EXTRAPOLATION PERFORMANCE OF DYNAMIC MODELS FOR A CONTINUOUS DISTILLATION COLUMN

Modelling has always played an important role in the process engmeermg. An important characteristic of any model is its ability to extrapolate beyond the operating regions that were used for the model development. White - box models, which built based on fundamental laws, are generally expecte...

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Main Author: HOANG, SON TRUONG
Format: Thesis
Language:English
Published: 2012
Subjects:
Online Access:http://utpedia.utp.edu.my/21127/1/2012%20-%20ELECTRICAL%20AND%20ELECTRONIC-EXTRAPOLATION%20PERFORMANCE%20OF%20DYNAMIC%20MODELS%20FOR%20A%20CONTINOUS%20DISTILLATION%20COLUMN-HOANG%20SON%20TRUONG.pdf
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spelling my-utp-utpedia.211272021-09-15T20:08:26Z http://utpedia.utp.edu.my/21127/ EXTRAPOLATION PERFORMANCE OF DYNAMIC MODELS FOR A CONTINUOUS DISTILLATION COLUMN HOANG, SON TRUONG Instrumentation and Control Modelling has always played an important role in the process engmeermg. An important characteristic of any model is its ability to extrapolate beyond the operating regions that were used for the model development. White - box models, which built based on fundamental laws, are generally expected to have better extrapolation performance than the empirical - based, (or black - box) models. However, this expectation is vague for there have been no experimental proof and quantitative analysis on a real, complex process. This thesis was aimed to provide a clear understanding with experimental proof on the extrapolation performances of black - box and white - box models. First, a rigorous white - box model of a pilot - scale continuous distillation column was developed based on conservation laws of mass and energy. The model has nine unknown parameters that need to be estimated. The unknown parameters were categorized into static (six parameters) and dynamic (three parameters) for the ease of the estimation. Second, black- box models of autoregressive with exogenous input (ARX) and state - space structures were selected with a quantitative criterion for selection. Two experiments were carefully designed and carried out on the distillation column to collect data for parameter estimation and validation of the models. Finally, analysis and comparison of the models' performances, with emphasis on the extrapolation performance of the models, were carried out. Four ARX and five state- space models were selected based on the average fit indexes of the models' simulated outputs against validation data. The white - box model outperforms the black- box models with 69.1% average fit to validation data, while the best black- box model could only produce 59.2% average fit. However, in terms of extrapolation performance the white - box model is the worst with negative average fit indexes for both sets of extrapolation data (-16.4% and -19.94%), while a state- space model produces the best fit results (55.76% and 53.11 %). 2012-01 Thesis NonPeerReviewed application/pdf en http://utpedia.utp.edu.my/21127/1/2012%20-%20ELECTRICAL%20AND%20ELECTRONIC-EXTRAPOLATION%20PERFORMANCE%20OF%20DYNAMIC%20MODELS%20FOR%20A%20CONTINOUS%20DISTILLATION%20COLUMN-HOANG%20SON%20TRUONG.pdf HOANG, SON TRUONG (2012) EXTRAPOLATION PERFORMANCE OF DYNAMIC MODELS FOR A CONTINUOUS DISTILLATION COLUMN. Masters thesis, Universiti Teknologi PETRONAS.
institution Universiti Teknologi Petronas
building UTP Resource Centre
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Petronas
content_source UTP Electronic and Digitized Intellectual Asset
url_provider http://utpedia.utp.edu.my/
language English
topic Instrumentation and Control
spellingShingle Instrumentation and Control
HOANG, SON TRUONG
EXTRAPOLATION PERFORMANCE OF DYNAMIC MODELS FOR A CONTINUOUS DISTILLATION COLUMN
description Modelling has always played an important role in the process engmeermg. An important characteristic of any model is its ability to extrapolate beyond the operating regions that were used for the model development. White - box models, which built based on fundamental laws, are generally expected to have better extrapolation performance than the empirical - based, (or black - box) models. However, this expectation is vague for there have been no experimental proof and quantitative analysis on a real, complex process. This thesis was aimed to provide a clear understanding with experimental proof on the extrapolation performances of black - box and white - box models. First, a rigorous white - box model of a pilot - scale continuous distillation column was developed based on conservation laws of mass and energy. The model has nine unknown parameters that need to be estimated. The unknown parameters were categorized into static (six parameters) and dynamic (three parameters) for the ease of the estimation. Second, black- box models of autoregressive with exogenous input (ARX) and state - space structures were selected with a quantitative criterion for selection. Two experiments were carefully designed and carried out on the distillation column to collect data for parameter estimation and validation of the models. Finally, analysis and comparison of the models' performances, with emphasis on the extrapolation performance of the models, were carried out. Four ARX and five state- space models were selected based on the average fit indexes of the models' simulated outputs against validation data. The white - box model outperforms the black- box models with 69.1% average fit to validation data, while the best black- box model could only produce 59.2% average fit. However, in terms of extrapolation performance the white - box model is the worst with negative average fit indexes for both sets of extrapolation data (-16.4% and -19.94%), while a state- space model produces the best fit results (55.76% and 53.11 %).
format Thesis
author HOANG, SON TRUONG
author_facet HOANG, SON TRUONG
author_sort HOANG, SON TRUONG
title EXTRAPOLATION PERFORMANCE OF DYNAMIC MODELS FOR A CONTINUOUS DISTILLATION COLUMN
title_short EXTRAPOLATION PERFORMANCE OF DYNAMIC MODELS FOR A CONTINUOUS DISTILLATION COLUMN
title_full EXTRAPOLATION PERFORMANCE OF DYNAMIC MODELS FOR A CONTINUOUS DISTILLATION COLUMN
title_fullStr EXTRAPOLATION PERFORMANCE OF DYNAMIC MODELS FOR A CONTINUOUS DISTILLATION COLUMN
title_full_unstemmed EXTRAPOLATION PERFORMANCE OF DYNAMIC MODELS FOR A CONTINUOUS DISTILLATION COLUMN
title_sort extrapolation performance of dynamic models for a continuous distillation column
publishDate 2012
url http://utpedia.utp.edu.my/21127/1/2012%20-%20ELECTRICAL%20AND%20ELECTRONIC-EXTRAPOLATION%20PERFORMANCE%20OF%20DYNAMIC%20MODELS%20FOR%20A%20CONTINOUS%20DISTILLATION%20COLUMN-HOANG%20SON%20TRUONG.pdf
http://utpedia.utp.edu.my/21127/
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score 13.18916