In this work, proper operation and improved control of a heterogeneous azeo
tropic distillation of isopropyl alcohol (IPA) + water (H2O) with cyclohexa
ne (CyH) as an entrainer were investigated. A simple operating procedure un
der inverse double loop control strategy is proposed to automatically adjus
t the manipulated variables to be at optimum operating point. A simple one-
way decoupling control scheme is also proposed to account for the high inte
ractions between two temperature control loops. Both feed rate and composit
ion load disturbances will be introduced to test the proposed decoupling co
ntrol scheme. (C) 2000 Elsevier Science Ltd. All rights reserved.