The Canadian Journal of Chemical Engineering · 1985 · 20 citations · 8 references
EngineeringChemical EngineeringDynamical SystemsProcess DynamicsProcess Systems EngineeringDistillationDynamic SimulationDynamic Systems AnalysisMultivariable Process DynamicsNonlinear DynamicsNonlinear Process DynamicsColumn DesignDistillation Column ModelingDynamic Transient BehaviorMulticomponent Distillation
Abstract The dynamic behavior of an existing industrial distillation column with eight components and twenty trays has been investigated. The column exhibits “asymmetric dynamics”, since the time required to move from one steady state to another can vary significantly depending on the direction of the change. The column also exhibits highly nonlinear behavior and very long response times for intermediate ranges of step disturbances. These long response times are associated with the migration of key components through the column.
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