Impact of mathematical model selection on prediction of steady state and dynamic behaviour of a reactive distillation column
نویسندگان
چکیده
A reactive distillation column in general can exhibit multiple steady states which reduce column operability and controllability during perturbations of manipulated variables and particularly during start-up and shut down. The objective of this paper was to compare the equilibrium (EQ) and nonequilibrium (NEQ) models of a reactive distillation column, focusing on the phenomenon of multiple steady states. In particular, isolated solution branches have been found at several values of chosen reactant feed flow rate, making the column to be prone to operability and control problems. Certain perturbations in the reactants feed flow rate were found to cause transitions between parallel steady states.
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عنوان ژورنال:
- Computers & Chemical Engineering
دوره 33 شماره
صفحات -
تاریخ انتشار 2009