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Input-Output Linearization

in process control, input-output linearization techniques are usually preferred to state-space approaches, mostly due to the higher complexity of the latter, in the following, only input-output feedback linearization basic concepts are briefly reviewed. [Pg.95]

The same definition applies for Lgh, where the function g plays the same role as / in (5.8). Of course, higher-order Lie derivatives can be defined in a recursive way, e.g., [Pg.95]

If the relative order y, of y with respect to u is l,1 then Lgh 0, and the procedure stops here. Otherwise, the procedure is iterated until LgL xh 0, i.e., until the derivative of order y, is computed  [Pg.96]


M.A. Henson and D.E. Seborg. Input-output linearization of general non-linear process. A.I.Ch.E. Journal, 36 1753-, 1990. [Pg.50]

Proposition 4. Since the AD model (2) is a minimum-phase system and has a well-defined relative degree r under NOC. Then, the following input-output linearizing controller will make converge exponentially the total concentration of organic substrate St to a desired value for all t > 0... [Pg.180]

Proof. By implementing the input-output linearizing controller (6) to the AD model in the normal form (5), it is obtained that... [Pg.181]

Remark 1. From Proposition 4, the existence of an input-output linearizing control law capable to regulate exponentially the total concentration of organic substrate St in a desired value S was demonstrated. However, in order to implement this controller in practice, a perfect knowledge of the process dynamics is required. In other words, this implies that either the influent composition St,in or the process kinetics k, /j,. ) must be perfectly known. Nevertheless, this condition is difficult to satisfy in practice limiting its application. But what about if the uncertain terms can be estimated from available measurements and a control scheme with a similar structure to that of the input-output linearizing controller (6) is used. In the next section, a robust approach is proposed based in this fact. [Pg.181]

The GMC control response can be designed via the tuning parameters K and K2 based on the tuning curve given by [24], It should be noted that the GMC approach is a special case of the global input output linearizing control technique in which a transformed control action is chosen properly with the external PI controller. The use of Eq. (16) forces y toward its set point, ysp, with zero offset. If Eq. (15) is differentiated, and the Eq. (16) is substituted into the resulting equation, the GMC control law is... [Pg.107]

Several process control design methods, such as the Generic Model Control (GMC) [41], the Globally Linearizing Control (GLC) [37], the Internal Decoupling Control (IDC) [7], the reference system synthesis [8], and the Nonlinear Internal Model Control (NIMC) [29], are based on input-output linearization. [Pg.96]

The Generic Model Control (GMC) is a model-based control strategy developed by Lee and Sullivan in 1988 [41], It can be shown that GMC is an input-output linearization technique for processes with unitary relative order [31],... [Pg.96]

C. Kravaris and C.B. Chung. Nonlinear state feedback synthesis by global input-output linearization. AIChE Journal, 33 592-603,1987. [Pg.118]

We used the model of the fast dynamics of the system in Equation (4.36) to design a nonlinear input-output linearizing output feedback controller with integral action (Daoutidis and Kravaris 1992) for x. The controller was designed to produce the critically damped second-order response... [Pg.88]

We then used the model (5.51) as the basis for synthesizing an input-output linearizing controller with integral action (Daoutidis and Kravaris 1992) for the product purity xB = 1 — Cs - C6, using the condenser vapor holdup setpoint... [Pg.123]

The non-stiff, low-dimensional model (6.63) is ideally suited for control purposes. We used it to design an input-output linearizing controller with integral action that manipulates QH and enforces a first-order response in the Tr dynamics, namely... [Pg.170]

The term Cb + 71,1 dCB/dt is statically equivalent to Cb, and corresponds to requesting a first-order response in Cb when using a standard input-output linearizing controller. However, such a controller would lead to closed-loop instability, and the output requires a statically equivalent addition that would allow one to overcome this limitation. [Pg.211]

With the outputs y and M, using the reduced-order model (7.38), a multi-variable input-output linearizing controller with integral action (Daoutidis and Kravaris 1994) was designed for the product purity and reactor holdup, requesting a decoupled first-order response ... [Pg.212]

Listing C.l. Symbolic derivation of reduced-order model of the slow dynamics, and of the input-output linearizing temperature controller for the reactor-feed effluent heat exchanger system in Section 6.6... [Pg.237]

Kloppenburg E. and Gilles E.D., Automatic control of the simulated moving bed process for Cg aromatics separation using asymptotically exact input/output-linearization. J. of Process Control 9 (2000) pp. 41-50. [Pg.181]

A general input-output linear model for a single-output system with input u and output y can be written ... [Pg.185]

R. Marino, S. Peresada, and P. VaUgi. Adaptive input-output linearizing control of induction motors. IEEE Transaction on Autemiatic Control, 3S(2) 20 22l, 1993. [Pg.320]


See other pages where Input-Output Linearization is mentioned: [Pg.37]    [Pg.174]    [Pg.95]    [Pg.57]    [Pg.88]    [Pg.125]    [Pg.211]    [Pg.238]    [Pg.241]    [Pg.241]    [Pg.214]    [Pg.214]    [Pg.123]   


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Input/output

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