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Modelling for controller design in tray distillation. II. Comparison of lumped and distributed parameter model performance

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2 Author(s)
Tabrizi, M.H.N. ; Univ. of East Carolina, Greenville, NC, USA ; Edwards, J.B.

For pt.I see ibid., p.301-4. An algorithm for fitting the parameters of a fourth-order lumped parameter model (for a column comprising only a single-state rectifier and stripping section) derived in part I, to responses computed for a multitray column, is demonstrated. The multivariable first-order lag approximation of D.H. Owens (1975) is used as a basis for control system design and shown to produce near-identical closed-loop responses. The fitting algorithm is shown also to cope with nonminimum-phase responses generated by packed columns for which the multivariable first-order model is totally inappropriate. The fourth-order lumped parameter model for either type of column therefore provides a good basis for column controller design in general

Published in:
Southeastcon '88., IEEE Conference Proceedings

Date of Conference: 11-13 Apr 1988

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