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A new controlled polymerization reactor is introduced.
The proposed approach is applied to control a jacketed styrene polymerization reactor.
This is evaluated by a case study of a polymerization reactor.
The effectiveness of the proposed method is illustrated through simulations on a nonlinear polymerization reactor.
Two industrial systems are studied by simulation: styrene polymerization reactor and fluid catalytic cracking (FCC) unit.
A literature example and an industrial polymerization reactor are treated to illustrate these properties.
The KBS was evaluated using simulation studies with a polymerization reactor through a nonlinear dynamic model.
The utility of the proposed approach is demonstrated on an isothermal polymerization reactor case study.
The length-scales involved in a typical heterogeneously catalyzed fluid-bed polymerization reactor.
In this paper, an optimal control policy applied to a batch methyl methacrylate polymerization reactor is presented.
In this research, the HNNRF modeling capability over a large operating region was evaluated employing a simulated polymerization reactor system.
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