The dynamic behaviour of a non-linear process can often be approximated wit
h a time-varying linear model. In the presented methodology the dynamics is
modeled non-conservatively as parametric uncertainty in linear lime invari
ant models. The obtained uncertainty description makes it possible to perfo
rm robustness analysis on a control system using the structured singular va
lue. The idea behind the proposed method is to fit a rational function to t
he parameter variation. The parameter variation can then be expressed as a
linear fractional transformation (LFT), It is discussed how the proposed me
thod can be utilized in identification of a nominal model with uncertainty
description. The method is demonstrated on a binary distillation column ope
rating in the LV configuration. The dynamics of the column is approximated
by a second order linear model, wherein the parameters vary as the operatin
g point changes. It is shown that a diagonal PI control structure provides
robust performance towards variations in feed flow rate or feed concentrati
ons. However including both liquid and vapor flow delays robust performance
specifications cannot be satisfied with this simple diagonal control struc
ture. (C) 1999 Elsevier Science Ltd. All rights reserved.