Teaching Digital Control and Filtering Using MATLAB and Vissim

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Teaching Digital Control and Filtering Using MATLAB and Vissim Teaching Digital Control and Filtering Using MATLAB andVisSim Raymond G. Jacquot and Jerry C.Hamann College of Engineering, University of Wyoming Laramie, WY 82071-3295 Abstract In the past, the authors have taught essentially the identical course material, but due to computational The authors report the revision for a course limitations the problem assignments have been rather entitled Discrete Data Systems which is a blend of simple, usually of the second-order variety. With the classical and modern digital control, and digital convenience offered by MATLAB for Windows [1] and filtering. This revision reflects computing resources now VisSim [2], the authors have made the assigned problems available and as a result no longer are low order system more realistic and can concentrate class time on problems assigned. The authors have incorporated algorithms for the design process rather than getting symbolic computing in several appropriate places where bogged down with detailed classroom calculations. In it can increase understanding and yield error-free addition, the Symbolic Toolbox of MATLAB allows algebraic manipulations. In most exercises, the some rather tedious, error-prone algebraic manipulations computing is of the numerical type using algorithms to be accomplished with zero errors. The authors and developed in the course. Simulation employing a others have reported previously the use of symbolic graphical-oriented simulation language lends reality as computation in a digital filter design course [3]. VisSim to how control laws and estimation algorithms are is a simulation environment which handles mixed implemented in practice and lets students explore the continuous- and discrete-time elements with a graphical effects of controller parameters and sampling interval on user interface. The learning curve for VisSim is responses. essentially negligible, and students progress rapidly in their ability to simulate complex systems. Simulink [4] is Introduction an alternative to the use of VisSim and runs seamlessly with MATLAB. A “theme problem” is employed for most of the At the University of Wyoming a lower level exercises in the course. This problem is one that is graduate course is offered to introduce graduate students, interesting from both a classical and a state space design in a variety of specialty areas, to discrete-time control point-of-view and one not amenable to hand calculations, and digital filtering. The students are typically from the thus motivating the students to develop an interest in the controls, power systems and signal processing areas with modern software tools. an occasional mechanical or chemical engineer thrown in for good measure. The course is a blend of classical discrete-data control topics, modern digital control topics Theme Problem Plant and digital filter synthesis techniques. A topical outline is given in Table 1. The plant chosen for the homework exercise is the thermal environmental chamber illustrated in Fig. 1. Table 1. Course Outline The outer chamber is heated by a flow of steam which is Review of z-transforms controlled by a valve for which the dynamics may not be The pulse transfer function neglected. Fig. 1 is labeled with the perturbed Single-loop controller design temperature variables (x1(t), x2(t), w(t)) and the perturbed PID and lead-lag controllers valve gate motion variable (x3(t)). This model is then Ragazzini controller design analyzed for small perturbations in the physical variables Digital filter synthesis about an equilibrium condition, with x1(t) and x2(t) being Discrete-time state variable representation the temperature perturbations in the inner and outer State feedback and associated algorithms chambers respectively. The variable x3(t) is the Prediction, current and reduced order observers perturbation in the valve opening while the current used Nonzero setpoints versus regulators to produce that perturbation is denoted as u(t). The L-Q optimal control perturbation in the environmental temperature is denoted Reciprocal root locus as w(t). w(t) b x2(t) u(t) x1(t) x3(t) N S S N K2/2 Coil K2/2 X From Steam Generator Valve Figure 1. Thermal Chamber System to be Controlled The governing differential equations for the perturbations Pulse Transfer Function are, assuming appropriate coefficients, dx1 = -x1 + x2 After a brief review of the z-transform it is dt appropriate to examine how a discrete-time dx2 representation of the plant and the associated data = x1 - 2x2 + 2x3 + w(t) (1) dt converters can be obtained. The A/D and D/A converters dx are assumed to operate synchronously at a rate specified 3 = -4x + u(t) dt 3 by the sampling interval T and to have infinitely precise If the temperature of the inner chamber is taken to be the representations of the digital data. The so-called pulse system output, the transfer function for the open-loop transfer function is then given by plant is z -1 ì -1 éG(s)ù ü G(z) = ZíL t=kT ý (5) X (s) z ëê s ûú G(s) = 1 = 2 (2) î þ U(s) s3 + 7s2 + 13s + 4 where Z{.} represents the taking of the z-transform and -1 From relations (1) the continuous-time state description L [.] represents the taking of the inverse Laplace matrices are transform. MATLAB is particularly useful utilizing the é-1 1 0 ù é0ù ‘residue’ function for evaluation of the partial fraction coefficients for G(s)/s. The ‘deconv’ function is F = ê 1 -2 2 ú , g = ê0ú (3) ê ú ê ú particularly attractive for the reassembly of the z-domain ëê 0 0 -4ûú ëê1ûú fractions into a single polynomial ratio for G(z). The and pulse transfer function for this plant for a sampling cT = [1 0 0] (4) interval of T = 0.2 s is It is in this setting that the problem exercises are 0.001899(z + 2.6629)(z + 0.1865) constructed. Of course, the problems could be of higher G(z) = (6) (z - 0.9625)(z - 0.5924)(z-.4493) order, but in the authors’ opinions this system is of sufficient complexity to be instructive while illustrating the power of contemporary computing tools. Cascade Controller Design State Variable Representation This content focuses on the synthesis of a The first step in the discrete-time state variable discrete-time controller with transfer function D(z) which design process is to find a discrete-time state variable will reshape either the root locus diagram or the open- representation of the plant and the associated data loop frequency response to yield performance which is converters. The plant and data converters can be improved. Here the polynomial handling facilities of represented by the matrix-vector difference equation MATLAB are invaluable particularly in the synthesis of x(k +1) = Ax(k) + bu(k) (7) finite settling time and ripple-free controllers. Easy The process of evaluation of the A and b matrices can be calculation and graphical display are highly desirable for carried out either analytically or numerically. The these trial-and-error designs. The ease of mixed discrete- analytical process involves the inversion of Laplace time and continuous-time system simulation make transforms for which the ‘residue’ function is invaluable. VisSim attractive for design evaluation and for The numeric process involves the calculation of the understanding of control law implementation. matrix exponential, for which MATLAB is particularly well-suited. The discrete-time state variable matrices Digital Filter Synthesis computed for a sampling interval of T = 0.2s are é0.8341 0.1494 0.0254ù é0.0019ù In this course there is in-depth discussion of ê A = 0.1494 0.6847 0.2227ú , b = ê0.0273ú (8) several approaches to digital filter synthesis. The reason ê ú ê ú for examination of this topic is that often controllers are ëê 0 0 0.4493ûú ëê0.1377ûú synthesized in the s-domain and are to then be At this point it is also advantageous to explore system implemented in discrete-time form. The two methods controllability and observability employing the ‘rank’ addressed are the bilinear transform method (Tustin’s function in MATLAB. method) and the matched-pole-zero technique. The authors have previously discussed the use of State and Estimated State Feedback symbolic computing for the bilinear-transform synthesis of digital filters [3]. The approach taken is that the The design process begins with the designer starts with a unit frequency lowpass prototype of consideration of pole placement using full state feedback. Butterworth, Chebyshev, inverse Chebyshev or elliptic This involves the expansion of a symbolic determinant type. The first step is to perform either a lowpass, and equating it to the desired closed-loop characteristic bandpass, bandstop or highpass transformation to yield equation ac(z) an s-domain filter of the correct type. The next step is to det[zI - A + bf T ] = a (z) (9) prewarp the poles of this filter so they will have the c This nasty algebraic expansion involves the symbol z and correct critical frequencies after the bilinear transform to the symbolic elements of the vector fT and as such is a the z-domain has been performed. Depending upon the process that is quite prone to human error in attempted extent to which one desires to involve the student in the manipulation and simplification. This is an ideal process, the MATLAB Symbolic Toolbox can be used to application of the MATLAB Symbolic Toolbox which is advantage for both of these processes while demanding a also incorporated into the Student Edition of MATLAB substantial degree of mastery of the process on the part of [5]. In the absence of a complete set of state the student. Alternatively, purely numerical alternatives measurements, the appropriate control law is to feed back which demand very little process expertise can also be estimates of the states obtained from an asymptotic employed, for example the functions 'lp2bp' and observer either of the prediction or current variety.
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