Modeling and Control for a Petroleum Process

This paper introduces a calculation procedure for modeling and control simulation of a condensate distillation column based on the energy balance (L-V) structure. In this control, the reflux rate L and the boilup rate V are used as the inputs to control the outputs of the purity of the distillate ov...

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Main Author: Vu, Trieu Minh
Format: Book Section
Institution: Universiti Teknologi Petronas
Record Id / ISBN-0: utp-eprints.2827 /
Published: Taiwan 2010
Subjects:
T Technology (General)
Online Access: http://eprints.utp.edu.my/2827/1/Scopus.pdf
http://www.scopus.com/record/display.url?eid=2-s2.0-77956043475&origin=inward&txGid=9qbBDksXwkgUmb1OgVllCtJ%3a2
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spelling utp-eprints.28272017-03-20T02:00:00Z Modeling and Control for a Petroleum Process Vu, Trieu Minh T Technology (General) This paper introduces a calculation procedure for modeling and control simulation of a condensate distillation column based on the energy balance (L-V) structure. In this control, the reflux rate L and the boilup rate V are used as the inputs to control the outputs of the purity of the distillate overhead and the impurity of the bottom products. The mathematical modeling simulation is an important part for the process dynamic analysis and the plant initial design. In this paper, the mathematical modeling simulation is accomplished over three phases: the basic nonlinear model of the plant; the full-order linearised model; and the reduced-order linear model. The reduced-order linear model is then used as the reference model for a model-reference adaptive control (MRAC) system to verify the applicable ability of a conventional adaptive controller for a distillation column dealing with the disturbance and the model-plant mismatch as the influence of the plant feed disturbances. Taiwan 2010 Book Section PeerReviewed application/pdf http://eprints.utp.edu.my/2827/1/Scopus.pdf http://www.scopus.com/record/display.url?eid=2-s2.0-77956043475&origin=inward&txGid=9qbBDksXwkgUmb1OgVllCtJ%3a2 Vu, Trieu Minh (2010) Modeling and Control for a Petroleum Process. In: 5th IEEE Conference on Industrial Electronics and Applications (ICIEA 2010). CFP1020A-USB, 2010 (551681). Taiwan, pp. 259-263. ISBN 978-142445046-6 http://eprints.utp.edu.my/2827/
institution Universiti Teknologi Petronas
collection UTP Institutional Repository
topic T Technology (General)
spellingShingle T Technology (General)
Vu, Trieu Minh
Modeling and Control for a Petroleum Process
description This paper introduces a calculation procedure for modeling and control simulation of a condensate distillation column based on the energy balance (L-V) structure. In this control, the reflux rate L and the boilup rate V are used as the inputs to control the outputs of the purity of the distillate overhead and the impurity of the bottom products. The mathematical modeling simulation is an important part for the process dynamic analysis and the plant initial design. In this paper, the mathematical modeling simulation is accomplished over three phases: the basic nonlinear model of the plant; the full-order linearised model; and the reduced-order linear model. The reduced-order linear model is then used as the reference model for a model-reference adaptive control (MRAC) system to verify the applicable ability of a conventional adaptive controller for a distillation column dealing with the disturbance and the model-plant mismatch as the influence of the plant feed disturbances.
format Book Section
author Vu, Trieu Minh
author_sort Vu, Trieu Minh
title Modeling and Control for a Petroleum Process
title_short Modeling and Control for a Petroleum Process
title_full Modeling and Control for a Petroleum Process
title_fullStr Modeling and Control for a Petroleum Process
title_full_unstemmed Modeling and Control for a Petroleum Process
title_sort modeling and control for a petroleum process
publisher Taiwan
publishDate 2010
url http://eprints.utp.edu.my/2827/1/Scopus.pdf
http://www.scopus.com/record/display.url?eid=2-s2.0-77956043475&origin=inward&txGid=9qbBDksXwkgUmb1OgVllCtJ%3a2
http://eprints.utp.edu.my/2827/
_version_ 1741196061631840256
score 11.62408

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