“…is embodied by a pair of nonlinear differential equations for each column stage (ie, composition and liquid flowrate equations). These equations can be integrated directly using a numerical technique, although for the purposes of control studies many authors prefer to use local linearisation, which permits the use of analog computers 17,18,28,30 The performance of the equations has been checked experimentally.4, i6-is, 30, 3i 1 Where plate design is such that liquid overflow does not conform to (12) Although gas flow dynamics may be considered fast, gas flowrate may still have a significant effect on liquid flowrate and holdup.4 In terms of modelling this involves a modification to Eqn (13) which on linearisation might produce a relationship of the form Ln = ~t Mm '~ ~2 G ... (21 ) The mechanism involved is not well-understood, but an increase in vapour flowrate during distillation can reduce liquid overflow from some columns which may result in an inverse response in composition. This phenomenon has been modelled and simulated by both Luyben29 and Stainthorp63 in the course of studying the control of such systems.…”