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Full-order state observer

A full-order state observer estimates all of the system state variables. If, however, some of the state variables are measured, it may only be neeessary to estimate a few of them. This is referred to as a redueed-order state observer. All observers use some form of mathematieal model to produee an estimate x of the aetual state veetor x. Figure 8.8 shows a simple arrangement of a full-order state observer. [Pg.254]

Effect of a full-order state observer on a closed-loop system... [Pg.260]

Figure 8.10 shows a elosed-loop system that ineludes a full-order state observer. In Figure 8.10 the system equations are... [Pg.260]

A full-order state observer estimates all state variables, irrespeetive of whether they are being measured. In praetiee, it would appear logieal to use a eombination of measured states from y = Cx and observed states (for those state variables that are either not being measured, or not being measured with suffieient aeeuraey). [Pg.262]

Example 8.12 shows how acker uses the transpose of the A and C matriees to design a full-order state observer. [Pg.406]

The pole placement design predicates on the feedback of all the state variables x (Fig. 9.1). Under many circumstances, this may not be true. We have to estimate unmeasureable state variables or signals that are too noisy to be measured accurately. One approach to work around this problem is to estimate the state vector with a model. The algorithm that performs this estimation is called the state observer or the state estimator. The estimated state X is then used as the feedback signal in a control system (Fig. 9.3). A full-order state observer estimates all the states even when some of them are measured. A reduced-order observer does the smart thing and skip these measurable states. [Pg.181]

Fig. 8.10 Closed-loop control system with full-order observer state feedback. Fig. 8.10 Closed-loop control system with full-order observer state feedback.
Equation (8.157) shows that the desired elosed-loop poles for the eontrol system are not ehanged by the introduetion of the state observer. Sinee the observer is normally designed to have a more rapid response than the eontrol system with full order observed state feedbaek, the pole-plaeement roots will dominate. [Pg.261]

In order to tackle the problem of uncertainties in the available model, nonlinear robust and adaptive strategies have been developed, while, in the absence of full state measurements, output-feedback control schemes can be adopted, where the unmeasurable state variables can be estimated by resorting to state observers. The development of model-based nonlinear strategies has been fostered by the development of efficient experimental identification methods for nonlinear models and by significantly improved capabilities of computer-control hardware and software. [Pg.92]

Figure 21. Linear-logarithmic plot of the crossover chemical potential vs. the crossover period. Data obtained from the peaks observed in plots of Var(lgl) vs. /ito full circles), and Var( g ) vs. r (full squares). The full line showi ng the border between dynamic ordered states and dynamic disordered states has been drawn in order to guide the eye. Also, the vertical dashed line corresponds to the mininnim period at which dynamic disordered states were observed. More details are provided in the text. (Reprinted from Ref. [17], with permission from the the American Chemical Society.)... Figure 21. Linear-logarithmic plot of the crossover chemical potential vs. the crossover period. Data obtained from the peaks observed in plots of Var(lgl) vs. /ito full circles), and Var( g ) vs. r (full squares). The full line showi ng the border between dynamic ordered states and dynamic disordered states has been drawn in order to guide the eye. Also, the vertical dashed line corresponds to the mininnim period at which dynamic disordered states were observed. More details are provided in the text. (Reprinted from Ref. [17], with permission from the the American Chemical Society.)...
A full development of the rate law for the bimolecular reaction of MDI to yield carbodiimide and CO indicates that the reaction should truly be 2nd-order in MDI. This would be observed experimentally under conditions in which MDI is at limiting concentrations. This is not the case for these experimements MDI is present in considerable excess (usually 5.5-6 g of MDI (4.7-5.1 ml) are used in an 8.8 ml vessel). So at least at the early stages of reaction, the carbon dioxide evolution would be expected to display pseudo-zero order kinetics. As the amount of MDI is depleted, then 2nd-order kinetics should be observed. In fact, the asymptotic portion of the 225 C Isotherm can be fitted to a 2nd-order rate law. This kinetic analysis is consistent with a more detailed mechanism for the decomposition, in which 2 molecules of MDI form a cyclic intermediate through a thermally allowed [2+2] cycloaddition, which is formed at steady state concentrations and may then decompose to carbodiimide and carbon dioxide. Isocyanates and other related compounds have been reported to participate in [2 + 2] and [4 + 2] cycloaddition reactions (8.91. [Pg.435]

Design with full-state and reduced-order observers (estimators). [Pg.171]


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See also in sourсe #XX -- [ Pg.254 , Pg.260 , Pg.271 ]




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