2003
DOI: 10.1016/s0009-2509(02)00559-6
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Control of a solution copolymerization reactor using multi-model predictive control

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Cited by 77 publications
(41 citation statements)
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“…⋄ Remark1: It could be noticed that gain synthesis through multiple operating point with such LMI consideration provide only one single gain for all OP due to Bilinear Matrix inequality (BMI) problem in term (2, 1) of LMI (17). However, other system such piecewise linear system could use the same approach with a multiple gain synthesis as in (Ozkan et al, 2003).…”
Section: Control Law Synthesis In Fault-free Casementioning
confidence: 99%
“…⋄ Remark1: It could be noticed that gain synthesis through multiple operating point with such LMI consideration provide only one single gain for all OP due to Bilinear Matrix inequality (BMI) problem in term (2, 1) of LMI (17). However, other system such piecewise linear system could use the same approach with a multiple gain synthesis as in (Ozkan et al, 2003).…”
Section: Control Law Synthesis In Fault-free Casementioning
confidence: 99%
“…Indeed, these methods consider a particular multiple or multi-model approach where each model is dedicated to a specified fault. A polytopic representation is sometimes used in multi-model or piecewise linear models [9]. This paper addresses a more general method that could allow to detect actuator fault in a nonlinear system.…”
Section: Introductionmentioning
confidence: 99%
“…These four operating points developed are: Vr = 27.90h −1 . The nonlinear model has been discretized through a Tustin method in order to provide discrete linear models represented in equation (11). Disturbance matrices of modeling error E i are directly obtained by a second order linearization and an unique matrix E * is computed through an optimization technique based on Singular Value Decomposition as proposed in [1].…”
Section: Experiments and Resultsmentioning
confidence: 99%
“…Matrices (A i , B i , C i , D i ) are invariant matrices defined around the i th operating point (OP i ) generally obtained from a nonlinear system using a first-order Taylor expansion around (x i e , u i e ) with y i e = C i x i e + D i u i e or identification of a nonlinear system around predefined operating points as for example in chemical processes in [11] and [10]. The fault distribution matrix is represented by F i ∈ R n×p .…”
Section: A Nonlinear Representationmentioning
confidence: 99%
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