

Parallel FOPID

11

11

03

0.5

0.4

Series FOPID (case I)

11

11

03

0.5

0.4

Series FOPID (case II)

11

1

01

0.75

0.5

V. CONCLUSION AND FUTURE SCOPE OF WORK The use of fractional calculus has gained popularity among many research areas during the last decade. Its theoretical and practical interests are well established nowadays, and its applicability to science and engineering can be considered as an emerging new analytical approach. The introduction of fractional order calculus to conventional controller design extends the scope of added performance improvement. Many existing control schemes can be modified with the notion of fractional order calculus. Conventional PID performance has many limits due to dead time, disturbances, noise, etc. Fractional-order PID control is the development of the integer-order PID control. Design of fractional order controller is an on-going research topic now a days. Significant work has been done on CRONE controller and its industrial applications. Compared to integer PID controller, fractional PID controller has more advantages, but the difficulty of tuning methods of the fractional PID is still a challenge to be resolved. Fractional order PID controllers could benefit the industry significantly with a wide spread impact when FOPID parameter tuning techniques have been well developed. In order to achieve better results and to make industry acceptable FOPID, a need is felt for designing new methods for auto-tuning and self-tuning the parameters of PIλDμ controllers and development digital algorithm for implementation of FOPID using microprocessor or microcontroller.

Simulation results (Fig.5) shows that fractional order PID with parallel configuration gives better response to step input in terms of peak overshoot and settling time, even when the parameters of FOPID were not optimized. Parallel FOPID do not offer any overshoot and settling time is also much less as compared to the conventional PID controller. Response of series FOPID - case I, with (similar parameters as that of parallel FOPID) higher integral gain and lower values of ‗alpha‘ exhibit high peak overshoot and damping. The integral gain can be lowered while fractional order of integration can be increased in order to minimize the peak overshoot and damping (as in series FOPID-case II). Fractional order controller provides additional flexibility in terms of two additional control parameters- alpha and beta. For second order system it is seen that series configuration of FOPID also gives better response like parallel configuration. Based on process under control one can select configuration of controller.

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1.4 Series FOPID responce with Kp=11,Ki=11,alfa=0.5,beta=0.4 & Kd=3

1.2 1

[2]

0.8 Responce of PID-optimized 0.6

Parallel FOPID responce with Kp=11,Ki=11,alfa=0.5, beta=0.4 & Kd=3

0.4

Series FOPID responce with Kp=11,Ki=1,alfa=0.75,beta=0.5 & Kd=1

0.2 0

[3]

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[6]

Fig.5. Responses of Fractional (Series & Parallel) and conventional PID to step input

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