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Kinetics Modelling of

Natural gas contains high amounts of impurities that are important to remove for commercial usage. One of these impurities are known to be carbon dioxide and it is the main culprit in degrading the gas. It reduces the energy content of natural gas has as well as speeds up corrosion in pipelines and...

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第一著者: a/l Ranjeet Singh, Hardith Singh Mander
フォーマット: Final Year Project
言語:English
出版事項: IRC 2015
主題:
TP Chemical technology
オンライン･アクセス:http://utpedia.utp.edu.my/15754/1/HARDITH%20SINGH%20MANDER%20DISSERTATION%20FYP.pdf
http://utpedia.utp.edu.my/15754/
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spelling my-utp-utpedia.157542017-01-25T09:36:27Z http://utpedia.utp.edu.my/15754/ Kinetics Modelling of a/l Ranjeet Singh, Hardith Singh Mander TP Chemical technology Natural gas contains high amounts of impurities that are important to remove for commercial usage. One of these impurities are known to be carbon dioxide and it is the main culprit in degrading the gas. It reduces the energy content of natural gas has as well as speeds up corrosion in pipelines and equipment. There are several methods in the removal of this gas one being chemical absorption where the usage of amines are incorporated. In this project, kinetics modelling of blended amine solution of aqueous N-methyldiethanolamine (MDEA) and diethanolamine (DEA) were studied where its behavior was simulated using MATLAB. Determining the reaction rate kinetics and the equilibrium constants enabled us the determination of liquid bulk concentration for the overall system. The kinetics at five different temperatures were observed; 303K, 308K, 313K, 318K and 323K for blended amine solution of different MDEA concentrations (1.0 and 1.5 kmol/m3) and DEA concentrations (0.1, 0.2, 0.3 and 0.4 kmol/m3). The Arrhenius relation, activation energy and reaction rate coefficients were obtained showed promising results at three different randomly selected temperatures; 303K, 308K and 323K, where the condition is at its best at 323K at 0.999952193kmol/m3 of MDEA concentration and 0.999912787kmol/ m3 of DEA concentration. This concludes that the kinetic model developed is valid thus can be further enhanced using different and more sophisticated software to ensure best operating conditions for the solution. IRC 2015-01 Final Year Project NonPeerReviewed application/pdf en http://utpedia.utp.edu.my/15754/1/HARDITH%20SINGH%20MANDER%20DISSERTATION%20FYP.pdf a/l Ranjeet Singh, Hardith Singh Mander (2015) Kinetics Modelling of. IRC, 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
a/l Ranjeet Singh, Hardith Singh Mander
Kinetics Modelling of
description Natural gas contains high amounts of impurities that are important to remove for commercial usage. One of these impurities are known to be carbon dioxide and it is the main culprit in degrading the gas. It reduces the energy content of natural gas has as well as speeds up corrosion in pipelines and equipment. There are several methods in the removal of this gas one being chemical absorption where the usage of amines are incorporated. In this project, kinetics modelling of blended amine solution of aqueous N-methyldiethanolamine (MDEA) and diethanolamine (DEA) were studied where its behavior was simulated using MATLAB. Determining the reaction rate kinetics and the equilibrium constants enabled us the determination of liquid bulk concentration for the overall system. The kinetics at five different temperatures were observed; 303K, 308K, 313K, 318K and 323K for blended amine solution of different MDEA concentrations (1.0 and 1.5 kmol/m3) and DEA concentrations (0.1, 0.2, 0.3 and 0.4 kmol/m3). The Arrhenius relation, activation energy and reaction rate coefficients were obtained showed promising results at three different randomly selected temperatures; 303K, 308K and 323K, where the condition is at its best at 323K at 0.999952193kmol/m3 of MDEA concentration and 0.999912787kmol/ m3 of DEA concentration. This concludes that the kinetic model developed is valid thus can be further enhanced using different and more sophisticated software to ensure best operating conditions for the solution.
format Final Year Project
author a/l Ranjeet Singh, Hardith Singh Mander
author_facet a/l Ranjeet Singh, Hardith Singh Mander
author_sort a/l Ranjeet Singh, Hardith Singh Mander
title Kinetics Modelling of
title_short Kinetics Modelling of
title_full Kinetics Modelling of
title_fullStr Kinetics Modelling of
title_full_unstemmed Kinetics Modelling of
title_sort kinetics modelling of
publisher IRC
publishDate 2015
url http://utpedia.utp.edu.my/15754/1/HARDITH%20SINGH%20MANDER%20DISSERTATION%20FYP.pdf
http://utpedia.utp.edu.my/15754/
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score 13.251813

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