Two-point control of a reactive distillation column for composition and conversion |
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Authors: | Martin G. Sneesby Moses O. Tade Terence N. Smith |
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Affiliation: | ag School of Chemical Engineering, Curtin University of Technology, Perth, Western Australia |
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Abstract: | Reactive distillation is a hybrid process with dual process objectives: reactant conversion and product composition. Control schemes for reactive distillation frequently neglect the effect of the principal operating parameters on the reactant conversion, and this has a detrimental effect on the overall process profitability. An ETBE reactive distillation column has been used as a case study to show how a two-point control configuration, which recognises the importance of both composition and conversion, can be developed and implemented for a reactive distillation process. The combined composition and conversion control configuration was tested using SpeedUp dynamic simulations and proved to be effective in maintaining a high isobutylene conversion despite process disturbances. The two-point control scheme also had superior disturbance rejection capability, especially for feed rate changes, and composition set-point sensitivity compared with a one-point control scheme. |
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Keywords: | Reactive distillation Two-point control Inferential model |
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