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Plant-model mismatch analysis in deethyleniser simulation. 1. Methodology

journal contribution
posted on 2024-10-31, 23:50 authored by Anthony Kamphausen, John O'Donnell
Confidence in the accuracy of a simulation model and by implication the thermodynamic data model(s) used, particularly for separation equipment such as a deethyleniser, requires validation against actual plant operating data. A methodology has been developed that quantifies plant-model mismatch with a Calculator module appended to a PROM (Simulation Sciences, Inc.) Column module to facilitate an assessment of the relative accuracy of alternative simulation model formulations. The methodology is based on a manual stepwise optimization procedure using a preferred formulation of the simulation model with the key adjustable modeling parameter defined as the effective average equilibrium tray efficiency eta(i)(eff). The methodology seeks to minimize an Error Objective Function that calculates the sum of the weighted and variance-normalized least-squares errors around the deethyleniser involving as many plant measurements as practical taking into account the wide range of accuracy inherent in the various measurements.

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    ISSN - Is published in 08885885

Journal

Industrial and Engineering Chemistry Research

Volume

43

Issue

21

Start page

6680

End page

6693

Total pages

14

Publisher

American Chemical Society

Place published

USA

Language

English

Copyright

Copyright © 2004 American Chemical Society

Former Identifier

2004000970

Esploro creation date

2020-06-22

Fedora creation date

2009-02-27

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