Modeling and Simulation Study of an Industrial Radial Moving Bed Reactor for Propane Dehydrogenation Process

An accurate model is required to optimize the propane dehydrogenation reaction carried out in the radial moving bed reactors (RMBR). The present study modeled the RMBR using a plug flow reactor model incorporated with kinetic models expressed in simple power-law model. Catalyst activity and coke for...

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Main Authors: Chin, S. Y., Anwaruddin, Hisyam, Haniif, Prasetiawan
Format: Article
Language:English
English
Published: De Gruyter 2016
Subjects:
Online Access:http://umpir.ump.edu.my/id/eprint/13431/
http://umpir.ump.edu.my/id/eprint/13431/1/Modeling%20and%20Simulation%20Study%20of%20an%20Industrial%20Radial%20Moving%20Bed%20Reactor%20for%20Propane%20Dehydrogenation%20Process.pdf
http://umpir.ump.edu.my/id/eprint/13431/7/fkksa-sim-2016-Modeling%20and%20Simulation%20Study%20of%20an%20Industrial1.pdf
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author Chin, S. Y.
Anwaruddin, Hisyam
Haniif, Prasetiawan
author_facet Chin, S. Y.
Anwaruddin, Hisyam
Haniif, Prasetiawan
author_sort Chin, S. Y.
building UMP Institutional Repository
collection Online Access
description An accurate model is required to optimize the propane dehydrogenation reaction carried out in the radial moving bed reactors (RMBR). The present study modeled the RMBR using a plug flow reactor model incorporated with kinetic models expressed in simple power-law model. Catalyst activity and coke formation were also considered. The model was solved numerically by discretizing the RMBR in axial and radial directions. The optimized kinetic parameters were then used to predict the trends of propane conversion, temperature, catalyst activity and coke content in the RMBR along axial and radial directions. It was found that the predicted activation energies of the propane dehydrogenation, propane cracking and ethylene hydrogenation were in reasonable agreement with the experimental values reported in the literature. The model developed has accurately predicted the reaction temperature profile, conversion profile and catalyst coke content. The deviations of these simulated results from the plant data were less than 5%.
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English
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publishDate 2016
publisher De Gruyter
recordtype eprints
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spelling ump-134312017-12-14T02:09:53Z http://umpir.ump.edu.my/id/eprint/13431/ Modeling and Simulation Study of an Industrial Radial Moving Bed Reactor for Propane Dehydrogenation Process Chin, S. Y. Anwaruddin, Hisyam Haniif, Prasetiawan TP Chemical technology An accurate model is required to optimize the propane dehydrogenation reaction carried out in the radial moving bed reactors (RMBR). The present study modeled the RMBR using a plug flow reactor model incorporated with kinetic models expressed in simple power-law model. Catalyst activity and coke formation were also considered. The model was solved numerically by discretizing the RMBR in axial and radial directions. The optimized kinetic parameters were then used to predict the trends of propane conversion, temperature, catalyst activity and coke content in the RMBR along axial and radial directions. It was found that the predicted activation energies of the propane dehydrogenation, propane cracking and ethylene hydrogenation were in reasonable agreement with the experimental values reported in the literature. The model developed has accurately predicted the reaction temperature profile, conversion profile and catalyst coke content. The deviations of these simulated results from the plant data were less than 5%. De Gruyter 2016-02 Article PeerReviewed application/pdf en http://umpir.ump.edu.my/id/eprint/13431/1/Modeling%20and%20Simulation%20Study%20of%20an%20Industrial%20Radial%20Moving%20Bed%20Reactor%20for%20Propane%20Dehydrogenation%20Process.pdf application/pdf en http://umpir.ump.edu.my/id/eprint/13431/7/fkksa-sim-2016-Modeling%20and%20Simulation%20Study%20of%20an%20Industrial1.pdf Chin, S. Y. and Anwaruddin, Hisyam and Haniif, Prasetiawan (2016) Modeling and Simulation Study of an Industrial Radial Moving Bed Reactor for Propane Dehydrogenation Process. International Journal of Chemical Reactor Engineering, 14 (1). pp. 33-44. ISSN 2194-5748 (Print); 1542-6580 (Online). (Published) https://doi.org/10.1515/ijcre-2014-0148 DOI: 10.1515/ijcre-2014-0148
spellingShingle TP Chemical technology
Chin, S. Y.
Anwaruddin, Hisyam
Haniif, Prasetiawan
Modeling and Simulation Study of an Industrial Radial Moving Bed Reactor for Propane Dehydrogenation Process
title Modeling and Simulation Study of an Industrial Radial Moving Bed Reactor for Propane Dehydrogenation Process
title_full Modeling and Simulation Study of an Industrial Radial Moving Bed Reactor for Propane Dehydrogenation Process
title_fullStr Modeling and Simulation Study of an Industrial Radial Moving Bed Reactor for Propane Dehydrogenation Process
title_full_unstemmed Modeling and Simulation Study of an Industrial Radial Moving Bed Reactor for Propane Dehydrogenation Process
title_short Modeling and Simulation Study of an Industrial Radial Moving Bed Reactor for Propane Dehydrogenation Process
title_sort modeling and simulation study of an industrial radial moving bed reactor for propane dehydrogenation process
topic TP Chemical technology
url http://umpir.ump.edu.my/id/eprint/13431/
http://umpir.ump.edu.my/id/eprint/13431/
http://umpir.ump.edu.my/id/eprint/13431/
http://umpir.ump.edu.my/id/eprint/13431/1/Modeling%20and%20Simulation%20Study%20of%20an%20Industrial%20Radial%20Moving%20Bed%20Reactor%20for%20Propane%20Dehydrogenation%20Process.pdf
http://umpir.ump.edu.my/id/eprint/13431/7/fkksa-sim-2016-Modeling%20and%20Simulation%20Study%20of%20an%20Industrial1.pdf