Customised Simulation Tool For The Industrial Propane Dehydrogenation Reactor

Modeling and simulation of the propane dehydrogenation reaction is important for predicting an optimum operating condition to maximize the propylene yield. The present study performed the modeling and simulation study of propane dehydrogenation over a platinum based catalyst in radial moving bed rea...

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Main Authors:	Chin, S. Y., Haniif, Prasetiawan, Anwaruddin, Hisyam, Abdullah, Azahari, Ikmal Hisham, Maharon
Format:	Conference or Workshop Item
Language:	English
Published:	2014
Subjects:	TP Chemical technology
Online Access:	http://umpir.ump.edu.my/id/eprint/7093/ http://umpir.ump.edu.my/id/eprint/7093/1/fkksa-2014-chin_sim-Customised_Simulation.pdf

id	ump-7093
recordtype	eprints
spelling	ump-70932018-04-18T00:43:59Z http://umpir.ump.edu.my/id/eprint/7093/ Customised Simulation Tool For The Industrial Propane Dehydrogenation Reactor Chin, S. Y. Haniif, Prasetiawan Anwaruddin, Hisyam Abdullah, Azahari Ikmal Hisham, Maharon TP Chemical technology Modeling and simulation of the propane dehydrogenation reaction is important for predicting an optimum operating condition to maximize the propylene yield. The present study performed the modeling and simulation study of propane dehydrogenation over a platinum based catalyst in radial moving bed reactor (RMBR). First order power law model was used to express the propane dehydrogenation reaction and side reactions. RMBR was discretized into axial and radial directions and the equations of the discretized bed were solved numerically. The kinetic parameters were optimized by comparing the simulation results with plant data. The predicted propane conversion, reactor outlet temperature and coke content deviated less than 5% from the plant data. A user friendly graphical user interface (GUI) was developed based on the validated model. GUI can be used easily by the plant personnel for the RMBR simulation. The sensitivity studies were performed to evaluate the inﬂuence of different possible disturbances on the process. It was found that the reactor inlet temperature and H2/HC molar ratio were the most influential parameter to the reactor performance. The maximum propylene yield 30.34% was produced when the WAIT was +10 K, H2/HC was -0.2 and Us was +100 kg/hr from the base case. 2014 Conference or Workshop Item NonPeerReviewed application/pdf en http://umpir.ump.edu.my/id/eprint/7093/1/fkksa-2014-chin_sim-Customised_Simulation.pdf Chin, S. Y. and Haniif, Prasetiawan and Anwaruddin, Hisyam and Abdullah, Azahari and Ikmal Hisham, Maharon (2014) Customised Simulation Tool For The Industrial Propane Dehydrogenation Reactor. In: 2nd National Conference Knowledge Transfer Programme (KTP02), 9-11 September 2014 , Putrajaya Marriot Hotel, Sepang . pp. 1-12..
repository_type	Digital Repository
institution_category	Local University
institution	Universiti Malaysia Pahang
building	UMP Institutional Repository
collection	Online Access
language	English
topic	TP Chemical technology
spellingShingle	TP Chemical technology Chin, S. Y. Haniif, Prasetiawan Anwaruddin, Hisyam Abdullah, Azahari Ikmal Hisham, Maharon Customised Simulation Tool For The Industrial Propane Dehydrogenation Reactor
description	Modeling and simulation of the propane dehydrogenation reaction is important for predicting an optimum operating condition to maximize the propylene yield. The present study performed the modeling and simulation study of propane dehydrogenation over a platinum based catalyst in radial moving bed reactor (RMBR). First order power law model was used to express the propane dehydrogenation reaction and side reactions. RMBR was discretized into axial and radial directions and the equations of the discretized bed were solved numerically. The kinetic parameters were optimized by comparing the simulation results with plant data. The predicted propane conversion, reactor outlet temperature and coke content deviated less than 5% from the plant data. A user friendly graphical user interface (GUI) was developed based on the validated model. GUI can be used easily by the plant personnel for the RMBR simulation. The sensitivity studies were performed to evaluate the inﬂuence of different possible disturbances on the process. It was found that the reactor inlet temperature and H2/HC molar ratio were the most influential parameter to the reactor performance. The maximum propylene yield 30.34% was produced when the WAIT was +10 K, H2/HC was -0.2 and Us was +100 kg/hr from the base case.
format	Conference or Workshop Item
author	Chin, S. Y. Haniif, Prasetiawan Anwaruddin, Hisyam Abdullah, Azahari Ikmal Hisham, Maharon
author_facet	Chin, S. Y. Haniif, Prasetiawan Anwaruddin, Hisyam Abdullah, Azahari Ikmal Hisham, Maharon
author_sort	Chin, S. Y.
title	Customised Simulation Tool For The Industrial Propane Dehydrogenation Reactor
title_short	Customised Simulation Tool For The Industrial Propane Dehydrogenation Reactor
title_full	Customised Simulation Tool For The Industrial Propane Dehydrogenation Reactor
title_fullStr	Customised Simulation Tool For The Industrial Propane Dehydrogenation Reactor
title_full_unstemmed	Customised Simulation Tool For The Industrial Propane Dehydrogenation Reactor
title_sort	customised simulation tool for the industrial propane dehydrogenation reactor
publishDate	2014
url	http://umpir.ump.edu.my/id/eprint/7093/ http://umpir.ump.edu.my/id/eprint/7093/1/fkksa-2014-chin_sim-Customised_Simulation.pdf
first_indexed	2023-09-18T22:03:26Z
last_indexed	2023-09-18T22:03:26Z
_version_	1777414550692298752

Customised Simulation Tool For The Industrial Propane Dehydrogenation Reactor

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