Article ID Journal Published Year Pages File Type
158428 Chemical Engineering Science 2007 5 Pages PDF
Abstract

The goal of this paper is to provide a controller design for a high-purity distillation column where the effect of uncertainties is taken into account. A structured uncertainty model has been developed which describes the dynamics of the high-purity distillation column for the entire operating range. Further, a two-point composition control scheme using the LV  -configuration is applied which yields acceptable performance specifications. The structured singular value (μ)(μ) is used as a tool for evaluating the achievable control performance which is defined in terms of the H∞H∞-norm of the weighted sensitivity function. In addition, a decentralised PID controller based on internal model control (IMC) scheme that is optimally tuned is found to be robust. The results of simulations show good disturbance rejection and set-point tracking for the controller.

Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
Authors
, ,