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Please use this identifier to cite or link to this item: http://hdl.handle.net/123456789/2533

Title: Dynamic modeling and control of a fluidized bed reactor for the oxidative dehydrogenation of ethylbenzene to styrene
Authors: Ajbar, Abdelhamid
Ali, Emaddine
Keywords: Dynamic modeling
Control
Fluidized bed reactor
Oxidative dehydrogenation
Ethylbenzene
Styrene
Issue Date: 1998
Publisher: King Saud University
Citation: J. King Saud Univ : 10(2); 141-162
Abstract: A dynamical model is proposed for a fluidized bed catalytic reactor for the production of styrene by oxidative dehydrogenation of ethylbenzene. A parametric sensitivity analysis carried out previously (Elnashaie et al., 1991) showed the feasibility of the fluidized bed technology to produce styrene in the reactor on a continuous basis. The static and dynamic bifurcation of the reactor model carried out in this paper shows that the reactor is to be operated in a multiplicity region in order to yield a maximum production rate of styrene.A model predictive control strategy is used with the proposed dynamic model for the tight control of the reactor. The performances of the control algorithm are illustrated for both perfect and imperfect models.
Description: Department of Chemical Engineering, King Saud University, Riyadh, 11421, P.O.Box 800, Kingdom of Saudi Arabia
Department of Chemical Engineering, King Saud University, Riyadh, 11421, P.O.Box 800, Kingdom of Saudi Arabia
URI: http://hdl.handle.net/123456789/2533
Appears in Collections:Journal of the King Saud University - Engineering Sciences

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