Fall 2003 BMI 226 / CS 426 AUTOMATIC SYNTHESIS OF IMPROVED TUNING RULES FOR PID CONTROLLERS

Size: px
Start display at page:

Download "Fall 2003 BMI 226 / CS 426 AUTOMATIC SYNTHESIS OF IMPROVED TUNING RULES FOR PID CONTROLLERS"

Transcription

1 Notes LL-1 AUTOMATIC SYNTHESIS OF IMPROVED TUNING RULES FOR PID CONTROLLERS

2 Notes LL-2 AUTOMATIC SYNTHESIS OF IMPROVED TUNING RULES FOR PID CONTROLLERS The PID controller was patented in 1939 by Albert Callender and Allan Stevenson of Imperial Chemical Limited of Northwich, England. The PID controller was an enormous improvement over previous manual and automatic methods for control. The quality of PID tuning rules is of considerable practical importance because a small percentage improvement in the operation of a plant can translate into large economic savings or other (e.g., environmental) benefits.

3 Notes LL-3 IMPROVED TUNING RULES CONTINUED In 1942, Ziegler and Nichols developed a set of mathematical rules for automatically selecting the parameter values associated with the proportional, integrative, and derivative blocks of a PID controller. The 1942 Ziegler-Nichols PID tuning rules do not require an analytic model of the plant. Instead, they are based on several parameters that provide a simple characterization of the to-be-controlled plant. These parameters have the practical advantage of being measurable for plants in the real world by means of relatively straightforward testing in the field. The Ziegler-Nichols rules have been in widespread use for tuning PID controllers since World War II.

4 Notes LL-4 IMPROVED TUNING RULES CONTINUED The question arises as to whether it is possible to improve upon the Ziegler-Nichols tuning rules. Åström and Hägglund answered that question in the affirmative in their 1995 book PID Controllers: Theory, Design, and Tuning in which they identified 4 families of plants that are representative for the dynamics of typical industrial processes.

5 Notes LL-5 ÅSTRÖM AND HÄGGLUND S 4 FAMILIES OF PLANTS Plants represented by transfer functions of the form -s e G( s) = (1+ st ) where T=0.1,, 10 n-lag plants G( s) 2, [A] 1 =, [B] n (1 + s) where n=3, 4, and 8 Plants represented by transfer functions of the form G( s) (1 + s)(1 + α s)(1 + α s)(1 + α s) =, [C] where α=0.2, 0.5, and 0.7 Plants represented by transfer functions of the form 1- αs G ( s) = 3, [D] (s+ 1) where α=0.1, 0.2, 0.5, 1.0, and 2.0

6 Notes LL-6 ÅSTRÖM AND HÄGGLUND S APPROACH Åström and Hägglund (1995) developed rules for automatically tuning PID controllers for the 16 plants from these 4 industrially representative families of plants. The PID tuning rules developed by Åström and Hägglund (like those of Ziegler and Nichols) are based on several parameters representing important overall characteristics of the plant that can be obtained by straightforward testing in the field. In one version of their method, Åström and Hägglund characterize a plant by two frequency-domain parameters: ultimate gain, K u (the minimum value of the gain that must be introduced into the feedback path to cause the system to oscillate) ultimate period, T u (the period of this lowest frequency oscillation)

7 Notes LL-7 ÅSTRÖM AND HÄGGLUND S APPROACH CONTINUED In another version of their method, Åström and Hägglund characterize a plant by two time-domain parameters time constant, T r dead time, L (the period before the plant output begins to respond significantly to a new reference signal). Åström and Hägglund (1995) describe a procedure for estimating these two timedomain parameters from the plant s response to a simple step input.

8 Notes LL-8 ÅSTRÖM AND HÄGGLUND S APPROACH CONTINUED Åström and Hägglund (1995) set out to develop new tuning rules to yield improved performance with respect to the multiple (often conflicting) issues associated with most practical control systems including setpoint response, disturbance rejection, sensor noise attenuation, and robustness in the face of plant model changes as expressed by the stability margin. Åström and Hägglund approached the challenge of improving on the 1942 Ziegler- Nichols tuning rules with a shrewd combination of mathematical analysis, domain-specific knowledge, rough-and-ready approximations, creative flair, and intuition sharpened over years of practical experience.

9 Notes LL-9 ÅSTRÖM AND HÄGGLUND S APPROACH CONTINUED Åström and Hägglund started by identifying industrially representative analytic plant models Next, they characterized each of the plants in their test bed in terms of parameters that are easily measured in the field. Then they applied the known analytic design technique of dominant pole design to the analytic plant models and recorded the resulting parameters for PID controllers They decided that functions of the form f(x) = + 0 * ax a x a e, where x=1/k u, were the appropriate form for the tuning rules. Finally, they fit approximating functions of the chosen form to the PID controller parameters produced by the dominant pole design technique.

10 Notes LL-10 ÅSTRÖM AND HÄGGLUND (1995) RESULT The tuning rules developed by Åström and Hägglund in their 1995 book outperform the 1942 Ziegler-Nichols tuning rules on all 16 industrially representative plants used by Åström and Hägglund. As Åström and Hägglund observe, [Our] new methods give substantial improvements in control performance while retaining much of the simplicity of the Ziegler-Nichols rules.

11 Notes LL-11 THE TOPOLOGY OF A PID CONTROLLER WITH NONZERO SETPOINT WEIGHTING OF THE REFERENCE SIGNAL IN THE PROPORTIONAL BLOCK 270 BUT NO SETPOINT WEIGHTING FOR THE DERIVATIVE BLOCK 280 Reference Signal 200 Plant Feedback Equation 1 - Equation Equation /s Control Variable Equation s

12 Notes LL-12 ÅSTRÖM AND HÄGGLUND (1995) TUNING RULES The PID tuning rules developed by Åström and Hägglund are expressed by 4 equations of the form f(x) = a + 0 * e, ax a x where x=1/k u. Equation 1 implements setpoint weighting 210 of the reference signal 200 (the setpoint) for the proportional (P) part Equation 1 specifies that the setpoint weighting, b, is given by b = * K u e K u. [1] Equation 2 specifies the gain, K p, for the proportional (P) block 230 of the controller K p = * * K u K u u K e. [2] 2

13 Notes LL-13 ÅSTRÖM AND HÄGGLUND (1995) TUNING RULES CONTINUED Equation 3 specifies the gain 250, K i, that is associated with the input to the integrative (I) block 260 K i = 0.72* K * e u 0.59* T * e u K u Ku K u Ku 2 Equation 4 specifies the gain 280, K d, that is associated with the input to the derivative (D) block 290 K d =. [3] Ku K 2 Ku K 2 u u 0.108* * * * K T e e. [4] u u

14 Notes LL-14 ÅSTRÖM AND HÄGGLUND (1995) TUNING RULES CONTINUED The transfer function for the Åström- Hägglund PID controller is K A = K ( * - ) + i p b R P ( R- P) + Kd * s* (-P), s where A is the output of the Åström- Hägglund controller, R is the reference signal, P is the plant output, and b, K p, K i, and K d are given by the four equations above Note that only P (as opposed to R P) appears in the derivative term of this transfer function because Åström and Hägglund apply a setpoint weighting of zero to the reference signal R in the derivative block.

15 Notes LL-15 IMPROVED TUNING RULES USING GP The goal here is to use genetic programming is used to discover PID tuning rules that improve upon the tuning rules developed by Åström and Hägglund in their 1995 book. The topology of the to-be-evolved controller is not open-ended here, but, instead, fixed as the PID controller topology. That is, we are not searching here for a parameterized topology

16 Notes LL-16 TEST BED OF 33 PLANTS Family Parameter value Ku Tu L Tr Runs in which the plant is used A T = A, P, 1, 2, 3 A T = A, P, 1, 2, 3 A T = A, P, 1, 2, 3 A T = A, P, 1, 2, 3 A T = P A T = P, 2, 3 A T = P A T = P A T = A, P, 1, 2, 3 B n = A, P, 1, 2, 3 B n = A, P, 1, 2, 3 B n = P, 2, 3 B n = P, 1, 2, 3 B n = P, 2, 3 B n = A, P, 1, 2, 3 B n = C α = C α = A, P, 1, 2, 3 C α = P C α = P C α = P C α = P, 2, 3 C α = P, 2, 3 C α = A, P, 1, 2, 3 C α = P, 2, 3 C α = A, P, 1, 2, 3 C α = D α = A, P, 1, 2, 3 D α = A, P, 1, 2, 3 D α = A, P, 1, 2, 3 D α = P, 2, 3 D α = A, P, 1, 2, 3 D α = A, P, 1, 2, 3

17 Notes LL-17 TEST BED OF 33 PLANTS 16 A plants used in Åström-Hägglund (1995) 30 P plants that are used to evolve the improved PID tuning rules 20 1 plants that are used to evolve the 1 st non-pid controller 24 2 / 3 plants used to evolve the 2 nd /3 rd non-pid controller

18 Notes LL ADDITIONAL PLANTS All 18 additional plants are members of Åström and Hägglund s families A, C, and D Family Parameter K u T u L T r value A A A A A A C C C C C C D D D D D D

19 Notes LL-19 PERFORMANCE OF THE ÅSTRÖM- HÄGGLUND PID CONTROLLER ON THE 33 PLANTS Plant Plant parameter value ITAE 1 ITAE 2 ITAE 3 ITAE 4 ITAE 5 ITAE 6 Stability margin A A A A A A A A A B B B B B B B C C C C C C C C C C C D D D D D D Sensor noise

20 Notes LL-20 PERFORMANCE OF THE ÅSTRÖM- HÄGGLUND PID CONTROLLER ON THE 18 ADDITIONAL PLANTS Plant Plant parameter value ITAE 1 ITAE 2 ITAE 3 ITAE 4 ITAE 5 ITAE 6 Stability margin A A A A A A C C C C C C D D D D D D Sensor noise

21 Notes LL-21 SEARCH FOR IMPROVED PID TUNING RULES The controller s topology is not subject to evolution, but instead, is prespecified to be the PID topology We are seeking four mathematical expressions (for K p, K i, K d, and b). Each of the expressions may contain free variables representing the plant s ultimate gain, K u, and the plant s ultimate period, T u. Note that there is no search for, or evolution of, the topology here. The problem is simply a search for four surfaces in threedimensional space.

22 Notes LL-22 SEARCH FOR IMPROVED PID TUNING RULES CONTINUED Initial experimentation quickly confirmed the fact that the Åström and Hägglund tuning rules are highly effective. Starting from scratch, genetic programming readily evolved threedimensional surfaces that closely match the Åström-Hägglund surfaces and that outperform the Åström-Hägglund tuning rules on average. However, these genetically evolved surfaces did not satisfy our goal, namely outperforming the Åström-Hägglund tuning rules for every plant in the test bed.

23 Notes LL-23 SEARCH FOR IMPROVED PID TUNING RULES CONTINUED Thus, we decided to approach the problem of discovering improved tuning rules by building on the known and highly effective Åström-Hägglund results. Specifically, we use genetic programming to evolve four mathematical expressions (containing the free variables K u and T u ) which, when added to the corresponding mathematical expressions developed by Åström and Hägglund, yield improved performance on every plant in the test bed. Although we anticipated that the resulting three-dimensional surfaces would be similar to the Åström-Hägglund surfaces (i.e., the magnitudes of the added numbers would be relatively small), this additive approach can, in fact, yield any surface (or, more precisely, any surface that can be represented by the generously large number of points that a single program tree may contain).

24 Notes LL-24 PREPARATORY STEPS FOR IMPROVED PID TUNING RULES PROGRAM ARCHITECTURE The architecture of each program tree in the population has four result-producing branches (one associated with each of the problem s four independent variables, namely K p, K i, K d, and b). TERMINAL SET The terminal set, T, for each of the four result-producing branches is T = {R, KU, TU}, where R denotes a perturbable numerical value between 5.0 and FUNCTION SET F = {+, -, *, %, REXP, RLOG, POW}. The two-argument POW function returns the value of its first argument to the power of the value of its second argument.

25 Notes LL-25 PREPARATORY STEPS FOR IMPROVED PID TUNING RULES CONTINUED FITNESS Fitness is measured by means of eight separate invocations of the SPICE simulator for each plant under consideration. When the aim is to automatically create a solution to a category of problems in the form of mathematical expressions containing free variable(s), the possibility of overfitting is especially salient. Overfitting occurs when an evolved solution performs well on the fitness cases that are incorporated in the fitness measure (i.e., in the training phase), but then performs poorly on previously unseen fitness cases.

26 Notes LL-26 PREPARATORY STEPS FOR IMPROVED PID TUNING RULES CONTINUED FITNESS CONTINUED In this problem, four presumptively nonlinear and complicated functions mathematical expressions (each incorporating two free variables) must be evolved. In applying genetic programming to this program, we were especially concerned about overfitting because there are only 16 plants in the test bed used by Åström and Hägglund. Moreover, there are only three plants in two of the four families. GP must usually consider a multiplicity of data points in order to discover even a linear relationship. A fortiori, a multiplicity of data points is required when the underlying function is actually nonlinear (as is usually the case in non-trivial problems).

27 Notes LL-27 PREPARATORY STEPS FOR IMPROVED PID TUNING RULES CONTINUED FITNESS CONTINUED Concerned about possible overfitting, we used the 30 plants marked P (in the table) so that the fitness measure entails 240 separate invocations of the SPICE simulator. The choice of 30 plants for this first run was governed primarily by considerations of computer time. Ideally, we would have used even more plants. We did not know in advance whether 30 plants would prove to be sufficient to enable genetic programming to unearth the complicated relationships inherent in this problem.

28 Notes LL-28 PREPARATORY STEPS FOR IMPROVED PID TUNING RULES CONTINUED CONTROL PARAMETERS The population size is 100,000

29 Notes LL-29 RESULTS IMPROVED PID TUNING RULES The best-of-run individual emerged in generation 76, so the fitness of approximately 7,700,000 individuals was evaluated during the run. The average time to evaluate the fitness of an individual (i.e., to perform the 240 SPICE simulations) was 51 seconds. It took hours (4.4 days) to produce the best-of-run individual from generation 76. The improved PID tuning rules are obtained by adding the genetically evolved adjustments below to the values of K p, K i, and K d, and b developed by Åström and Hägglund in their 1995 book.

30 Notes LL-30 RESULTS IMPROVED PID TUNING RULES CONTINUED The quantity, K p-adj, that is to be added to K p for the proportional part of the controller is K p-adj -6 = * T u *10. The quantity, K i-adj, that is to be added to K i for the integrative part is K K i-adj = * u T u The quantity, K d-adj, that is to be added to K d for the derivative part is log log K d-adj = ( ) ( K u T ) e u. The quantity, b adj, that is to be added to b for the setpoint weighting of the reference signal in the proportional block is K b adj = u K e u.

31 Notes LL-31 RESULTS IMPROVED PID TUNING RULES CONTINUED In other words, after adding, the final values (K p-final, K i-final, K d-final, and b final ) for the genetically evolved PID tuning rules are as follows: K 2 K p-final -6 = u 0.72* K * Ku u e * T u *10 K i-final = K u Ku * Ku * e K * + T K u * T * e Ku u u u K K d-final u K Ku K T = 0.108* K * * u * u ( u u Tu e e e ) K ( u ) log log K 2 b final = u 0.25* Ku K u e + K e u The authors refer to these genetically evolved PID tuning rules as the Keane-Koza- Streeter (KKS) PID tuning rules. The automatically designed controller is parameterized (i.e., general) in the sense that it contains free variables (K u and T u ) and thereby provides a solution to an entire category of problems (i.e., the control of all the plants in all the families).

32 Notes LL-32 RESULTS IMPROVED PID TUNING RULES CONTINUED Averaged over the 30 plants used in this run, the best-of-run tuning rules from generation 76 have 91.6% of the setpoint ITAE of the Åström-Hägglund tuning rules, 96.2% of the disturbance rejection ITAE of the Åström-Hägglund tuning rules, 99.5% of the reciprocal of minimum attenuation of the Åström-Hägglund tuning rules, and 98.6% of the maximum sensitivity, M s, of the Åström-Hägglund tuning rules.

33 Notes LL-33 IMPROVED PID TUNING RULES CONTINUED CROSS-VALIDATION Averaged over the 18 additional plants, the best-of-run tuning rules from generation 76 have 89.7% of the setpoint ITAE of the Åström-Hägglund tuning rules, 95.6% of the disturbance rejection ITAE of the Åström-Hägglund tuning rules, 99.5% of the reciprocal of minimum attenuation of the Åström-Hägglund tuning rules, and 98.5% of the maximum sensitivity, M s, of the Åström-Hägglund tuning rules. As can be seen, the results obtained for the 18 previously unseen additional plants are similar to those for the results for the plants used by the evolutionary process.

34 Notes LL-34 IMPROVED PID TUNING RULES CONTINUED COMPARISON TO ÅSTRÖM AND HÄGGLUND Averaged over the 16 plants used by Åström and Hägglund in their 1995 book, the best-of-run tuning rules from generation 76 have 90.5% of the setpoint ITAE of the Åström-Hägglund tuning rules, 96% of the disturbance rejection ITAE of the Åström-Hägglund tuning rules, 99.3% of the reciprocal of minimum attenuation of the Åström-Hägglund tuning rules, and 98.5% of the maximum sensitivity, M s, of the Åström-Hägglund tuning rules.

35 Notes LL-35 COMPARISON TO ÅSTRÖM- HÄGGLUND TUNING RULES THE GENETICALLY EVOLVED ADJUSTMENT, K P-ADJ, FOR THE PROPORTIONAL (P) PART The genetically evolved adjustment becomes as large as 5% only in the combination of circumstances when K u is at the low end of its range and T u is at the high end of its range.

36 Notes LL-36 COMPARISON TO ÅSTRÖM- HÄGGLUND TUNING RULES CONTINUED ADJUSTMENT, K I-ADJ, FOR THE INTEGRATIVE (I) PART BBB3862 The genetically evolved adjustment is about 5.5% for most values of K u, but drops to as little as 4% when K u is at the low end of its range.

37 Notes LL-37 COMPARISON CONTINUED ADJUSTMENT, K D-ADJ, FOR THE DERIVATIVE (D) PART As can be seen from the figure, the genetically evolved adjustment is near zero for most values of K u and T u,but becomes as large as 40% when both K u and T u are at the low ends of their ranges.

38 Notes LL-38 COMPARISON CONTINUED ADJUSTMENT, B ADJ, FOR THE SETPOINT WEIGHTING OF THE REFERENCE SIGNAL OF THE CONTROLLER S P BLOCK The genetically evolved adjustments range between 0% and about +80% and depend only on K u. It is near zero for most values of K u, but rises sharply when K u is at the low end of its range.

39 Notes LL-39

Feedback Control of Linear SISO systems. Process Dynamics and Control

Feedback Control of Linear SISO systems. Process Dynamics and Control Feedback Control of Linear SISO systems Process Dynamics and Control 1 Open-Loop Process The study of dynamics was limited to open-loop systems Observe process behavior as a result of specific input signals

More information

CHBE320 LECTURE XI CONTROLLER DESIGN AND PID CONTOLLER TUNING. Professor Dae Ryook Yang

CHBE320 LECTURE XI CONTROLLER DESIGN AND PID CONTOLLER TUNING. Professor Dae Ryook Yang CHBE320 LECTURE XI CONTROLLER DESIGN AND PID CONTOLLER TUNING Professor Dae Ryook Yang Spring 2018 Dept. of Chemical and Biological Engineering 11-1 Road Map of the Lecture XI Controller Design and PID

More information

Open Loop Tuning Rules

Open Loop Tuning Rules Open Loop Tuning Rules Based on approximate process models Process Reaction Curve: The process reaction curve is an approximate model of the process, assuming the process behaves as a first order plus

More information

A Simple PID Control Design for Systems with Time Delay

A Simple PID Control Design for Systems with Time Delay Industrial Electrical Engineering and Automation CODEN:LUTEDX/(TEIE-7266)/1-16/(2017) A Simple PID Control Design for Systems with Time Delay Mats Lilja Division of Industrial Electrical Engineering and

More information

CHAPTER 5 ROBUSTNESS ANALYSIS OF THE CONTROLLER

CHAPTER 5 ROBUSTNESS ANALYSIS OF THE CONTROLLER 114 CHAPTER 5 ROBUSTNESS ANALYSIS OF THE CONTROLLER 5.1 INTRODUCTION Robust control is a branch of control theory that explicitly deals with uncertainty in its approach to controller design. It also refers

More information

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

Design and Tuning of Fractional-order PID Controllers for Time-delayed Processes Design and Tuning of Fractional-order PID Controllers for Time-delayed Processes Emmanuel Edet Technology and Innovation Centre University of Strathclyde 99 George Street Glasgow, United Kingdom emmanuel.edet@strath.ac.uk

More information

AUTOMATIC CREATION OF A GENETIC NETWORK FOR THE lac OPERON FROM OBSERVED DATA BY MEANS OF GENETIC PROGRAMMING

AUTOMATIC CREATION OF A GENETIC NETWORK FOR THE lac OPERON FROM OBSERVED DATA BY MEANS OF GENETIC PROGRAMMING AUTOMATIC CREATION OF A GENETIC NETWORK FOR THE lac OPERON FROM OBSERVED DATA BY MEANS OF GENETIC PROGRAMMING Guido Lanza Genetic Programming Inc., Los Altos, California, guidissimo@hotmail.com William

More information

Solutions for Tutorial 10 Stability Analysis

Solutions for Tutorial 10 Stability Analysis Solutions for Tutorial 1 Stability Analysis 1.1 In this question, you will analyze the series of three isothermal CSTR s show in Figure 1.1. The model for each reactor is the same at presented in Textbook

More information

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

Lecture 5 Classical Control Overview III. Dr. Radhakant Padhi Asst. Professor Dept. of Aerospace Engineering Indian Institute of Science - Bangalore Lecture 5 Classical Control Overview III Dr. Radhakant Padhi Asst. Professor Dept. of Aerospace Engineering Indian Institute of Science - Bangalore A Fundamental Problem in Control Systems Poles of open

More information

PID control of FOPDT plants with dominant dead time based on the modulus optimum criterion

PID control of FOPDT plants with dominant dead time based on the modulus optimum criterion Archives of Control Sciences Volume 6LXII, 016 No. 1, pages 5 17 PID control of FOPDT plants with dominant dead time based on the modulus optimum criterion JAN CVEJN The modulus optimum MO criterion can

More information

Tuning Method of PI Controller with Desired Damping Coefficient for a First-order Lag Plus Deadtime System

Tuning Method of PI Controller with Desired Damping Coefficient for a First-order Lag Plus Deadtime System PID' Brescia (Italy), March 8-0, 0 FrA. Tuning Method of PI Controller with Desired Damping Coefficient for a First-order Lag Plus Deadtime System Yuji Yamakawa*. Yohei Okada** Takanori Yamazaki***. Shigeru

More information

Improved Identification and Control of 2-by-2 MIMO System using Relay Feedback

Improved Identification and Control of 2-by-2 MIMO System using Relay Feedback CEAI, Vol.17, No.4 pp. 23-32, 2015 Printed in Romania Improved Identification and Control of 2-by-2 MIMO System using Relay Feedback D.Kalpana, T.Thyagarajan, R.Thenral Department of Instrumentation Engineering,

More information

Chapter 8. Feedback Controllers. Figure 8.1 Schematic diagram for a stirred-tank blending system.

Chapter 8. Feedback Controllers. Figure 8.1 Schematic diagram for a stirred-tank blending system. Feedback Controllers Figure 8.1 Schematic diagram for a stirred-tank blending system. 1 Basic Control Modes Next we consider the three basic control modes starting with the simplest mode, proportional

More information

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

Analysis and Synthesis of Single-Input Single-Output Control Systems Lino Guzzella Analysis and Synthesis of Single-Input Single-Output Control Systems l+kja» \Uja>)W2(ja»\ um Contents 1 Definitions and Problem Formulations 1 1.1 Introduction 1 1.2 Definitions 1 1.2.1 Systems

More information

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

Additional Closed-Loop Frequency Response Material (Second edition, Chapter 14) Appendix J Additional Closed-Loop Frequency Response Material (Second edition, Chapter 4) APPENDIX CONTENTS J. Closed-Loop Behavior J.2 Bode Stability Criterion J.3 Nyquist Stability Criterion J.4 Gain

More information

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

A NEW APPROACH TO MIXED H 2 /H OPTIMAL PI/PID CONTROLLER DESIGN Copyright 2002 IFAC 15th Triennial World Congress, Barcelona, Spain A NEW APPROACH TO MIXED H 2 /H OPTIMAL PI/PID CONTROLLER DESIGN Chyi Hwang,1 Chun-Yen Hsiao Department of Chemical Engineering National

More information

CHAPTER 3 TUNING METHODS OF CONTROLLER

CHAPTER 3 TUNING METHODS OF CONTROLLER 57 CHAPTER 3 TUNING METHODS OF CONTROLLER 3.1 INTRODUCTION This chapter deals with a simple method of designing PI and PID controllers for first order plus time delay with integrator systems (FOPTDI).

More information

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

CompensatorTuning for Didturbance Rejection Associated with Delayed Double Integrating Processes, Part II: Feedback Lag-lead First-order Compensator CompensatorTuning for Didturbance Rejection Associated with Delayed Double Integrating Processes, Part II: Feedback Lag-lead First-order Compensator Galal Ali Hassaan Department of Mechanical Design &

More information

Iterative Controller Tuning Using Bode s Integrals

Iterative Controller Tuning Using Bode s Integrals Iterative Controller Tuning Using Bode s Integrals A. Karimi, D. Garcia and R. Longchamp Laboratoire d automatique, École Polytechnique Fédérale de Lausanne (EPFL), 05 Lausanne, Switzerland. email: alireza.karimi@epfl.ch

More information

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

Chapter 2. Classical Control System Design. Dutch Institute of Systems and Control Chapter 2 Classical Control System Design Overview Ch. 2. 2. Classical control system design Introduction Introduction Steady-state Steady-state errors errors Type Type k k systems systems Integral Integral

More information

K c < K u K c = K u K c > K u step 4 Calculate and implement PID parameters using the the Ziegler-Nichols tuning tables: 30

K c < K u K c = K u K c > K u step 4 Calculate and implement PID parameters using the the Ziegler-Nichols tuning tables: 30 1.5 QUANTITIVE PID TUNING METHODS Tuning PID parameters is not a trivial task in general. Various tuning methods have been proposed for dierent model descriptions and performance criteria. 1.5.1 CONTINUOUS

More information

CHAPTER 10: STABILITY &TUNING

CHAPTER 10: STABILITY &TUNING When I complete this chapter, I want to be able to do the following. Determine the stability of a process without control Determine the stability of a closed-loop feedback control system Use these approaches

More information

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

1 An Overview and Brief History of Feedback Control 1. 2 Dynamic Models 23. Contents. Preface. xiii Contents 1 An Overview and Brief History of Feedback Control 1 A Perspective on Feedback Control 1 Chapter Overview 2 1.1 A Simple Feedback System 3 1.2 A First Analysis of Feedback 6 1.3 Feedback System

More information

Vehicle longitudinal speed control

Vehicle longitudinal speed control Vehicle longitudinal speed control Prof. R.G. Longoria Department of Mechanical Engineering The University of Texas at Austin February 10, 2015 1 Introduction 2 Control concepts Open vs. Closed Loop Control

More information

ECE 388 Automatic Control

ECE 388 Automatic Control Lead Compensator and PID Control Associate Prof. Dr. of Mechatronics Engineeering Çankaya University Compulsory Course in Electronic and Communication Engineering Credits (2/2/3) Course Webpage: http://ece388.cankaya.edu.tr

More information

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

Index. INDEX_p /15/02 3:08 PM Page 765 INDEX_p.765-770 11/15/02 3:08 PM Page 765 Index N A Adaptive control, 144 Adiabatic reactors, 465 Algorithm, control, 5 All-pass factorization, 257 All-pass, frequency response, 225 Amplitude, 216 Amplitude

More information

REVERSE ENGINEERING BY MEANS OF GENETIC PROGRAMMING OF METABOLIC PATHWAYS FROM OBSERVED DATA

REVERSE ENGINEERING BY MEANS OF GENETIC PROGRAMMING OF METABOLIC PATHWAYS FROM OBSERVED DATA REVERSE ENGINEERING BY MEANS OF GENETIC PROGRAMMING OF METABOLIC PATHWAYS FROM OBSERVED DATA John R. Koza Biomedical Informatics, Department of Medicine Department of Electrical Engineering Stanford University,

More information

Ali Karimpour Associate Professor Ferdowsi University of Mashhad

Ali Karimpour Associate Professor Ferdowsi University of Mashhad CONTROL IN INSTRUMENTATION Ali Karimpour Associate Professor Ferdowsi University of Mashhad Reference: - Advanced PID Control by Karl j. Astrom and Tore Hagglund, ISA, 2006 مدلسازی و کنترل صنعتی تالیف

More information

ABB PSPG-E7 SteamTMax Precise control of main and reheat ST. ABB Group May 8, 2014 Slide 1 ABB

ABB PSPG-E7 SteamTMax Precise control of main and reheat ST. ABB Group May 8, 2014 Slide 1 ABB ABB PSPG-E7 SteamTMax Precise control of main and reheat ST May 8, 2014 Slide 1 Challenge m S m att T in T out Live steam and reheated steam temperatures are controlled process variables critical in steam

More information

Index Accumulation, 53 Accuracy: numerical integration, sensor, 383, Adaptive tuning: expert system, 528 gain scheduling, 518, 529, 709,

Index Accumulation, 53 Accuracy: numerical integration, sensor, 383, Adaptive tuning: expert system, 528 gain scheduling, 518, 529, 709, Accumulation, 53 Accuracy: numerical integration, 83-84 sensor, 383, 772-773 Adaptive tuning: expert system, 528 gain scheduling, 518, 529, 709, 715 input conversion, 519 reasons for, 512-517 relay auto-tuning,

More information

Improved Model Reduction and Tuning of Fractional Order PI λ D μ Controllers for Analytical Rule Extraction with Genetic Programming

Improved Model Reduction and Tuning of Fractional Order PI λ D μ Controllers for Analytical Rule Extraction with Genetic Programming 1 Improved Model Reduction and Tuning of Fractional Order PI λ D μ Controllers for Analytical Rule Extraction with Genetic Programg Saptarshi Das a,b, Indranil Pan b, Shantanu Das c and Amitava Gupta a,b

More information

Professional Portfolio Selection Techniques: From Markowitz to Innovative Engineering

Professional Portfolio Selection Techniques: From Markowitz to Innovative Engineering Massachusetts Institute of Technology Sponsor: Electrical Engineering and Computer Science Cosponsor: Science Engineering and Business Club Professional Portfolio Selection Techniques: From Markowitz to

More information

Improved cascade control structure for enhanced performance

Improved cascade control structure for enhanced performance Improved cascade control structure for enhanced performance Article (Unspecified) Kaya, İbrahim, Tan, Nusret and Atherton, Derek P. (7) Improved cascade control structure for enhanced performance. Journal

More information

Control Systems. EC / EE / IN. For

Control Systems.   EC / EE / IN. For Control Systems For EC / EE / IN By www.thegateacademy.com Syllabus Syllabus for Control Systems Basic Control System Components; Block Diagrammatic Description, Reduction of Block Diagrams. Open Loop

More information

Review: stability; Routh Hurwitz criterion Today s topic: basic properties and benefits of feedback control

Review: stability; Routh Hurwitz criterion Today s topic: basic properties and benefits of feedback control Plan of the Lecture Review: stability; Routh Hurwitz criterion Today s topic: basic properties and benefits of feedback control Goal: understand the difference between open-loop and closed-loop (feedback)

More information

Analyzing Control Problems and Improving Control Loop Performance

Analyzing Control Problems and Improving Control Loop Performance OptiControls Inc. Houston, TX Ph: 713-459-6291 www.opticontrols.com info@opticontrols.com Analyzing Control s and Improving Control Loop Performance -by Jacques F. Smuts Page: 1 Presenter Principal Consultant

More information

A Comparative Study on Automatic Flight Control for small UAV

A Comparative Study on Automatic Flight Control for small UAV Proceedings of the 5 th International Conference of Control, Dynamic Systems, and Robotics (CDSR'18) Niagara Falls, Canada June 7 9, 18 Paper No. 13 DOI: 1.11159/cdsr18.13 A Comparative Study on Automatic

More information

An Adaptive LQG Combined With the MRAS Based LFFC for Motion Control Systems

An Adaptive LQG Combined With the MRAS Based LFFC for Motion Control Systems Journal of Automation Control Engineering Vol 3 No 2 April 2015 An Adaptive LQG Combined With the MRAS Based LFFC for Motion Control Systems Nguyen Duy Cuong Nguyen Van Lanh Gia Thi Dinh Electronics Faculty

More information

Linear-Quadratic Optimal Control: Full-State Feedback

Linear-Quadratic Optimal Control: Full-State Feedback Chapter 4 Linear-Quadratic Optimal Control: Full-State Feedback 1 Linear quadratic optimization is a basic method for designing controllers for linear (and often nonlinear) dynamical systems and is actually

More information

Chapter 2 Review of Linear and Nonlinear Controller Designs

Chapter 2 Review of Linear and Nonlinear Controller Designs Chapter 2 Review of Linear and Nonlinear Controller Designs This Chapter reviews several flight controller designs for unmanned rotorcraft. 1 Flight control systems have been proposed and tested on a wide

More information

Part II. Advanced PID Design Methods

Part II. Advanced PID Design Methods Part II Advanced PID Design Methods 54 Controller transfer function C(s) = k p (1 + 1 T i s + T d s) (71) Many extensions known to the basic design methods introduced in RT I. Four advanced approaches

More information

CONTROL MODE SETTINGS. The quality of control obtained from a particular system depends largely on the adj ustments made to the various mode

CONTROL MODE SETTINGS. The quality of control obtained from a particular system depends largely on the adj ustments made to the various mode Instrumentation & Control - Course 136 CONTROL MODE SETTINGS The quality of control obtained from a particular system depends largely on the adj ustments made to the various mode settings. Many control

More information

Dr Ian R. Manchester

Dr Ian R. Manchester Week Content Notes 1 Introduction 2 Frequency Domain Modelling 3 Transient Performance and the s-plane 4 Block Diagrams 5 Feedback System Characteristics Assign 1 Due 6 Root Locus 7 Root Locus 2 Assign

More information

Plan of the Lecture. Review: stability; Routh Hurwitz criterion Today s topic: basic properties and benefits of feedback control

Plan of the Lecture. Review: stability; Routh Hurwitz criterion Today s topic: basic properties and benefits of feedback control Plan of the Lecture Review: stability; Routh Hurwitz criterion Today s topic: basic properties and benefits of feedback control Plan of the Lecture Review: stability; Routh Hurwitz criterion Today s topic:

More information

CHAPTER 7 MODELING AND CONTROL OF SPHERICAL TANK LEVEL PROCESS 7.1 INTRODUCTION

CHAPTER 7 MODELING AND CONTROL OF SPHERICAL TANK LEVEL PROCESS 7.1 INTRODUCTION 141 CHAPTER 7 MODELING AND CONTROL OF SPHERICAL TANK LEVEL PROCESS 7.1 INTRODUCTION In most of the industrial processes like a water treatment plant, paper making industries, petrochemical industries,

More information

Robust QFT-based PI controller for a feedforward control scheme

Robust QFT-based PI controller for a feedforward control scheme Integral-Derivative Control, Ghent, Belgium, May 9-11, 218 ThAT4.4 Robust QFT-based PI controller for a feedforward control scheme Ángeles Hoyo José Carlos Moreno José Luis Guzmán Tore Hägglund Dep. of

More information

Improved Autotuning Using the Shape Factor from Relay Feedback

Improved Autotuning Using the Shape Factor from Relay Feedback Article Subscriber access provided by NATIONAL TAIWAN UNIV Improved Autotuning Using the Shape Factor from Relay Feedback T. Thyagarajan, and Cheng-Ching Yu Ind. Eng. Chem. Res., 2003, 42 (20), 4425-4440

More information

Tuning and robustness analysis of event-based PID controllers under different event generation strategies

Tuning and robustness analysis of event-based PID controllers under different event generation strategies Tuning and robustness analysis of event-based PID controllers under different event generation strategies Julio Ariel Romero Pérez and Roberto Sanchis Llopis Departament of Industrial Systems Engineering

More information

ECEN 667 Power System Stability Lecture 15: PIDs, Governors, Transient Stability Solutions

ECEN 667 Power System Stability Lecture 15: PIDs, Governors, Transient Stability Solutions ECEN 667 Power System Stability Lecture 15: PIDs, Governors, Transient Stability Solutions Prof. Tom Overbye Dept. of Electrical and Computer Engineering Texas A&M University, overbye@tamu.edu 1 Announcements

More information

Cascade Control of a Continuous Stirred Tank Reactor (CSTR)

Cascade Control of a Continuous Stirred Tank Reactor (CSTR) Journal of Applied and Industrial Sciences, 213, 1 (4): 16-23, ISSN: 2328-4595 (PRINT), ISSN: 2328-469 (ONLINE) Research Article Cascade Control of a Continuous Stirred Tank Reactor (CSTR) 16 A. O. Ahmed

More information

Control System Design

Control System Design ELEC ENG 4CL4: Control System Design Notes for Lecture #24 Wednesday, March 10, 2004 Dr. Ian C. Bruce Room: CRL-229 Phone ext.: 26984 Email: ibruce@mail.ece.mcmaster.ca Remedies We next turn to the question

More information

Tuning of Internal Model Control Proportional Integral Derivative Controller for Optimized Control

Tuning of Internal Model Control Proportional Integral Derivative Controller for Optimized Control Tuning of Internal Model Control Proportional Integral Derivative Controller for Optimized Control Thesis submitted in partial fulfilment of the requirement for the award of Degree of MASTER OF ENGINEERING

More information

Robust Loop Shaping Controller Design for Spectral Models by Quadratic Programming

Robust Loop Shaping Controller Design for Spectral Models by Quadratic Programming Robust Loop Shaping Controller Design for Spectral Models by Quadratic Programming Gorka Galdos, Alireza Karimi and Roland Longchamp Abstract A quadratic programming approach is proposed to tune fixed-order

More information

Control Systems Lab - SC4070 Control techniques

Control Systems Lab - SC4070 Control techniques Control Systems Lab - SC4070 Control techniques Dr. Manuel Mazo Jr. Delft Center for Systems and Control (TU Delft) m.mazo@tudelft.nl Tel.:015-2788131 TU Delft, February 16, 2015 (slides modified from

More information

CHAPTER 6 CLOSED LOOP STUDIES

CHAPTER 6 CLOSED LOOP STUDIES 180 CHAPTER 6 CLOSED LOOP STUDIES Improvement of closed-loop performance needs proper tuning of controller parameters that requires process model structure and the estimation of respective parameters which

More information

An Improved Relay Auto Tuning of PID Controllers for SOPTD Systems

An Improved Relay Auto Tuning of PID Controllers for SOPTD Systems Proceedings of the World Congress on Engineering and Computer Science 7 WCECS 7, October 4-6, 7, San Francisco, USA An Improved Relay Auto Tuning of PID Controllers for SOPTD Systems Sathe Vivek and M.

More information

An improved auto-tuning scheme for PI controllers

An improved auto-tuning scheme for PI controllers ISA Transactions 47 (2008) 45 52 www.elsevier.com/locate/isatrans An improved auto-tuning scheme for PI controllers Rajani K. Mudi a,, Chanchal Dey b, Tsu-Tian Lee c a Department of Instrumentation and

More information

Anisochronic First Order Model and Its Application to Internal Model Control

Anisochronic First Order Model and Its Application to Internal Model Control Anisochronic First Order Model and Its Application to Internal Model Control Vyhlídal, Tomáš Ing., Czech Technical University, Inst. of Instrumentation and Control Eng., Technická 4, Praha 6, 66 7, vyhlidal@student.fsid.cvut.cz

More information

A Method for PID Controller Tuning Using Nonlinear Control Techniques*

A Method for PID Controller Tuning Using Nonlinear Control Techniques* A Method for PID Controller Tuning Using Nonlinear Control Techniques* Prashant Mhaskar, Nael H. El-Farra and Panagiotis D. Christofides Department of Chemical Engineering University of California, Los

More information

MULTILOOP PI CONTROLLER FOR ACHIEVING SIMULTANEOUS TIME AND FREQUENCY DOMAIN SPECIFICATIONS

MULTILOOP PI CONTROLLER FOR ACHIEVING SIMULTANEOUS TIME AND FREQUENCY DOMAIN SPECIFICATIONS Journal of Engineering Science and Technology Vol. 1, No. 8 (215) 113-1115 School of Engineering, Taylor s University MULTILOOP PI CONTROLLER FOR ACHIEVING SIMULTANEOUS TIME AND FREQUENCY DOMAIN SPECIFICATIONS

More information

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

Design of Decentralised PI Controller using Model Reference Adaptive Control for Quadruple Tank Process Design of Decentralised PI Controller using Model Reference Adaptive Control for Quadruple Tank Process D.Angeline Vijula #, Dr.N.Devarajan * # Electronics and Instrumentation Engineering Sri Ramakrishna

More information

The Basic Feedback Loop. Design and Diagnosis. of the Basic Feedback Loop. Parallel form. The PID Controller. Tore Hägglund. The textbook version:

The Basic Feedback Loop. Design and Diagnosis. of the Basic Feedback Loop. Parallel form. The PID Controller. Tore Hägglund. The textbook version: The Basic Feedback Loop Design and Diagnosis l n of the Basic Feedback Loop sp Σ e x Controller Σ Process Σ Tore Hägglnd Department of Atomatic Control Lnd Institte of Technolog Lnd, Sweden The PID Controller

More information

TRACKING TIME ADJUSTMENT IN BACK CALCULATION ANTI-WINDUP SCHEME

TRACKING TIME ADJUSTMENT IN BACK CALCULATION ANTI-WINDUP SCHEME TRACKING TIME ADJUSTMENT IN BACK CALCULATION ANTI-WINDUP SCHEME Hayk Markaroglu Mujde Guzelkaya Ibrahim Eksin Engin Yesil Istanbul Technical University, Faculty of Electrical and Electronics Engineering,

More information

Topic # Feedback Control Systems

Topic # Feedback Control Systems Topic #19 16.31 Feedback Control Systems Stengel Chapter 6 Question: how well do the large gain and phase margins discussed for LQR map over to DOFB using LQR and LQE (called LQG)? Fall 2010 16.30/31 19

More information

Tuning of PID Controllers Based on Sensitivity Margin Specification

Tuning of PID Controllers Based on Sensitivity Margin Specification Tuning of D Controllers ased on Sensitivity Margin Specification S. Dormido and F. Morilla Dpto. de nformática y Automática-UNED c/ Juan del Rosal 6, 84 Madrid, Spain e-mail: {sdormido,fmorilla}@dia.uned.es

More information

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

Model-based PID tuning for high-order processes: when to approximate Proceedings of the 44th IEEE Conference on Decision and Control, and the European Control Conference 25 Seville, Spain, December 2-5, 25 ThB5. Model-based PID tuning for high-order processes: when to approximate

More information

for the Heating and Cooling Coil in Buildings

for the Heating and Cooling Coil in Buildings An On-line Self-tuning Algorithm of P Controller for the Heating and Cooling Coil in Buildings Q. Zhou and M. Liu Energy Systems Laboratory Texas Engineering Experiment Station ABSTRACT An on-line self-tuning

More information

Transient Stability Analysis with PowerWorld Simulator

Transient Stability Analysis with PowerWorld Simulator Transient Stability Analysis with PowerWorld Simulator T1: Transient Stability Overview, Models and Relationships 2001 South First Street Champaign, Illinois 61820 +1 (217) 384.6330 support@powerworld.com

More information

TUNING-RULES FOR FRACTIONAL PID CONTROLLERS

TUNING-RULES FOR FRACTIONAL PID CONTROLLERS TUNING-RULES FOR FRACTIONAL PID CONTROLLERS Duarte Valério, José Sá da Costa Technical Univ. of Lisbon Instituto Superior Técnico Department of Mechanical Engineering GCAR Av. Rovisco Pais, 49- Lisboa,

More information

EE3CL4: Introduction to Linear Control Systems

EE3CL4: Introduction to Linear Control Systems 1 / 17 EE3CL4: Introduction to Linear Control Systems Section 7: McMaster University Winter 2018 2 / 17 Outline 1 4 / 17 Cascade compensation Throughout this lecture we consider the case of H(s) = 1. We

More information

4.0 Update Algorithms For Linear Closed-Loop Systems

4.0 Update Algorithms For Linear Closed-Loop Systems 4. Update Algorithms For Linear Closed-Loop Systems A controller design methodology has been developed that combines an adaptive finite impulse response (FIR) filter with feedback. FIR filters are used

More information

Introduction to. Process Control. Ahmet Palazoglu. Second Edition. Jose A. Romagnoli. CRC Press. Taylor & Francis Group. Taylor & Francis Group,

Introduction to. Process Control. Ahmet Palazoglu. Second Edition. Jose A. Romagnoli. CRC Press. Taylor & Francis Group. Taylor & Francis Group, Introduction to Process Control Second Edition Jose A. Romagnoli Ahmet Palazoglu CRC Press Taylor & Francis Group Boca Raton London NewYork CRC Press is an imprint of the Taylor & Francis Group, an informa

More information

Koza s Algorithm. Choose a set of possible functions and terminals for the program.

Koza s Algorithm. Choose a set of possible functions and terminals for the program. Step 1 Koza s Algorithm Choose a set of possible functions and terminals for the program. You don t know ahead of time which functions and terminals will be needed. User needs to make intelligent choices

More information

H-Infinity Controller Design for a Continuous Stirred Tank Reactor

H-Infinity Controller Design for a Continuous Stirred Tank Reactor International Journal of Electronic and Electrical Engineering. ISSN 974-2174 Volume 7, Number 8 (214), pp. 767-772 International Research Publication House http://www.irphouse.com H-Infinity Controller

More information

Introduction to control theory

Introduction to control theory Introduction to control theory Reference These slides are freely adapted from the book Embedded Systems design - A unified Hardware/Software introduction, Frank Vahid, Tony Givargis Some figures are excerpt

More information

Desired Bode plot shape

Desired Bode plot shape Desired Bode plot shape 0dB Want high gain Use PI or lag control Low freq ess, type High low freq gain for steady state tracking Low high freq gain for noise attenuation Sufficient PM near ω gc for stability

More information

Feedback Control of Dynamic Systems

Feedback Control of Dynamic Systems THIRD EDITION Feedback Control of Dynamic Systems Gene F. Franklin Stanford University J. David Powell Stanford University Abbas Emami-Naeini Integrated Systems, Inc. TT Addison-Wesley Publishing Company

More information

Principles and Practice of Automatic Process Control

Principles and Practice of Automatic Process Control Principles and Practice of Automatic Process Control Third Edition Carlos A. Smith, Ph.D., P.E. Department of Chemical Engineering University of South Florida Armando B. Corripio, Ph.D., P.E. Gordon A.

More information

MULTIVARIABLE PROPORTIONAL-INTEGRAL-PLUS (PIP) CONTROL OF THE ALSTOM NONLINEAR GASIFIER MODEL

MULTIVARIABLE PROPORTIONAL-INTEGRAL-PLUS (PIP) CONTROL OF THE ALSTOM NONLINEAR GASIFIER MODEL Control 24, University of Bath, UK, September 24 MULTIVARIABLE PROPORTIONAL-INTEGRAL-PLUS (PIP) CONTROL OF THE ALSTOM NONLINEAR GASIFIER MODEL C. J. Taylor, E. M. Shaban Engineering Department, Lancaster

More information

Controlling the Inverted Pendulum

Controlling the Inverted Pendulum Controlling the Inverted Pendulum Steven A. P. Quintero Department of Electrical and Computer Engineering University of California, Santa Barbara Email: squintero@umail.ucsb.edu Abstract The strategies

More information

D(s) G(s) A control system design definition

D(s) G(s) A control system design definition R E Compensation D(s) U Plant G(s) Y Figure 7. A control system design definition x x x 2 x 2 U 2 s s 7 2 Y Figure 7.2 A block diagram representing Eq. (7.) in control form z U 2 s z Y 4 z 2 s z 2 3 Figure

More information

ME 475/591 Control Systems Final Exam Fall '99

ME 475/591 Control Systems Final Exam Fall '99 ME 475/591 Control Systems Final Exam Fall '99 Closed book closed notes portion of exam. Answer 5 of the 6 questions below (20 points total) 1) What is a phase margin? Under ideal circumstances, what does

More information

ADAPTIVE PID CONTROLLER WITH ON LINE IDENTIFICATION

ADAPTIVE PID CONTROLLER WITH ON LINE IDENTIFICATION Journal of ELECTRICAL ENGINEERING, VOL. 53, NO. 9-10, 00, 33 40 ADAPTIVE PID CONTROLLER WITH ON LINE IDENTIFICATION Jiří Macháče Vladimír Bobál A digital adaptive PID controller algorithm which contains

More information

Active Guidance for a Finless Rocket using Neuroevolution

Active Guidance for a Finless Rocket using Neuroevolution Active Guidance for a Finless Rocket using Neuroevolution Gomez, F.J. & Miikulainen, R. (2003). Genetic and Evolutionary Computation Gecco, 2724, 2084 2095. Introduction Sounding rockets are used for making

More information

Automatic Control (TSRT15): Lecture 7

Automatic Control (TSRT15): Lecture 7 Automatic Control (TSRT15): Lecture 7 Tianshi Chen Division of Automatic Control Dept. of Electrical Engineering Email: tschen@isy.liu.se Phone: 13-282226 Office: B-house extrance 25-27 Outline 2 Feedforward

More information

Competences. The smart choice of Fluid Control Systems

Competences. The smart choice of Fluid Control Systems Competences The smart choice of Fluid Control Systems Contents 1. Open-loop and closed-loop control Page 4 1.1. Function and sequence of an open-loop control system Page 4 1.2. Function and sequence of

More information

Control Systems Design

Control Systems Design ELEC4410 Control Systems Design Lecture 3, Part 2: Introduction to Affine Parametrisation School of Electrical Engineering and Computer Science Lecture 3, Part 2: Affine Parametrisation p. 1/29 Outline

More information

Controls Problems for Qualifying Exam - Spring 2014

Controls Problems for Qualifying Exam - Spring 2014 Controls Problems for Qualifying Exam - Spring 2014 Problem 1 Consider the system block diagram given in Figure 1. Find the overall transfer function T(s) = C(s)/R(s). Note that this transfer function

More information

magnitude [db] phase [deg] frequency [Hz] feedforward motor load -

magnitude [db] phase [deg] frequency [Hz] feedforward motor load - ITERATIVE LEARNING CONTROL OF INDUSTRIAL MOTION SYSTEMS Maarten Steinbuch and René van de Molengraft Eindhoven University of Technology, Faculty of Mechanical Engineering, Systems and Control Group, P.O.

More information

ISA Transactions ( ) Contents lists available at ScienceDirect. ISA Transactions. journal homepage:

ISA Transactions ( ) Contents lists available at ScienceDirect. ISA Transactions. journal homepage: ISA Transactions ( ) Contents lists available at ScienceDirect ISA Transactions journal homepage: www.elsevier.com/locate/isatrans An improved auto-tuning scheme for PID controllers Chanchal Dey a, Rajani

More information

Video 5.1 Vijay Kumar and Ani Hsieh

Video 5.1 Vijay Kumar and Ani Hsieh Video 5.1 Vijay Kumar and Ani Hsieh Robo3x-1.1 1 The Purpose of Control Input/Stimulus/ Disturbance System or Plant Output/ Response Understand the Black Box Evaluate the Performance Change the Behavior

More information

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

A FEEDBACK STRUCTURE WITH HIGHER ORDER DERIVATIVES IN REGULATOR. Ryszard Gessing A FEEDBACK STRUCTURE WITH HIGHER ORDER DERIVATIVES IN REGULATOR Ryszard Gessing Politechnika Śl aska Instytut Automatyki, ul. Akademicka 16, 44-101 Gliwice, Poland, fax: +4832 372127, email: gessing@ia.gliwice.edu.pl

More information

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

IMC based automatic tuning method for PID controllers in a Smith predictor configuration Computers and Chemical Engineering 28 (2004) 281 290 IMC based automatic tuning method for PID controllers in a Smith predictor configuration Ibrahim Kaya Department of Electrical and Electronics Engineering,

More information

Control System Design

Control System Design ELEC ENG 4CL4: Control System Design Notes for Lecture #36 Dr. Ian C. Bruce Room: CRL-229 Phone ext.: 26984 Email: ibruce@mail.ece.mcmaster.ca Friday, April 4, 2003 3. Cascade Control Next we turn to an

More information

Observer Based Friction Cancellation in Mechanical Systems

Observer Based Friction Cancellation in Mechanical Systems 2014 14th International Conference on Control, Automation and Systems (ICCAS 2014) Oct. 22 25, 2014 in KINTEX, Gyeonggi-do, Korea Observer Based Friction Cancellation in Mechanical Systems Caner Odabaş

More information

Robust and Optimal Control, Spring A: SISO Feedback Control A.1 Internal Stability and Youla Parameterization

Robust and Optimal Control, Spring A: SISO Feedback Control A.1 Internal Stability and Youla Parameterization Robust and Optimal Control, Spring 2015 Instructor: Prof. Masayuki Fujita (S5-303B) A: SISO Feedback Control A.1 Internal Stability and Youla Parameterization A.2 Sensitivity and Feedback Performance A.3

More information

Determination of Dynamic Model of Natural Gas Cooler in CPS Molve III Using Computer

Determination of Dynamic Model of Natural Gas Cooler in CPS Molve III Using Computer Determination of Dynamic Model of Natural Gas Cooler in CPS Molve III Using Computer Petar Crnošija, Toni Bjažić, Fetah Kolonić Faculty of Electrical Engineering and Computing Unska 3, HR- Zagreb, Croatia

More information

Control Systems I. Lecture 2: Modeling. Suggested Readings: Åström & Murray Ch. 2-3, Guzzella Ch Emilio Frazzoli

Control Systems I. Lecture 2: Modeling. Suggested Readings: Åström & Murray Ch. 2-3, Guzzella Ch Emilio Frazzoli Control Systems I Lecture 2: Modeling Suggested Readings: Åström & Murray Ch. 2-3, Guzzella Ch. 2-3 Emilio Frazzoli Institute for Dynamic Systems and Control D-MAVT ETH Zürich September 29, 2017 E. Frazzoli

More information

Practical work: Active control of vibrations of a ski mock-up with a piezoelectric actuator

Practical work: Active control of vibrations of a ski mock-up with a piezoelectric actuator Jean Luc Dion Gaël Chevallier SUPMECA Paris (Mechanical Engineering School) Practical work: Active control of vibrations of a ski mock-up with a piezoelectric actuator THIS WORK HAS OBTAINED THE FIRST

More information

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

A unified double-loop multi-scale control strategy for NMP integrating-unstable systems Home Search Collections Journals About Contact us My IOPscience A unified double-loop multi-scale control strategy for NMP integrating-unstable systems This content has been downloaded from IOPscience.

More information