Dynamic Simulation of High Purity Distillation Column

This report presents a research study on dynamic simulation ofhigh purity distillation column via MATLAB.The dynamic nature and the nonlinear behaviour ofdistillation equipment pose challenging control system design when products ofconstant purity are to be recovered. Several alternative column c...

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Main Author: Zubir, Abdullah Baihaqi Adzha
Format: Final Year Project
Language:English
Published: Universiti Teknologi PETRONAS 2009
Subjects:
Online Access:http://utpedia.utp.edu.my/9374/1/2009%20-Dynamic%20Simulation%20Of%20High%20Purity%20Distillation%20Column.pdf
http://utpedia.utp.edu.my/9374/
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spelling my-utp-utpedia.93742013-10-22T12:04:19Z http://utpedia.utp.edu.my/9374/ Dynamic Simulation of High Purity Distillation Column Zubir, Abdullah Baihaqi Adzha TP Chemical technology This report presents a research study on dynamic simulation ofhigh purity distillation column via MATLAB.The dynamic nature and the nonlinear behaviour ofdistillation equipment pose challenging control system design when products ofconstant purity are to be recovered. Several alternative column configurations and operating policies have been studied. However, issues related to the online operation of such process have not been properly addressed. The present work describes the investigation with experimental verification of computer based control strategies to distillation. The scope ofwork for the project is to conduct a literature review on dynamic behaviour of high purity distillation column The study provides a method ofstudying the dynamic behaviour ofcolumn comprising the steps of: a) generating a principle steady state and dynamic model corresponding to the distillation process; b) simulating the dynamic model for different operating condition via MATLAB; c) Develop output trend towards changes in input via Pseudo Random Binary Sequence (PRBS); e) Develop step response of first order process ; and f) obtain the gain and time constant for any changes ofcolumn operating condition through first order process response for control purposes A distillation model with 41-stage column with the overhead condenser as stage 1, the feed tray as stage 21 and the reboiler as stage 41 is used. The findings show that the models represent an ideal distillation column. All the research and findings obtained will be used to improve the overall performance ofthe column as well as to improve the quality ofthe product and maximise profitability. The successful outcome of this project will be a great helping hand for industrial application. IV Universiti Teknologi PETRONAS 2009-06 Final Year Project NonPeerReviewed application/pdf en http://utpedia.utp.edu.my/9374/1/2009%20-Dynamic%20Simulation%20Of%20High%20Purity%20Distillation%20Column.pdf Zubir, Abdullah Baihaqi Adzha (2009) Dynamic Simulation of High Purity Distillation Column. Universiti Teknologi PETRONAS. (Unpublished)
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 TP Chemical technology
spellingShingle TP Chemical technology
Zubir, Abdullah Baihaqi Adzha
Dynamic Simulation of High Purity Distillation Column
description This report presents a research study on dynamic simulation ofhigh purity distillation column via MATLAB.The dynamic nature and the nonlinear behaviour ofdistillation equipment pose challenging control system design when products ofconstant purity are to be recovered. Several alternative column configurations and operating policies have been studied. However, issues related to the online operation of such process have not been properly addressed. The present work describes the investigation with experimental verification of computer based control strategies to distillation. The scope ofwork for the project is to conduct a literature review on dynamic behaviour of high purity distillation column The study provides a method ofstudying the dynamic behaviour ofcolumn comprising the steps of: a) generating a principle steady state and dynamic model corresponding to the distillation process; b) simulating the dynamic model for different operating condition via MATLAB; c) Develop output trend towards changes in input via Pseudo Random Binary Sequence (PRBS); e) Develop step response of first order process ; and f) obtain the gain and time constant for any changes ofcolumn operating condition through first order process response for control purposes A distillation model with 41-stage column with the overhead condenser as stage 1, the feed tray as stage 21 and the reboiler as stage 41 is used. The findings show that the models represent an ideal distillation column. All the research and findings obtained will be used to improve the overall performance ofthe column as well as to improve the quality ofthe product and maximise profitability. The successful outcome of this project will be a great helping hand for industrial application. IV
format Final Year Project
author Zubir, Abdullah Baihaqi Adzha
author_facet Zubir, Abdullah Baihaqi Adzha
author_sort Zubir, Abdullah Baihaqi Adzha
title Dynamic Simulation of High Purity Distillation Column
title_short Dynamic Simulation of High Purity Distillation Column
title_full Dynamic Simulation of High Purity Distillation Column
title_fullStr Dynamic Simulation of High Purity Distillation Column
title_full_unstemmed Dynamic Simulation of High Purity Distillation Column
title_sort dynamic simulation of high purity distillation column
publisher Universiti Teknologi PETRONAS
publishDate 2009
url http://utpedia.utp.edu.my/9374/1/2009%20-Dynamic%20Simulation%20Of%20High%20Purity%20Distillation%20Column.pdf
http://utpedia.utp.edu.my/9374/
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score 13.18916