63 research outputs found
Robust mixed H-2/Hâ control for a class of nonlinear stochastic systems
The problem of mixed H2/Hâ control is considered for a class of uncertain discrete-time nonlinear stochastic systems. The nonlinearities are described by statistical means of the stochastic variables and the uncertainties are represented by deterministic norm-bounded parameter perturbations. The mixed H2/Hâ control problem is formulated in terms of the notion of exponentially mean-square quadratic stability and the characterisations of both the H2 control performance and the Hâ robustness performance. A new technique is developed to deal with the matrix trace terms arising from the stochastic nonlinearities and the well-known S-procedure is adopted to handle the deterministic uncertainities. A unified framework is established to solve the addressed mixed H2/Hâ control problem using a linear matrix inequality approach. Within such a framework, two additional optimisation problems are discussed, one is to optimise the Hâ robustness performance, and the other is to optimise the H2 control performance. An illustrative example is provided to demonstrate the effectiveness of the proposed method.This work was supported in part by the Engineering and Physical Sciences Research Council (EPSRC) of the UK under Grant GR/S27658/01, the Nuffield Foundation of
the UK under Grant NAL/00630/G and the Alexander von Humboldt Foundation of Germany, the National Natural Science Foundation of China under Grant 60474049 and the Fujian provincial Natural Science Foundation of China under Grant A0410012
Gestion des dĂ©chets hospitaliers au Maroc. Cas du CHU de Rabat-SalĂ© et de lâHĂŽpital Militaire Moulay Ismail de MeknĂšs.
Le secteur des déchets, et en particulier celui des déchets hospitaliers représente un fardeau de plus en plus encombrant: prÚs de 8000 tonnes de déchets solides hospitaliers sont produits chaque année au Maroc(les déchets liquides étant difficilement quantifiables).
Ces dĂ©chets, qui se distinguent en dĂ©chets mĂ©dicaux proprement dit, et en dĂ©chets mĂ©nagers et assimilables, se rĂ©partissent entre deux grands types dâhĂŽpitaux: les centres hospitaliers universitaires et les hĂŽpitaux pĂ©riphĂ©riques.
Dans notre Ă©tude, nous avons pris lâexemple du CHU de Rabat-SalĂ© oĂč la gestion des dĂ©chets hospitaliers est Ă lâordre du jour; A son niveau, il existe une production quotidienne de 9,75 pour une capacitĂ© litiĂšre de 3250 lits; Mais Ă fin de mieux cerner le problĂšme de la gestion des dĂ©chets au CHU, nous avons choisi lâHĂŽpital dâEnfant de Rabat oĂč lâensemble des services gĂ©nĂšres une production de dĂ©chets dâenviron 3594 kg/jour.
En parallĂšle, nous avons choisi lâHĂŽpital Militaire Moulay Ismail de MeknĂšs; Ă son niveau, lâestimation de la quantitĂ© de dĂ©chets produits chaque jour, est de 1075kg.
Dâautre part, grĂące Ă une Ă©tude de proximitĂ©, nous avons pu constater lâampleur de la problĂ©matique des dĂ©chets hospitaliers, analysons ces diffĂ©rents problĂšmes et nous proposons dans la mesure de nos moyens quelques solutions.
Au niveau de certains hĂŽpitaux, la prise de conscience de la problĂ©matique des dĂ©chets par lâensemble des acteurs concernes, a permis de rechercher une solution pour lâamĂ©lioration de ce secteur; Celle-ci repose sur la bonne maĂźtrise tout le long de la chaĂźne dâĂ©limination: tri, collecte, entreposage, transport et traitement.
Enfin, la 28-00 de loi, a permis de combler le vide juridique qui se faisait sentir dans ce domaine
Global input constrained adaptive lambda-tracking with application to a nonlinear distributed parameter exothermic chemical reaction models in tubular reactor
We consider input constrained adaptive output feedback control for
exothermic chemical tubular reactor with axial dispersion. we use a non linear
distributed parameter model with boundary control for both the evolution of the
temperature and concentration. Our objective is the set point control of the output
i.e, the temperature of the reaction. Practical consideration lead us to work in the
presence of input constraints. we apply a λ-tracking controller, we show that for
all initial temperature and under a simple feasibility assumptions that the tracking
error tends asymptotically to a ball centred at the reference temperature and of
arbitrary prescribed radius
Adaptive local tracking of a temperature profile in tubular reactor with partial measurements
In this work, a local constrained adaptive output feedback is presented for a class of exothermic tubular reactors models described by a nonlinear partial differential equations. The considered output is the measured temperature in a fixed zone of the reactor to regulate the temperature throughout the reactor to a ball with radius λ (arbitrarily small) centered at the fixed temperature profile. For a given measurement zone with length given in terms of the desired profile and λ and for initial temperature in a fixed domain, it is shown that the tracking error through the reactor tends asymptotically to a ball of arbitrary prescribed radius λ > 0, centered at the given temperature profile. Numerical simulations have been performed to illustrate the performance of the proposed approach
Constrained Global Adaptive Controller for a Plug flow Tubular Reactor with Partial Temperature Measurements
In this work, a global constrained adaptive output feedback is presented for a class of plug-flow tubular reactors models described by non-linear partial differential equations. The output of the system is the measured temperature in a fixed zone of the reactor. It is then used to regulate the temperature throughout the reactor to a ball with radius λ (arbitrarily small) centred at the fixed temperature profile
Global Adaptive λ Tracking of a Temperature Profile in Tubular Reactor
This paper deals with the control design for a class of nonlinear distributed parameter
systems, i.e. convection-diffusion-reaction systems, encountered under the form of
non-isothermal tubular reactors in chemical engineering applications. More specifically
the design concentrates on the boundary control of the temperature profile in an
exothermic chemical reactor under input constraints. Our objective is to analyze the
global stability of the closed-loop system by considering a simple control structure, i.e.
an adaptive λ-tracking controller. It is shown that for all initial
temperature and under simple feasibility assumptions, the tracking error tends
asymptotically to a ball of arbitrary prescribed radius λ> 0, centered at the
given temperature profile
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