Introduction to Robust Control Dr Abraham T Mathew What is a Control System? Is it the physical system? Is it the mathematical system? ENVIRONMENT SYSTEM BOUNDARY INPUT INPUT CONTROL SYSTEM OUTPUT INPUT SUCCESS IN CONTROL DESIGN IS SAID TO BE BASED ON THE SUCCESS IN IDENTIFYING THE SYSTEM BOUNDARY, INPUTS,OUTPUTS & THE ENVIRONMENT Model Based Control Design- Issues Analytical or computational models cannot truly characterize and emulate the phenomenon. A model, no matter how detailed, is never a completely accurate representation of a real physical system Control Design-classical way Normally, in the conventional control design for SISO system, the stability margin is specified to ensure stability in the presence of model uncertainties But, the uncertainties or perturbations are not quantified, nor performance was not taken into account in terms of disturbance, noise etc. For MIMO systems, many of the SISO methods cannot be scaled up Robust Control Design a controller such that some level of performance of the controlled system is guaranteed irrespective of the changes in the plant dynamics/process dynamics within a predefined class and the stability is guaranteed Control design targets Stability Disturbance rejection Sensor(measurement) noise rejection Avoidance of actuator saturation Robustness- the process/plant performance should not deteriorate to unacceptable level if there occurs the changes due to the uncertainties All these targets cannot be achieved simultaneously and perfectly. So there has to be some compromise or tradeoffs, because of various reasons Modeling in the context of robust control We consider a simple example !! Modeling a DC Servo We consider a DC servo mechanism consisting of a DC motor, gear train, and the load shaft It is required to control the angular displacement and speed using a voltage signal applied across the armature Motor Load Linear Model of the DC Servo-Physical Equations of dynamics 0 0 L i 0 1 0 NK m La 0 0 0 1 NK m 0 v(t ) TL 1 Je Je Ra i L 0 a La 1 0 0 0 1 0 i TF FORM (s) NK m J e La a0 2 2 2 v( s ) 2 Ra N K m s s b1s b2 s s s La J e La Nominal Model Km=0.05 Nm/A, Ra=1.2 ohms, La=0.05H Jm=8x10-4 kgm2 , J=0.020 kgm2 N=12 Je=J+N2Jm=0.1352 kgm2 Uncertainty Let the parameters are subject to changes as follows 0.04≤Km ≤0.06 6x10-4 ≤Jm ≤ 10-3 0.01≤J ≤0.05 Model with Uncertainty (as an Interval System) [74.22, 99.58] G( s) 2 s s 12s [47.8, 53.4] Abstracting a Control System Structure Control System Structure Disturbance w(t) wm Noise v(t) Sensor S1 Input yd Controller C u Plant/Process P y Sensor S Output ym System Equations If the Plant is LTI the zero state linearity dictates that y is a linear combination of effects of the two plant inputs u and w That is y(s) P(s)u(s) P (s)w(s) (1) Quite often it is convenient to work with the disturbance d(s) at the plant output given as w d (s) P (s)w(s) Then, we have w y(s) P(s)u(s) d (s) (2) (3) System Equations Sensor is assumed to have two inputs, plant output y and the measurement noise v. So, we have y ( s ) P ( s ) y ( s ) v( s ) Ideally Ps(s)=1 and v(t)=0 so that ym=y m s (4) (this is achieved if sensor bandwidth is larger than system bandwidth or we say the sensor is fast and accurate) Now, look at the Controller Disturbance w(t) wm Noise v(t) Sensor S1 yd Controller C u Plant/Process P y Sensor S ym Contd… Controller gets three inputs ym, yd and wm Here wm is the disturbance measured using suitable sensor Let the controller be LTI. Then s) all Fdthe (s) ythree ( s) Fm (s)need ym (sto ) be Fwused (s)wmalways (s) here. Several (5) d u(Not inputs control structures are defined according to whether ym, yd or wm is used to produce u or not . Accordingly we will have different schemes of control 1. Single Degree of Freedom controller When Fm=-Fd and Fw=0, we have u(s) F ( s)[ y ( s) y (s)] d d m The figure shows 1DoF Control Structure realizing this equation yd + ym Fd u Two Degree of Freedom Controller If we have a structure of the form given below, designer will have freedom to independently select Fm and Fd we will have the TDoF Feedback Controller structure yd Fd + + u Fm ym Feedback Control Scheme v w Fw Pw yd Fd + + d u P + + Fm + y Ps + + ym Problem formulation System enclosed in the dotted box is seen to have three inputs and one output By assuming linearity, we can say that plant output y(t) is produced as a superposition of the effects of these three signals coming to the output port through three transfer channels That is y(s) H (s) y (s) H (s)w(s) H (s)v(s) d d w v Tracking problem Let the error e(t) be defined as e(t)=yd-y That is, e( s) y ( s ) H ( s) y ( s ) H ( s) w( s) H ( s )v( s) d d d w v Or e( s) 1 H ( s)y ( s) H ( s) w( s ) H ( s )v( s) d d w v The central design problem is to obtain Hd, Hw, and Hv with desirable properties using appropriate methods or criteria Look at it again v w Fw Pw yd Fd + + d u P + + Fm + y Ps + + ym Emphasis for output disturbance In cases where it is desirable or convenient to work with the output disturbance d rather than w, we have y(s) H (s) y (s) H (s)d (s) H (s)v(s) d d wd v e( s ) y ( s ) H ( s ) y ( s ) H ( s ) d ( s ) H ( s ) v ( s ) d d d wd v Or e( s) 1 H ( s)y ( s ) H ( s)d ( s ) H ( s)v( s) d d wd v Tracking performance For the system to ideally track the reference, the error must be zero To achieve this for all possible yd,v,w and d, we would require Hd(s)=1 and Hw(s)= Hwd(s)=Hv(s)=0 In the practical setting, as we see more in detail, we can see that this condition cannot be satisfied perfectly for the entire bandwidth or entire region of system perturbations Some design tradeoffs, optimality conditions and so on would have to be called for as we have already noted. Admissible/acceptable designs In order to do the adjustment/tradeoff for obtaining an admissible or acceptable design and discriminate between acceptable and unacceptable departures from the ideal performance, we need to have the specifications These specifications give rise to different control structures like open loop, feedforward, feedback, etc. We may differentiate between SISO and MIMO and start with SISO and generalize the notations for MIMO, subsequently Control System Performance From a system’s perspective, the performance specification for control system starts with “Stability” Followed by Sensitivity, Disturbance Rejection, Noise Rejection etc. where needed. Stability When it comes to stability, in the modern settings of design, we consider two classes of stability, namely Input-output stability Internal stability Internal stability is of paramount importance in the MIMO system framework, both in Matrix Transfer function form and State variable/transfer function forms Internal Stability A system to be internally stable means all the transfer functions associated with all the transfer channels connecting exogenous input to the output(including set point, disturbance & noise) shall be stable In reality, it is possible for a system to be internally unstable and yet to have a stable “set point to output” channel transfer functions Under this circumstance, we say that system has unstable hidden modes Therefore, internal stability must be ensured before the transfer function that define the response to the system inputs are considered Design Model be a set of all plants that each member of set P is an admissible model, given the uncertainty region (interval) Let P P0 in P is one model with the nominal value of the parameters If P0 is used for the robust designs, then let us call P0 as Design model (for the sake of convenience!!) Model Uncertainty & Internal stability If the plant is expected to deviate from the design model(nominal model), it is better represented by a set of models centered on the design model(nominal model) For a control system to be acceptable, the design must be internally stable for every model in the set This property is known as robust stability Once stability & robustness are assured, we can shift the attention to “response” Summary A model of the physical system is only an approximation of the real phenomenon/process Control system output is the measurement showing the status or effectiveness of control Inputs, in a general framework will include set point, disturbance and measurement noise Summary contd… Models are subjected to various uncertainties Nominal model in the set of uncertain models can be used as Design model Internal Stability and robust stability are starting points for good control system design Once stability is assured, other performance measures can be specified Design Dilemma It will not usually be possible(which we will see in detail) to have good set point tracking, and disturbance rejection and noise rejection uniformly effectively for all functions of yd, v, w and d Also, emphasis on sensitivity on one may negatively affect the other Robust Control System A system is said to be robust when It is durable, hardy and resilient It has low sensitivities in the system passband It is stable over the range of parameter variations The performance continues to meet the specifications in the presence of a set of changes in the system parameters Robustness is the sensitivity to the effects that are not considered in the analysis and designfor example, the disturbances, measurement noise, and unmodeled dynamics Sensitivity & Sensitivity Analysis Sensitivity It is the percentage change in system transmission or response or some quantity of interest with respect to the percentage change in another quantity In control theory we use Parameter Sensitivity System Sensitivity Root Sensitivity Eigenvalue Sensitivity Parameter Sensitivity Let T be the system function which depends on a parameter Then, the parameter sensitivity ST of T with respect to s defined as T T ln T T T S ln T System Sensitivity Let T be the system closed loop transfer function which depends on the open loop transfer function G Then sensitivity of T w.r.t G is given as T T ln T T T S G ln G G G G T G Root Sensitivity Let T be the system closed loop transfer function with the ith root given as i and the parameter of interest is say K Root sensitivity is the sensitivity in terms of the position of the roots of the characteristic equation on the (, j) plane(root locus plane) Significance of Root Sensitivity Roots of the characteristic equation represents the dominant(visible) modes of the transient response The effect of parameter variation on the position of the root and the direction of shift of the root are important and useful measures to say about the sensitivity Can be combined with Root Locus Method for Control Designs Definition of Root Sensitivity The root sensitivity of the system T(s) is defined as S ln K K i i i K Let K m T ( s) K ( s z ) 1 j j 1 n ( s ) i 1 i Contd… Let K be a parameter that influences the location of the roots i and the gain K1 Then the root sensitivity is related to the system sensitivity to K and is given as(if zeros of T(s) are not dependent) ln K 1 S ln K ln K ( s ) n T 1 K i i 1 i In the event of gain K1 independent of K, we have 1 1 S S ln K ( s ) (s ) T K n n i i i 1 i 1 i K i Eigenvalue Sensitivity Let us assume that we have the relation(A is from the state space equation) A i i i Differentiating with respect to the element akj of A we will have A A a a a a i i i kj i i kj kj i kj Contd… Premultiplying with i , the left eigenvector we have ii=1 and i (A-i I)=0 Then, we get A a a i i i kj kj Contd… All elements in which will be 1 Therefore we get A will a be zero except the (k,j)th element, kj a i ik kj This is the eigenvalue sensitivity ji Sensitivity Analysis of transfer functions Consider a closed loop system as shown in Figure yd + u - T G 1 G T ln T T G T 1 S ln G G T G 1 G G T G G y Waterbed effect Now, add T and S We get T+S =1 System with cascade compensator We consider the following system yd + K u G y - T GK 1 GK T ln T T G T 1 S ln G G T G 1 GK G T G Check T+S System with feedback compensator Consider the following system yd + u G y - H T G 1 GH T ln T T G T 1 S ln G G T G 1 GH G T G Check T+S Sensitivity & Complimentary Sensitivity Functions In the Robust Control Literature, Sensitivity Function plays a crucial role Let S(s) be the Sensitivity Function Then T(s) is the Complimentary Sensitivity Function such that S+T=1 for SISO and S+T=I for MIMO Open Loop Control Open Loop Control It is the simplest control structure Limited in performance Usually reserved for special applications where feedback control is either impossible or unnecessary It is a good starting point for control design It helps to appreciate the advantages of feedback control Stability, performance etc are relatively in simpler forms to understand Open Loop Structure d yd F u + P + y - e + Input-Output Relations In open loop control input yd is usually a synthesized signal for the given application and u is derived from that as shown Open loop control requires no measurements. Now, from Figure above, we write as y FPy d d and e (1 FP) y d d H ( s) F ( s) P( s) d and H ( s) 1 wd Tracking Performance Perfect tracking of yd occurs if H ( s ) F ( s ) P( s ) 1 d That is, if F ( s ) P( s ) 1 The practical objective is to make in the system passband F ( j ) P( j ) 1 Disturbance rejection Since open H ( s) 1 loop control does nothing to attenuate wd the effects of disturbance inputs nor does it amplify them either Sensitivity The sensitivity of H with (s) respect to P(s) is calculated as d follows H F ( P P) FP FP 0 d FP S H P P 0 FP 0 1 P 0 A sensitivity 1 implies that a given percent change in P translates into the equal percent change in the transmission function H d ( j ) Open loop control does not affect sensitivity Stability Conditions We modify the block diagram of the Open loop control system as shown here v yd + F + z u P y Analysis In any system, any addition or deletion of some of the input lines or some output lines won’t alter the internal stability We shall add inputs and outputs and view this as injecting test inputs into the system and taking extra measurements, neither of which is expected to change the stability properties of the system The test inputs and and outputs are chosen so that the resulting system is controllable and observable For such a fully controllable and observable system there shall not be any hidden modes So, internal stability is then guaranteed by input-output stability Fig.1 yd F u y P v Fig.2 yd + F + u P z The system, in Fig 1 and Fig 2 are same but with additional input v and one additional output z in Fig 2 y Controllability/Observability/Stability System in Fig.2 is controllable and observable if both F(s) and P(s) are controllable and observable System in Fig 2 is internally stable if and only if the both F(s) and P(s) are stable. See below Y ( s ) FPy ( s ) Pv( s ) d z ( s ) Fy ( s ) d Or y( s ) FP P y ( s ) z ( s ) F 0 v( s ) d Analysis contd… Because the realization is controllable and observable, it is internally stable if, and only if, it is input-output stable. That is, if all elements of the matrix transfer function above are stable Thus F(s), P(s) and F(s)P(s) must have only LHP poles If P is of non-minimum phase type, then F cannot be used to cancel the RHP zeros of P, because then F will become unstable. Feedforward Control Feedforward control is a variation of open loop control. It is applicable when the disturbance input is measured The open lop controller F is chosen, to make the output to follow the reference, in spite of the disturbance w Pw u + P y’ + z d y w Pw Pw d F u Here, to realize Feedforward control: + P y’ + z 1. d has to be obtained by proper measurements 2. F is chosen such that y’ is close to –d 3. Or FP is almost unity d y Closed loop control-1 DoF Closed loop control-1 DoF Consider the following system d e yd + F u + P + + - y e ym Ps + + v Analysis We have FP 1 y( s ) y (s) d (s) 1 FP 1 FP d 1 1 e( s ) y ( s ) y( s ) y (s) d (s) 1 FP 1 FP d d With Sensor noise/Measurement Noise If yd =d=0 and v0, then y( s ) FP( y v ) y( s ) FP v( s ) T ( s )v( s ) 1 FP and e( s ) y y( s ) T ( s )v( s ) d Norms are Performance Measures Signal forms and Signal Norms Norm based approach for control design gives a sound platform for robust control designs Different types of norms are used in control systems Use would be depending on the mathematical approaches used to define the norm Norms of signals and systems Euclidean Norm or l2 norm for vector x is given as n x x 2 1 2 i i 1 2 ( x x) T 1 2 For a vector signal x(t), l2 norm is x x (t ) x(t )dt 2 T 1 2 This norm is the square root of the energy in each component of the vector If norm exists x(t) l2 Norms of signals and systems For power signals, we may use the root mean square value(rms) norm 1 rms( x ) lim x (t ) x(t )dt 2T T T T T 1 2 Frobenius Norm For an mxr matrix A, the Frobenius norm is defines as m r A a 2 It can be shown that 2 i 1 j 1 1 2 i, j 2 A 2 tr ( A A) tr ( AA ) T T System Norm LTI systems are generalization of matrices- A matrix operates on a vector to produce another vector An LTI system operates on a signal to produce another signal So, analogous to Frobenius norm, we can define the system norm L2 Norm for LTI systems Let G(s) be an mxr matrix transfer function Then the L2 norm for G(s) is defined as 1 G tr G ( j)G( j)d 2 2 1 2 T ||G||2 exists if an only if each element of G(s) is strictly proper. For SISO we have a scalar TF which need to be strictly proper. There should not any poles on the imaginary axis for either case. Then we say G L2 G(s) plane in H2 When G L2 we can write the norm with respect to complex s plane as 1 G tr (G ( s )G( s ))ds 2j 2 2 T 1 tr (G ( s )G( s ))ds 2j T Contour of integration for the last integral is along the entire imaginary axis and the infinite semicircle in the LHP or RHP Since G(s) is strictly proper, it is easily shown that the integral vanishes over the semicircle If G L2 and in addition, G is stable, then we say that G H2 H2 is the Hardy Space defined with the 2-norm Exercise Calculate the L2 norm of G(s) given as: ( s 3 ) ( s 2 ) 1 G( s ) s 3s 2 2 ( s 2) 2 Answer 3s 21 tr G ( s )G( s ) ( s 1)( s 2)( s 1)( s 2) 2 T Every term in G(s) is strictly proper Contour is Imaginary axis + LHP semicircle with radius L2 norm of G(s) =(3/2) Induced norm Induced norm is a different type of norm which applies to operators and is essentially a type of “maximum gain” For a matrix, the induced Euclidean norm is A max Ad 2i =sqrt(eigen(ATA)) d 2 1 ( A) is the max( ) and is min( ) 2 Induced norm for LTI system To obtain induced norm for an LTI system, consider first a stable, strictly proper SISO system Then, if the input u(.) l2 , then the output y(.) l2 By Parseval’s theorem 1 y G( j) u( j) d 2 2 2 2 2 (A) Clearly 1 y sup G( j) u( j) d 2 2 2 2 2 Or y sup G( j) u 2 2 2 2 2 (B) We argue that the RHS of the inequality in (B) can be reached arbitrarily closely for a fixed value of ||u||2 that is chosen to be 1 with no loss of generality Suppose |u(j)|2 approach an impulse of weight 2 in the frequency domain at = 0 Then the integral of Eq(A) 1 y G( j) u( j) d 2 will approach G( j ) 2 2 2 2 2 0 (A) If G( j)has a maximum at some finite value of , we may choose 0 to be that frequency If not, then G( j must ) approach a supremum as . We can make 0 as large as we like and will G( jbe 0as) close to the supremum as we wish The RHS of inequality in (B) can be reached arbitrarily closely and we get sup y sup G( j) u 2 1 2 Hinfinity Norm The norm calculated last is also the infinity norm given by G lim( G( j) ) p p 1 p The infinity norm of G(s) exists if and only if G is proper with no poles on the j axis In that case we write G L If in addition, G is stable, then we say G H H is the Hardy Space defined with the -norm Norms for Multivariable systems H norm for Multivariable systems For multivariable systems, we have 1 y G( j)u( j) d 2 2 2 2 This can be written as 1 y [ (G( j))] u( j) d 2 2 2 2 2 Further, we may write as 1 y sup (G( j) u( j) d 2 2 2 Or 2 y sup [G( j)] u 2 2 2 2 2 2 2 Contd… The factor ||u(j)||2 in the integrand refers to the 2-norm of the vector u(j) In SISO, the equivalent term refers to the 2-norm of a signal We argue that the RHS of the last inequality y 2 sup j)] by u propoer [G( closely, can be approached arbitrarily choice of 2 u(j) 2 2 2 Essentially we pick u(j) to be the eigenvector of G*(j)G(j) corresponding to the largest eigenvalue, and we concentrate the spectrum of u(j) at the frequency where is the largest (or for some frequencythat is arbitrarily large, if has no maximum, but a supremum. Therefore sup y sup [G( j)] u 2 1 2 MIMO H norm As a continuation of the development, we define G sup [G( j)] Disturbance Rejection Disturbance Rejection Disturbance rejection is a performance measure Effect of disturbance is studied in two ways Input disturbance Output disturbance Rejection of Input disturbance d yd + + u G - H y Analysis T (s ) yd G 1 GH and T (s ) d G 1 GH To suppress disturbance, we want |Td|<<1 For this we need |G|<<1 Keep |G(j)| small where d(t) contains stronger components in the spectrum Rejection of Output Disturbance d yd + u + G - H + y Analysis We have G T (s ) 1 GH and yd T (s ) d 1 1 GH To suppress disturbance, we want |Td|<<1 For this we need |G|>>1 Keep |G(j)| large where d(t) contains stronger components in the spectrum Contradiction The requirements to suppress disturbance at the input is opposite to that needed for suppressing disturbance at the output If the disturbance is present both at input and output we need to use some innovative ways to suppress both the disturbances Noise Rejection yd u + G y + H + n Analysis T (s ) yd G 1 GH and T (s ) n GH 1 GH To suppress noise, we want |Tn|<<1 For this, we need |G|<<1for a given H Keep |G(j)| small where n(t) contains stronger components in the spectrum Exercise yd u + K G y - H Derive the Sensitivity and Complimentary Sensitivity Functions with respect to of the system given as G(s). G(s) is containing Uncertainty Modeling the Uncertain Systems Modeling the Uncertainties/perturbations Uncertainties occur in control systems occur due to variety of reasons Actually, the purpose of control system itself is to deal with uncertainties Purpose of robust control is to render stability & acceptable performance if the uncertainties of certain class occur Structured Uncertainty Interval Models State Space model Transfer function model Unstructured Uncertainty Unstructured uncertainty is modeled, using the perturbation approach, rather than representing the parameters using the intervals There are different formulations that give the uncertain models, mostly use the norm bounds and the perturbations in the additive or multiplicative forms General Basis Given a set of plants P with uncertainty in the parameters. A plant transfer function P(,s)P is a transfer function admissible to represent the uncertain system being considered. P0(0,s) P is one such plant with nominal values of the parameters, where 0 stands for the nominal value of the parameter set(vector) 0 could be the mean value of in the interval [min, max], which is intuitively appealing Uncertainty could then be given as = 0[1+] 0 =(1/2)(min+max) & = (min -max)/ (min+max) ||1 is the perturbation Unmodeled dynamics Uncertainty due to neglected and unmodeled dynamics is more difficult to quantify The frequency domain is well suited for representing this class of uncertainty through complex perturbations, which are normalized such that ||||1 where |||| is the H norm of = sup ( j ) Classification of unstructured uncertainty-SISO Additive Uncertainty Multiplicative Uncertainty Inverse Multiplicative Uncertainty Division Uncertainty Use of the Uncertainty is depending on the problem being considered and the designer’s skill. For MIMO systems, the constraints of pre and post multiplication gives rise to more classes of uncertainty Additive Uncertainty Let us sue the property P0(0,s) P is one such plant with nominal values of the parameters, where 0 stands for the nominal value of the parameter set(vector) Let P(,s)= P0(0,s) +P(s) P(s) is the complex perturbation applied to obtain the class of uncertain plants P(,s) and is stable Then P(,s) is given in the Additive Uncertainty form Usually, this is written as P:Gp(s)=G(s)+wa(s) a(s) with ||||1 Example Consider the system P: Gp(s)=AG (s). The uncertainty is in the Gain A and is given as A[Amin ,Amax] Let A0 =(1/2)(Amin+Amax) A= (Amin -Amax)/ (Amin+Amax) A= A0[1+ A ] Gp(s)= A0[1+ A ] G (s)=A0 G (s)+ A0 A G (s) Multiplicative Uncertainty Let P(,s)= P0(0,s) + P0(0,s) P(s) P(,s)= P0(0,s)(1+ P(s)) Or P(,s)= P0(0,s)[1+ wm(s) m(s)] Or ||||1 Example P: Gp(s)=AG (s). The uncertainty is in the Gain A and is given as A[Amin ,Amax] Let A0 =(1/2)(Amin+Amax) A= (Amin -Amax)/ (Amin+Amax) A= A0[1+ A ] Gp(s)= A0 [1+ A ] G (s)=A0G (s) [1+ A ] General method to find the Additive & Multiplicative Uncertainty Model Examples have shown the derivation of unstructured uncertainty from parametric uncertainty This is simple for simple cases but Tough for high order systems with uncertainty in many parameters, because Assumption about model and parameters may be inexact The exact model structure is indispensable Unmodeled dynamics cannot be then handled Method Given a model with uncertainties Choose a nominal model(or lower order or delay free or a model of mean parameters or the central plant obtained from Nyquist plot corresponding to all plants in the given set) For Additive uncertainty, find the smallest radius l a() which includes all possible plants such that l a() =|Gp(j)-G (j)| Find a rational lower order transfer function wa(s) which is the uncertainty weight such that |wa (j)| l a() The uncertain additive plants Gp(s)=G(s)+wa (s) a(s) Contd… In the case of multiplicative uncertainty, find the smallest radius l a() such that for all possible plants l a()= G ( j ) G ( j ) max G p P p G ( j ) For a chosen rational weight wm(s), there must be |wm (j)| l m() Then Gp(s)=G(s)(1+wm(s) m(s)) Block diagram forms of uncertainty Additive Uncertainty Model a (s) wa(s) + G(s) + Multiplicative Uncertainty wm(s) m (s) + G(s) + Inverse Multiplicative im (s) + wim(s) + G(s) Division Uncertainty Consider the 1 G (s) s s 1 p 2 with 0.4 0.8 It is easy to see that =0.6+0.3 with ||1 G p ( s) 1 s 2 0.6s 1 G p ( s) G( s)[1 wd ( s)G( s)]1 1 w ( s ) 0.2s d Robust Control Robust Control Normally Robust control design considers two aspects Robust Stability(RS) Robust Performance(RP) As a bottom line we need Nominal stability(NS) and Nominal performance(NP) Robust Stability? How far the uncertainty can be, without violating the stability, if the nominal system is stable? Im (-1,j0) ? |1+G(j)| G(j) Nyquist Plot Re Robust Stability with Multiplicative Uncertainty Wm(s) + yd K(s) - Gp(s) m(s) + u + G(s) y Analysis We have G ( s ) G( s )(1 w ( s ) ( s )) p m m G(s) w ( s )G( s ) ( s ) m m m Assume that the nominal plant is stable Using Nyquist stability condition, we need w ( s )G( s ) 1 G( s ) m Or w ( s )G( s ) 1 1 G( s ) m 1 We have S ( s ) [1 K ( s )G( s )] 1 T ( s ) K ( s )G( s )[1 K ( s )G( s )] 1 S (s) T (s) 1 For robust stability, we want w ( s ) K ( s )G( s ) 1 1 K ( s )G( s ) m using H-inf we have Or w ( s)T ( s ) 1, and m w ( s )T ( s ) 1 m Robust Performance We find the bounds on the Sensitivity Function S and/or Complimentary Sensitivity Function T for the given bounds on Disturbance or Measurement noise Doyle’s Theorem A necessary and sufficient condition for robust performance is to satisfy the condition W1S W T 2 1 Books Prabha Kundur “Power System Stability & Control” Tata McGrawHill, 1994|2012 Richard C Dorf & Robert H Bishop, “Modern Control Systems” Addison Wesley, 1999 Pierre R. Belanger, “Control Engineering: A Modern Approach” Saunders College Publishing, 1995 John Dorsey, “Continuous & Discrete Time Control Systems”, McGrawHill International, 2002 Vladimir Zakian, “Control Systems Design-A new Framework”, Springer 2005
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