2010
DOI: 10.1016/j.isatra.2010.03.003
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Static and low order anti-windup synthesis for cascade control systems with actuator saturation: An application to temperature-based process control

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Cited by 22 publications
(11 citation statements)
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“…For this purpose, again consider system (20), but in an alternative form given by dedt=Ae+A1e(tτ)+[III]d,withd=[normalΨTnormalΘTnormalΦT]T, where I represents the identity matrix of appropriate dimensions. Although the asymptotic convergence of error e to zero under parametric uncertainties can be ensured by Theorem 10, the performance of the synchronization control can be improved for robustness with the help of additional constraints addressing the minimization of the effects of uncertainties in d at error e (see also [3335]). To that end, we provide a sufficient condition for robust asymptotic synchronization of FHN neurons with robustness bound γ in terms of the L 2 gain from the uncertain nonlinearities to the error.…”
Section: Local Nonlinear Controlmentioning
confidence: 99%
“…For this purpose, again consider system (20), but in an alternative form given by dedt=Ae+A1e(tτ)+[III]d,withd=[normalΨTnormalΘTnormalΦT]T, where I represents the identity matrix of appropriate dimensions. Although the asymptotic convergence of error e to zero under parametric uncertainties can be ensured by Theorem 10, the performance of the synchronization control can be improved for robustness with the help of additional constraints addressing the minimization of the effects of uncertainties in d at error e (see also [3335]). To that end, we provide a sufficient condition for robust asymptotic synchronization of FHN neurons with robustness bound γ in terms of the L 2 gain from the uncertain nonlinearities to the error.…”
Section: Local Nonlinear Controlmentioning
confidence: 99%
“…The plant model is identified using an identification technique of uniformly distributed numbers similar to that in [11,12]. For system identification, uniform random numbers (at every 30 sec) are applied at the plant input and output is recorded with a sampling time of 0.1 sec as shown in Fig.…”
Section: System Description Identification and Conditioningmentioning
confidence: 99%
“…2. This input-output plot can be used to obtain the magnitude plot for system identification in a similar way described in [11,12]. Fig.…”
Section: System Description Identification and Conditioningmentioning
confidence: 99%
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“…Temperature control systems are generally non-linear in nature. Such systems are controlled by both linear and nonlinear controllers [1][2][3][4]. Linear controllers are easy to design but their performance cannot be very good.…”
Section: Introductionmentioning
confidence: 99%