Simulation Of Maleic Anhydride Production In Fixed Bed Reactor

In this study, simulation of partial oxidation n-butane was developed. Aspen Plus V8.8 was used for stimulated, analysed, and optimized process partial oxidation of n-butane and oxygen. N-butane feed to RPLUG model is equal to 0.0075 mole fraction and 0.21 mole fraction of oxygen which is rich oxyge...

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Main Author: Talib, Amirul Hakim Abd
Format: Monograph
Language:English
Published: Universiti Sains Malaysia 2017
Subjects:
Online Access:http://eprints.usm.my/53287/
http://eprints.usm.my/53287/1/Simulation%20Of%20Maleic%20Anhydride%20Production%20In%20Fixed%20Bed%20Reactor_Amirul%20Hakim%20Abd%20Talib_K4_2017.pdf
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author Talib, Amirul Hakim Abd
author_facet Talib, Amirul Hakim Abd
author_sort Talib, Amirul Hakim Abd
building USM Institutional Repository
collection Online Access
description In this study, simulation of partial oxidation n-butane was developed. Aspen Plus V8.8 was used for stimulated, analysed, and optimized process partial oxidation of n-butane and oxygen. N-butane feed to RPLUG model is equal to 0.0075 mole fraction and 0.21 mole fraction of oxygen which is rich oxygen state. Temperature and pressure of feed streams are set at 379.85°C and 1.6 atm. Diameter for reactor is 0.0025 m and length with 1.0 m. Catalyst used in the simulation is vanadium phosphorus oxide. Simulation of Aspen model was compare with literature to validate. Sensitivity was carried out with three different condition which is temperature, pressure, and feed flow rate. In optimization, the objective function is to maximize conversion of n-butane. The optimization give optimum value which is molar flow rate n-butane in at 0.001 kmol/hr and reactor temperature at 550°C.
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format Monograph
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institution Universiti Sains Malaysia
institution_category Local University
language English
last_indexed 2025-11-15T18:35:41Z
publishDate 2017
publisher Universiti Sains Malaysia
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spelling usm-532872022-07-05T10:29:52Z http://eprints.usm.my/53287/ Simulation Of Maleic Anhydride Production In Fixed Bed Reactor Talib, Amirul Hakim Abd T Technology TP155-156 Chemical engineering In this study, simulation of partial oxidation n-butane was developed. Aspen Plus V8.8 was used for stimulated, analysed, and optimized process partial oxidation of n-butane and oxygen. N-butane feed to RPLUG model is equal to 0.0075 mole fraction and 0.21 mole fraction of oxygen which is rich oxygen state. Temperature and pressure of feed streams are set at 379.85°C and 1.6 atm. Diameter for reactor is 0.0025 m and length with 1.0 m. Catalyst used in the simulation is vanadium phosphorus oxide. Simulation of Aspen model was compare with literature to validate. Sensitivity was carried out with three different condition which is temperature, pressure, and feed flow rate. In optimization, the objective function is to maximize conversion of n-butane. The optimization give optimum value which is molar flow rate n-butane in at 0.001 kmol/hr and reactor temperature at 550°C. Universiti Sains Malaysia 2017-05-01 Monograph NonPeerReviewed application/pdf en http://eprints.usm.my/53287/1/Simulation%20Of%20Maleic%20Anhydride%20Production%20In%20Fixed%20Bed%20Reactor_Amirul%20Hakim%20Abd%20Talib_K4_2017.pdf Talib, Amirul Hakim Abd (2017) Simulation Of Maleic Anhydride Production In Fixed Bed Reactor. Project Report. Universiti Sains Malaysia, Pusat Pengajian Kejuruteraan Kimia. (Submitted)
spellingShingle T Technology
TP155-156 Chemical engineering
Talib, Amirul Hakim Abd
Simulation Of Maleic Anhydride Production In Fixed Bed Reactor
title Simulation Of Maleic Anhydride Production In Fixed Bed Reactor
title_full Simulation Of Maleic Anhydride Production In Fixed Bed Reactor
title_fullStr Simulation Of Maleic Anhydride Production In Fixed Bed Reactor
title_full_unstemmed Simulation Of Maleic Anhydride Production In Fixed Bed Reactor
title_short Simulation Of Maleic Anhydride Production In Fixed Bed Reactor
title_sort simulation of maleic anhydride production in fixed bed reactor
topic T Technology
TP155-156 Chemical engineering
url http://eprints.usm.my/53287/
http://eprints.usm.my/53287/1/Simulation%20Of%20Maleic%20Anhydride%20Production%20In%20Fixed%20Bed%20Reactor_Amirul%20Hakim%20Abd%20Talib_K4_2017.pdf