2011
DOI: 10.1049/iet-cta.2010.0232
|View full text |Cite
|
Sign up to set email alerts
|

Operator-based output tracking control for non-linear uncertain systems with unknown time-varying delays

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
2

Citation Types

0
14
0

Year Published

2011
2011
2018
2018

Publication Types

Select...
4
2
1

Relationship

0
7

Authors

Journals

citations
Cited by 33 publications
(14 citation statements)
references
References 10 publications
0
14
0
Order By: Relevance
“…5, where, Φ is a generalized Prandtl-Ishlinskii hysteresis operator such that u * (t) = Φ(u)(t), the real plantP and the model P have right factorization asP =ÑD −1 = (N + ΔN )D −1 and P = ND −1 respectively, ΔN is concerning with the unmodelled uncertainties and is bounded, A, B and F are operators to be designed, r ∈ U , u ∈ U , w ∈ W and y ∈ V are the reference input, control input, quasi-state and system output respectively. Proposed control design for nonlinear uncertain system with PI hysteresis In [13], the mismatch between the real plant and the nominal plant can be predicted by a prediction structure, which is denoted by ΔP * and the desired mismatch operator is equivalent to the plant perturbation ΔP , namely, ΔP * = ΔP . We assume that ΔP * have right factorization as ΔP * = ΔN * D −1 , and ΔN * is bounded.…”
Section: B Robust Control For System With Generalized Pi Hysteresismentioning
confidence: 99%
See 1 more Smart Citation
“…5, where, Φ is a generalized Prandtl-Ishlinskii hysteresis operator such that u * (t) = Φ(u)(t), the real plantP and the model P have right factorization asP =ÑD −1 = (N + ΔN )D −1 and P = ND −1 respectively, ΔN is concerning with the unmodelled uncertainties and is bounded, A, B and F are operators to be designed, r ∈ U , u ∈ U , w ∈ W and y ∈ V are the reference input, control input, quasi-state and system output respectively. Proposed control design for nonlinear uncertain system with PI hysteresis In [13], the mismatch between the real plant and the nominal plant can be predicted by a prediction structure, which is denoted by ΔP * and the desired mismatch operator is equivalent to the plant perturbation ΔP , namely, ΔP * = ΔP . We assume that ΔP * have right factorization as ΔP * = ΔN * D −1 , and ΔN * is bounded.…”
Section: B Robust Control For System With Generalized Pi Hysteresismentioning
confidence: 99%
“…We assume that ΔP * have right factorization as ΔP * = ΔN * D −1 , and ΔN * is bounded. As mentioned in [13], operator N can be divided into two parts, that is, N = N u + N s , where, N u is unimodular operator, N s is stable and is as small as possible. Then, if the uncertainty part is relatively small to N u , namely,…”
Section: B Robust Control For System With Generalized Pi Hysteresismentioning
confidence: 99%
“…The right coprime factorization approach based on Lipschitz condition from operator view of point has been considered by many authors . In , robust right coprime factorization for nonlinear systems is considered firstly.…”
Section: Introductionmentioning
confidence: 99%
“…The reason of considering these model including uncertainties is to approach real control systems. Next, operator based nonlinear feedback control systems are realized by using robust right coprime factorization corresponding to the MIMO nonlinear control system including coupling effects, and Lipschitz norm based robust stability conditions are applied to the system and to guarantee robust stability of the process and system [4], [5], [7],-, [9]. Moreover, the existed methods in [10] are applied to the processes to guarantee tracking performance.…”
Section: Introductionmentioning
confidence: 99%
“…G 12 (U 2 ( t )) = 0, (16) by (2) and (7) [7]. The nominal processes P i have the right coprime factorization Ni, Di as P i = NiDi 1 (i = 1, 2), 2g Yl ( t )…”
mentioning
confidence: 99%