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Control of an industrial multi-staged catalyst fixed bed reactor

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Figure

Fig. 1.  réacteur catalytique étagé d’oxydation du SO2 avec refroidissements intermédiaires [3]
Fig. 2.  Injection d'une perturbation impulsion sur C 1in  (C 1in  = 0.1), A 0.3 heure, durant: 10 minutes valant +20 %  La figure 3 montre que malgré l'occurrence d'une perturbation d'une intensité importante relative à la teneur en dioxyde  de  soufre  ;
Fig. 4.  Régulation de la température à 610 °C
Fig. 6.  Régulation de la température à 610 °C Injection d'une perturbation impulsion sur C 1in  (C 1in  =0.1) à 1 heure, valant -20 %,  durant 10 minutes

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