Keywords-Non-minimum phase process; fractional-order; unstable pole-zero cancellation; PID controller; flexible link robot;initial undershoot

Similar documents
IMC based automatic tuning method for PID controllers in a Smith predictor configuration

CHAPTER 7 FRACTIONAL ORDER SYSTEMS WITH FRACTIONAL ORDER CONTROLLERS

Feedback Control of Linear SISO systems. Process Dynamics and Control

Model-based PID tuning for high-order processes: when to approximate

Design and Tuning of Fractional-order PID Controllers for Time-delayed Processes

Optimal Polynomial Control for Discrete-Time Systems

Robust PID and Fractional PI Controllers Tuning for General Plant Model

Observer Based Friction Cancellation in Mechanical Systems

Additional Closed-Loop Frequency Response Material (Second edition, Chapter 14)

Lecture 12. Upcoming labs: Final Exam on 12/21/2015 (Monday)10:30-12:30

Dr Ian R. Manchester

Ian G. Horn, Jeffery R. Arulandu, Christopher J. Gombas, Jeremy G. VanAntwerp, and Richard D. Braatz*

PM diagram of the Transfer Function and its use in the Design of Controllers

MAS107 Control Theory Exam Solutions 2008

A unified double-loop multi-scale control strategy for NMP integrating-unstable systems

Lecture 6 Classical Control Overview IV. Dr. Radhakant Padhi Asst. Professor Dept. of Aerospace Engineering Indian Institute of Science - Bangalore

2 Problem formulation. Fig. 1 Unity-feedback system. where A(s) and B(s) are coprime polynomials. The reference input is.

Contents. PART I METHODS AND CONCEPTS 2. Transfer Function Approach Frequency Domain Representations... 42

6.1 Sketch the z-domain root locus and find the critical gain for the following systems K., the closed-loop characteristic equation is K + z 0.

Performance Limitations for Linear Feedback Systems in the Presence of Plant Uncertainty

Automatic Control 2. Loop shaping. Prof. Alberto Bemporad. University of Trento. Academic year

FEEDFORWARD CONTROLLER DESIGN BASED ON H ANALYSIS

Learn2Control Laboratory

Unit 11 - Week 7: Quantitative feedback theory (Part 1/2)

Control of integral processes with dead time Part IV: various issues about PI controllers

Chapter 2 Review of Linear and Nonlinear Controller Designs

A NEW APPROACH TO MIXED H 2 /H OPTIMAL PI/PID CONTROLLER DESIGN

Position in the xy plane y position x position

Research Article On Complementary Root Locus of Biproper Transfer Functions

Comparison of Feedback Controller for Link Stabilizing Units of the Laser Based Synchronization System used at the European XFEL

MULTILOOP PI CONTROLLER FOR ACHIEVING SIMULTANEOUS TIME AND FREQUENCY DOMAIN SPECIFICATIONS

INTRODUCTION TO DIGITAL CONTROL

Dr Ian R. Manchester Dr Ian R. Manchester AMME 3500 : Root Locus

CDS 101/110a: Lecture 8-1 Frequency Domain Design

Robust fixed-order H Controller Design for Spectral Models by Convex Optimization

Linear State Feedback Controller Design

H-infinity Model Reference Controller Design for Magnetic Levitation System

1 An Overview and Brief History of Feedback Control 1. 2 Dynamic Models 23. Contents. Preface. xiii

Let the plant and controller be described as:-

Robust Internal Model Control for Impulse Elimination of Singular Systems

H-Infinity Controller Design for a Continuous Stirred Tank Reactor

Design and Stability Analysis of Single-Input Fuzzy Logic Controller

Parameter Derivation of Type-2 Discrete-Time Phase-Locked Loops Containing Feedback Delays

Analysis and Synthesis of Single-Input Single-Output Control Systems

Process Identification for an SOPDT Model Using Rectangular Pulse Input

arxiv: v1 [math.oc] 1 May 2014

Simulation Study on Pressure Control using Nonlinear Input/Output Linearization Method and Classical PID Approach

Chapter 2. Classical Control System Design. Dutch Institute of Systems and Control

Realization of Hull Stability Control System for Continuous Track Vehicle with the Robot Arm

Tuning of fractional PI controllers for fractional order system models with and without time delays

Lecture 5 Classical Control Overview III. Dr. Radhakant Padhi Asst. Professor Dept. of Aerospace Engineering Indian Institute of Science - Bangalore

Inverted Pendulum. Objectives

CHAPTER 3 TUNING METHODS OF CONTROLLER

Lyapunov Stability of Linear Predictor Feedback for Distributed Input Delays

H CONTROL AND SLIDING MODE CONTROL OF MAGNETIC LEVITATION SYSTEM

Optimal Joint Detection and Estimation in Linear Models

Improve Performance of Multivariable Robust Control in Boiler System

Index. INDEX_p /15/02 3:08 PM Page 765

A FEEDBACK STRUCTURE WITH HIGHER ORDER DERIVATIVES IN REGULATOR. Ryszard Gessing

EE 422G - Signals and Systems Laboratory

ADAPTIVE TEMPERATURE CONTROL IN CONTINUOUS STIRRED TANK REACTOR

YTÜ Mechanical Engineering Department

QUANTITATIVE L P STABILITY ANALYSIS OF A CLASS OF LINEAR TIME-VARYING FEEDBACK SYSTEMS

RELAY CONTROL WITH PARALLEL COMPENSATOR FOR NONMINIMUM PHASE PLANTS. Ryszard Gessing

1 Loop Control. 1.1 Open-loop. ISS0065 Control Instrumentation

MEM 355 Performance Enhancement of Dynamical Systems

Advanced Aerospace Control. Marco Lovera Dipartimento di Scienze e Tecnologie Aerospaziali, Politecnico di Milano

On-Line Fast Algebraic Parameter and State Estimation for a DC Motor Applied to Adaptive Control

MULTILOOP CONTROL APPLIED TO INTEGRATOR MIMO. PROCESSES. A Preliminary Study

Review on Aircraft Gain Scheduling

Nonlinear Trajectory Tracking for Fixed Wing UAVs via Backstepping and Parameter Adaptation. Wei Ren

Robust Loop Shaping Controller Design for Spectral Models by Quadratic Programming

Chapter 2 Background and Preliminaries

Auto-tuning Fractional Order Control of a Laboratory Scale Equipment

ECSE 4962 Control Systems Design. A Brief Tutorial on Control Design

Design of Decentralised PI Controller using Model Reference Adaptive Control for Quadruple Tank Process

IMPROVED TECHNIQUE OF MULTI-STAGE COMPENSATION. K. M. Yanev A. Obok Opok

FEEDBACK CONTROL SYSTEMS

Iterative Controller Tuning Using Bode s Integrals

Design and Control of Novel Tri-rotor UAV

Exercises for lectures 13 Design using frequency methods

EECE Adaptive Control

Dr Ian R. Manchester Dr Ian R. Manchester AMME 3500 : Review

CompensatorTuning for Didturbance Rejection Associated with Delayed Double Integrating Processes, Part II: Feedback Lag-lead First-order Compensator

A Design Method for Smith Predictors for Minimum-Phase Time-Delay Plants

Chapter 7 Interconnected Systems and Feedback: Well-Posedness, Stability, and Performance 7. Introduction Feedback control is a powerful approach to o

Aircraft Stability & Control

Exam. 135 minutes + 15 minutes reading time

CYBER EXPLORATION LABORATORY EXPERIMENTS

THE ANNALS OF "DUNAREA DE JOS" UNIVERSITY OF GALATI FASCICLE III, 2000 ISSN X ELECTROTECHNICS, ELECTRONICS, AUTOMATIC CONTROL, INFORMATICS

MANY adaptive control methods rely on parameter estimation

Steam-Hydraulic Turbines Load Frequency Controller Based on Fuzzy Logic Control

Lecture 25: Tue Nov 27, 2018

Control Of Heat Exchanger Using Internal Model Controller

Cascade Control of a Continuous Stirred Tank Reactor (CSTR)

Research Article. World Journal of Engineering Research and Technology WJERT.

A Method for PID Controller Tuning Using Nonlinear Control Techniques*

Linear Quadratic Gausssian Control Design with Loop Transfer Recovery

Robust Control. 2nd class. Spring, 2018 Instructor: Prof. Masayuki Fujita (S5-303B) Tue., 17th April, 2018, 10:45~12:15, S423 Lecture Room

An Iteration-Domain Filter for Controlling Transient Growth in Iterative Learning Control

Transcription:

Method for Undershoot-Less Control of Non- Minimum Phase Plants Based on Partial Cancellation of the Non-Minimum Phase Zero: Application to Flexible-Link Robots F. Merrikh-Bayat and F. Bayat Department of Electrical and Computer Engineering Uniersity of Zanjan Zanjan, Iran Email: f.bayat@nu.ac.ir, bayat.farhad@nu.ac.ir Abstract As a well understood classical fact, non- minimum phase eros of the process located in a feedback connection cannot be cancelled by the corresponding poles of controller since such a cancellation leads to internal instability. This impossibility of cancellation is the source of many limitations in dealing with the feedback control of nonminimum phase processes. The aim of this paper is to study the possibility and usefulness of partial (fractional-order) cancellation of such eros for undershoot-less control of non-minimum phase processes. In this method first the nonminimum phase ero of the process is cancelled to an arbitrary degree by the proposed pre-compensator and then a classical controller is designed to control the series connection of these two systems. Since plants with multiple non-minimum phase eros and oscillatory poles are ery common in the problems related to robotics, the proposed method is applied to these systems to confirm its effectieness. Keywords-Non-minimum phase process; fractional-order; unstable pole-ero cancellation; PID controller; flexible link robot;initial undershoot I. INTRODUCTION It is well understood that non-minimum phase processes constitute a challenging research area in the field of control engineering. Non-minimum phase eros appear unaoidably in some important industrial processes such as steam generators [], aircrafts [2], [3], flexiblelink manipulators [4], continuous stirred tank reactors (CSTRs) [5], electronic circuits [6], and so on. As a ery well known classical fact, non-minimum phase eros of the process put some limitations on the performance of the corresponding feedback system [7]-[0]. More precisely, these limitations can be concluded, e.g., from the classical root-locus method [], asymptotic LQG theory [9], waterbed effect phenomena [2], and the LTR problem [3]. In the field of linear time-inariant (LTI) systems, the source of all of the aboe-mentioned limitations is that the non-minimum phase ero of the gien process cannot be cancelled by unstable pole of the controller since such a cancellation leads to internal instability [4]. During the past decades arious methods hae been deeloped by researchers for the control of processes with non-minimum phase eros (see, for example, [5]-[7] and the references therein for more information on this subject). Among others, according to the simplicity and high achieement of the feedback control strategy in dealing with most of the real-world industrial problems, it is strictly preferred to deelop more effectie methods to the control of non-minimum phase processes by using this technique. Howeer, as mentioned before, impossibility of unstable pole-ero cancellation is the main limitation of this method, which is to be partly remoed in this paper. An author of this paper already showed [8] that although unstable pole-ero cancellation is impractical in LTI feedback systems and leads to internal instability, the partial (or, fractional-order) unstable pole-ero cancellation is possible and can be ery effectie. In fact, it is proed in [8] that any non-minimum phase ero (unstable pole) of the gien process can partly be cancelled by a pole (ero) of the controller without resulting in an internally-unstable feedback system. Interesting obseration is that this cancellation can also increase the phase and gain margin of the closed-loop system, and consequently, partly remoe some of the classical limitations caused by non-minimum phase eros. Note that the method proposed in [8] can be used to

cancel any non-minimum phase ero or unstable pole of a process to an arbitrary degree. The aim of this paper is to study the control of certain class of robot arms by combining the proposed method for cancellation of non-minimum phase eros of the process and the classical PID control. A relatiely similar approach, which studies the integral performance indices of a feedback system (in which a PI controller is applied in series with a fractional-order pole-ero canceller to control a second order process) is presented in [9]. Here it is worth to mention that PID controllers commonly do not lead to satisfactory results when the process is nonminimum phase, has poles with a ery low damping ratio, or exhibit large dead times [20]. Hence, from the practical point of iew it is ery important to deelop effectie methods to remoe these limitations. Since transfer functions with multiple non-minimum phase eros and oscillatory poles frequently appear in dealing with flexible arm robots, the studies of this paper are mainly focused on these systems. Howeer, the proposed ideas are ery general and can be applied to any other non-minimum phase process as well. The rest of this paper is organied as follows. The proposed method for the control of non-minimum phase processes is presented in Section II. Illustratie examples, which are adopted from flexible-link robots, are studied in Section III, and finally Section IV concludes the paper. II. MAIN RESULTS Fig. shows the proposed feedback strategy to control a non-minimum phase process with transfer function Gs () ( rt (), dt () and nt () stand for the command, disturbance and noise, respectiely). As it is obsered, in this method first we partially cancel the non-minimum phase ero (or, if necessary, the unstable pole) of Gs () by putting a pre-compensator with transfer function C () s in series with it (see the discussion below). In fact, the role of C () s in Fig. is to remoe some of the limitations caused by non-minimum phase eros of the process by partially remoing them. It means that applying C () s will make the control problem easier to sole by increasing the phase and gain margin [8]. As it will be shown in the following, C () s is a rational function in non-integer (fractional) powers of s. Hence, Ps () C () sgs () in Fig. is a rational function in non-integer powers of s as well. C 2 () s in this figure is used to control the system with transfer function Ps (). Note that since Ps () contains fractional powers of s, C 2 () s may be designed using either classical design algorithms or the methods specially deeloped for the control of fractional-order processes (see, for example, [2]-[24] and the references therin for more information on the latter case). For the sake of simplicity we will use Fig. The general form of the proposed feedback system with precompensator (fractional-order pole-ero canceller) the first approach in this paper. In the following, we briefly reiew the main properties of the fractional-order pole ero canceller, C () s, without presenting the proofs. More details can be found in [8]. Suppose that Gs ( ) has a positie real ero of order one at s =, that is G ( ) = 0 and G ( ) 0 where is a positie real number. Such a transfer function can be decomposed as the following: Gs () = Gs (). () Clearly, the feedback system shown in Fig. is internally unstable if a pole of C () s (or C 2 () s ) cancels the non-minimum phase ero of Gs ( ). The following method can be used for partial cancellation of the nonminimum phase ero of Gs ( ) without leading to internal instability. In order to determine the transfer function of the fractional-order pole-ero canceller, C () s, first note that the term s / in () can be expanded using fractional powers of s in infinite many different ways as the following: s = = / / ( k )/, (2) Where theoretically can be considered equal to any positie integer. Assuming, ( k )/ Q () s ( s/ ), (3) Transfer function of the fractional-order unstable poleero canceller in Fig. can be defined as the following: C () s = = Q s ( k )/, (). (4)

(See [25] for time-domain interpretation of fractional powers of s and some real-world examples.) Note that by using the aboe definition for C () s, numerator of the series connection of C () s and Gs () (denoted as Ps () ) / will contain the term ( s / ) (instead of the term s / in the numerator of Gs ()), that is / Ps () = C () sgs () = Gs (). (5) It is proed in [8] that choosing C () s as gien in (4), and consequently, changing the non-minimum phase / term from s / to ( s / ) can highly increase the phase and gain margin and partly remoe the limitations put on the performance of the feedback system by nonminimum phase ero of the process (of course, without leading to internal instability). The only unknown parameter of the pre-compensator in Fig. is, which is larger than unity and should be determined by a simple trial and error. Theoretically, the non-minimum phase ero of Gs () can completely be cancelled by tending to infinity, which is obtained at the cost of using a more complicated setup. Howeer, the problem with applying larger alues of is that it decreases the bandwidth of the open-loop system, and consequently, increases the use of control effort. In practice, in order to design the feedback system first we assign a alue to and then design the controller C 2 () s using a desired method, and next simulate the system. If the responses were satisfactory, the job is done. Else, we should increase the alue of and repeat the procedure. In general, the controller C 2 () s in Fig. can be designed using any classical controller design algorithm. In this paper C 2 () s is considered as a PID and the effect of the fractional-order pole-ero canceller gien in (4) on time-domain responses is studied. Another important alternatie for the PID controller to be used in this system λ μ is the so-called fractional-order PID (FOPID) or PI D controller [24], which is defined as the following: 2 () ki μ,, + C s = kp + + kds λμ, kp, ki, kd. (6) λ s Note that unlike classical PID controllers, the FOPID controller gien in (6) has fie parameters to tune, which makes it a powerful tool to deal with complicated control problems. According to the aboe discussions, the feedback system shown in Fig. 2 can be used to control a nonminimum phase process with transfer function Gs (). If Gs () has more than one non-minimum phase ero, say at Fig. 2 The feedback system shown in Fig. with a special fractionalorder pre-compensator and a PID controller,, M, the transfer function of C () s in Fig. should M be considered as / Q, ( ) i s [8] (see Example 2 of i i= Section III for more details). Note that in this case nonminimum phase eros can be cancelled to dissimilar degrees, i.e., it is not necessary to subject all of the nonminimum phase eros of the process to the same amount of cancellation. This technique can also be used for partial cancellation of unstable poles of Gs ()[8], which is not discussed in this paper. The last point in relation to the proposed fractionalorder pole-ero canceller is about its realiation. It general two different methods can be used for this purpose. First, we can approximate the transfer function of C () s with an integer-order transfer function in the frequency range of interest and then realie it using classical methods. The second possible approach is to use the methods aailable for direct realiation of fractional-order systems. See [26]- [29] for more information on the latter case. III. ILLUSTRATIVE EXAMPLES Two illustratie examples are studied in this section to erify the theoretical results of preious section. The processes under consideration in both of these examples are adopted from the problems related to robotics. Since the transfer functions appear in robotics are often nonminimum phase and commonly hae oscillatory poles and eros, they are best suited to the proposed method. All of the following simulations are performed by taking the numerical inerse Laplace transform from the corresponding transfer functions. More precisely, in each case the unit step response of the feedback system is calculated by taking the numerical inerse Laplace transform from the closed-loop transfer function multiplied by / s. This method is based on the formula proposed in [30] for numerical inersion of Laplace transforms. The MATLAB code used in simulations of this paper, inlap.m, can freely be downloaded from http://www.mathworks.com/matlabcentral/fileexchange/.

Example. The following transfer function appears in the one-link flexible robot arm [3]: 2 4.906s 0.5884s+ 335.7 Gs () = 3 2 ss ( + 0.55437s + 39.6s+ 27.9). (7) 335.7 + 8.3257 = 4 3 2 s + 0.55437s + 39.6s + 27.9s The aboe transfer function has a non-minimum phase ero located at = and four poles located at p = 0, p 2 = 0.2, p3,4 = 0.772 ± j.809. Note that this system constitutes a relatiely difficult control problem since it has a non-minimum phase ero and two complex-conjugate poles with a ery low damping ratio ( ζ = 0.050 ). Assuming C () s = k, (8) equal to the series connection of C () s and C 2 () s as the following: 0.+ 0.5s Cs () = C() sc() s = 2 20 ( k )/20, () Which is almost bi-proper (the degree of numerator and denominator is equal to unity and 9/20, respectiely). Here, it should be emphasied that in general it is not necessary to use large alues of. In fact, in many cases een small alues of lead to satisfactory results. For example, Fig. 4 shows the unit step response of the closedloop system for = 2 and C 2 ( s ) = 0.05 + 0.05 s. As it is obsered in this figure, the response is satisfactory and still does not exhibit a sensible initial undershoot. Howeer, it should be remind that increasing commonly increases the control effort. Yields / 335.7 + 8.3257 Ps () =. (9) 4 3 2 s + 0.55437s + 39.6s + 27.9s Since Ps ( ) has a pole at the origin, tracking of step command without steady-state error can be achieed simply by using a PD-type controller. In order to design the PD controller, C 2 () s, first we assign a alue to and then tune the parameters of the controller assuming that the transfer function of process is equal to Ps (). Assuming = 20, after a simple trial and error the transfer function of controller is obtained as the following: Fig. 3 Unit step response of the closed-loop system shown in Fig. 2 for different alues of when the PD controller gien in (0) is applied C () s = 0. + 0.5 s. (0) 2 (Note that the low-pass filter of deriatie term is neglected for the sake of simplicity.) Fig. 3 shows the unit step response of the corresponding closed-loop system for = 5,20,25. The ery important obseration in this figure is that the step response does not exhibit a sensible initial undershoot. In fact, since Gs () (as well as the closed-loop transfer function) has odd number of nonminimum phase eros, it is expected that mere application of any PID controller leads to initial undershoot in the step response. Hence, it can be concluded that using the fractional-order pole-ero canceller has the important property of decreasing the initial undershoots. A releant discussion can be found in [8]. Note that in this example the final controller (using the nominal alue of = 20 ) is Fig. 4 Unit step response of the closed-loop system for =2 and C 2(s)=0.05+0.05s, corresponding to Example

Finally, it should be noticed that neither the step response of Fig. 3 nor of Fig. 4 are obtained using optimal controllers and better responses can be obtained in both cases. Example 2. The following transfer function is obtained by identification of a flexible-link manipulator [32]: 6 6 + + + 0 9 9 + + + 0 bs bs b Gs () = as as a, (2) Where a 9 =, a 8 = 486.7, a 7 = 6937.7, 8 a 6 = 0.66 0, 3 a 3 = 0.2624 0, 0 0 0 a 5 = 0.062 0, 4 a 2 = 0.3595 0, a =, b 6 = 4340.4953, 9 b 4 = 0.5697 0, 2 b 2 = 0.9354 0, 5 0 =0.2839 0 phase eros located at 400.0282 3 = 9.9982 a 4 = 0.667 0, 5 a = 0.42 0, b =0.4446 0, 5 b 3 = 0.908 0, 3 b = 0.699 0, b. This system has three non-minimum =, 2 = 45.005, and. Moreoer, similar to the preious example, it has poles with ery low damping ratios. Since the system itself has a pole at the origin we design a PD-type controller. In this example we subject all of the nonminimum phase eros of Gs () to the fractional-order pole-ero cancellation assuming = 5. That is, we consider C () s as the following: 7 Fig. 5 Unit step response of the closed-loop system shown in Fig. 2 for different alues of when the PD controller C 2(s)=5+2s is applied system. Second, although Gs () has an odd number of non-minimum phase eros, no considerable undershoot is obsered in the closed-loop step response, which is because of the effect of pre-compensator. The small undershoots obsered in Fig. 5 can be decreased by changing the alue of and parameters of the controller. The last point is that it is not necessary to cancel all of the non-minimum phase eros of Gs () to the same degree (here = 5 ). In fact the performance of the closed-loop system can be better adjusted by suitable choice of, 2 and 3. Where C () s = Q 3 i,5 5 i= Q i,5, (3) () s ( k )/5 =. (4) i Then after a simple trial and error the corresponding PD controller is obtained as C 2 () s = 5+ 2s. (Note that similar to the preious example, this controller is not optimal in any sense and many other controllers can be designed instead. Howeer, it is sufficient for the purpose of this example.) Fig. 5 shows the unit step response of the corresponding closed-loop system for = 4, 5, 6. Few points should be mentioned here. First, as it is obsered in Fig. 5, the closed-loop system becomes faster (of course, at the cost of increasing undershoots and using a more control effort) by decreasing the alue of. It is a general obseration that can be explained based on the relation between and bandwidth of the closed-loop REFERENCES [] K. J. Åström and R. D. Bell, Drum-boiler dynamics, Automatica, ol. 36, no. 3, pp. 363-378, 2000. [2] K. Cohen and D. E. Bossert, Fuy logic non-minimum phase autopilot design, AIAA Guidance, Naigation, and Control Conference and Exhibit, -4 August 2003, Austin, Texas, Paper 2003-5550. [3] J. Hauser, S. Sastry, and G. Meyer, Nonlinear control design for slightly non-minimum phase systems: Application to V/STOL aircraft, Automatica, ol. 28, no. 4, pp. 665-679, 992. [4] D.-S. Kwon and W. J. Book, A time-domain inerse dynamic tracking control of a single-link flexible manipulator, J. Dyn. Syst.-T. ASME, ol. 6, pp. 93-200, 994. [5] C. Kraaris and P. Daoutidis, Nonlinear state feedback control of second-order nonminimum-phase nonlinear systems, Comput. Chem. Eng., ol.4, no. 4/5, pp. 439-449, 990. [6] P. R. Gray and R. G. Meyer, Analysis and Design of Analog Integrated Circuits, 3rd ed., New York: Wiley, 993. [7] M. M. Seron, J. H. Braslasky, and G. C. Goodwin, Fundamental Limitations in Filtering and Control, New York: Springer-Verlag, 997. [8] M. M. Seron, J. H. Braslasky, P. V. Kokotoic, and D. Q. Mayne, Feedback limitations in nonlinear systems: From Bode integrals to cheap control, IEEE T. Automat. Contr., ol. 44, no. 4, pp. 829-833, April 999. [9] L. Qiu and E. J. Daison, Performance limitations of nonminimum phase systems in the seromechanism problem, Automatica, ol. 29, no. 2, pp. 337-349, 993.

[0] R. H. Middleton, Tradeoffs in linear control system design, Automatica, ol. 27, no. 2, pp. 28-292, 99. [] J. B. Hoagg and D. S. Bernstein, Nonminimum-phase eros, IEEE Contr. Syst. Mag., ol. 27, no. 3, pp. 45-57, 2007. [2] J. C. Doyle, B. A. Francis, and A. R. Tannenbaum, Feedback Control Theory, New York: Macmillan, 992. [3] S. Skogestad and I. Postlethwaite, Multiariable Feedback Control, New York: Wiley, 996. [4] T. Kailath, Linear Systems, Englewood Cliffs, NJ: Prentice-Hall, 980. [5] A. P. Aguiar, J. P. Hespanha, and P. V. Kokotoic, Pathfollowing for nonminimum phase systems remoes performance limitations, IEEE T. Automat. Contr., ol. 50, no. 2, pp. 234-239, 2005. [6] M. Fliess, H. Sira-Ramíre, and R. Marque, Regulation of nonminimum phase outputs: A flatness based approach, in Perspecties in Control- Theory and Applications: A Tribute to Ioan Doré Landau, D. Normand- Cyrot, Ed. London, U.K.: Springer-Verlag, 998, pp. 43 64. [7] S. Al-Hiddabi and N. McClamroch, Tracking and maneuer regulation control for nonlinear nonminimum phase systems: Application to flight control, IEEE T. Contr. Syst. T., ol. 0, no. 6, pp. 780-792, 2002. [8] F. Merrikh-Bayat, Fractional-order unstable pole-ero cancellation in linear feedback systems, J. Process Contr., ol. 23, no. 6, pp. 87-825, 203. [9] N. Khalili Zade Mahani, A. Khaki Sedigh, and F. Merrikh-Bayat, Performance ealuation of non-minimum phase linear control systems with fractional order partial pole-ero cancellation, the 9th Asian Control Conference (ASCC 203), June 23 26, 203, Istanbul, Turkey. [20] K. J. Åström and T. Hägglund, Adanced PID control, ISA, 2005. [2] F. Merrikh-Bayat and M. Karimi-Ghartemani, Method for designing PI λ D μ stabilisers for minimum-phase fractional-order systems, IET Control Theory A, ol. 4, no., pp. 6-70, 200. [22] S. E. Hamamci, An algorithm for stabiliation of fractional-order time delay systems using fractional-order PID controllers, IEEE T. Automat. Contr., ol. 22, no. 0, pp. 964-969, 2007. [23] C. Zhao, D. Xue, and Y.-Q. Chen, A fractional order PID tuning algorithm for a class of fractional order plants, International Conference on Mechatronics and Automation, Niagara falls, Canada, pp. 26-22, July 2005. [24] I. Podlubny, Fractional-order systems and PI λ D μ -controllers, IEEE T. Automat. Contr., ol. 44, no., pp. 208-24, 999. [25] I. Podlubny, Fractional Differential Equations, New York: Academic Press, 999. [26] J. A. T. Machado, Analysis and design of fractional-order digital control systems, J. Systems Anal.-Model.-Simulation, ol. 27, pp. 07-22, 997. [27] Y.-Q. Chen and K. L. Moore, Discretiation schemes for fractional-order differentiators and integrators, IEEE T. Circuits-I ol. 49, no. 3, pp. 363-367, 2002. [28] B. M. Vinagre, I. Podlubny, A. Hernande, and V. Feliu, Some approximations of fractional order operators used in control theory and applications, Fract. Calculus Appl. Anal., ol. 3, no. 3, pp. 23-248, 2000. [29] I. Petras, The fractional order controllers: Methods for their synthesis and application, J. Electrical Engineering, ol. 50, no. 9-0, pp. 284-288, 999. [30] J. Valsa and L. Brancik, Approximate formulae for numerical inersion of Laplace transforms, Int. J. Numer. Model El., ol., pp. 53-66, 998. [3] B.-S. Chen and T.-Y. Yang, Robust optimal model matching control design for flexible manipulators, J. Dyn. Syst.-T. ASME, ol. 5, pp. 73-78, 993. [32] M.-T. Ho and Y.-W. Tu, PID controller design for a flexible-link manipulator, Proceedings of the 44th IEEE Conference on Decision and Control, and the European Control Conference 2005, Seille, Spain, December 2-5, 2005, pp. 684-6846.