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- W2133834015 abstract "Nonlinear feedback control scheme for reactive distillation column has been proposed. The proposed control scheme is derived in the framework of Nonlinear Internal Model Control. The product compositions and liquid and vapor flow rates in sections of the reactive distillation column are estimated from selected tray temperature measurements by an observer. The control scheme is applied to example reactive distillation column in which two products are produced in a single column and the reversible reaction A + B = C + D occurs. The relative volatilities are favorable for reactive distillation so that the reactants are intermediate boilers between the light product C and the heavy product D. Ideal physical properties, kinetics, and vapor-liquid equilibrium are also assumed. It is shown the proposed control scheme keeps tight product composition control." @default.
- W2133834015 created "2016-06-24" @default.
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- W2133834015 date "2006-01-01" @default.
- W2133834015 modified "2023-10-16" @default.
- W2133834015 title "Nonlinear Model Based Control of Two-Product Reactive Distillation Column" @default.
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- W2133834015 doi "https://doi.org/10.1109/sice.2006.315014" @default.
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