Different hydrodynamic model for gas-phase propylene polymemation in a catalytic fluidized bed reactor

A comparative simulation study was carried out using the improved well-mixed, constant bubble size and well mixed models. These fluidized bed reactor models, combined with comprehensive kinetics for propylene homo-polymerization in the presence of a multiple active site Ziegler-Natta catalyst. In th...

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Main Authors:	Shamiri, A., Hussain, M.A., Mjalli, F.S., Mostoufi, N.
Format:	Conference or Workshop Item
Published:	2010
Subjects:	TA Engineering (General). Civil engineering (General) TP Chemical technology
Online Access:	http://www.scopus.com/inward/record.url?eid=2-s2.0-78651418585&partnerID=40&md5=c6f9d7f0c2f456aa71fbd795ba0e6dfe http://www.scopus.com/inward/record.url?eid=2-s2.0-78651418585&partnerID=40&md5=c6f9d7f0c2f456aa71fbd795ba0e6dfe http://eprints.um.edu.my/7024/1/Different_hydrodynamic_model_for_gas%2Dphase_propylene_polymemation_in_a_catalytic_fluidized_bed_reactor.pdf

id	um-7024
recordtype	eprints
spelling	um-70242014-12-19T02:47:16Z Different hydrodynamic model for gas-phase propylene polymemation in a catalytic fluidized bed reactor Shamiri, A. Hussain, M.A. Mjalli, F.S. Mostoufi, N. TA Engineering (General). Civil engineering (General) TP Chemical technology A comparative simulation study was carried out using the improved well-mixed, constant bubble size and well mixed models. These fluidized bed reactor models, combined with comprehensive kinetics for propylene homo-polymerization in the presence of a multiple active site Ziegler-Natta catalyst. In the improved model, the effect of the presence of particles in the bubbles and the excess gas in the emulsion phase was taken into account to improve the quantitative understanding of the actual fluidized bed process. The superficial gas velocity and catalyst feed rate have a strong effect on the hydrodynamics and reaction rate, which results in a greater variation in the polymer production rate and reactor temperature. At typical operating conditions the improved well mixed and well mixed models were in good agreement. While the COO!ICU bubble size model was found to over-predict the emulsion phase temperature and underpredict propylene concentration. 2010 Conference or Workshop Item PeerReviewed application/pdf http://eprints.um.edu.my/7024/1/Different_hydrodynamic_model_for_gas%2Dphase_propylene_polymemation_in_a_catalytic_fluidized_bed_reactor.pdf http://www.scopus.com/inward/record.url?eid=2-s2.0-78651418585&partnerID=40&md5=c6f9d7f0c2f456aa71fbd795ba0e6dfe Shamiri, A.; Hussain, M.A.; Mjalli, F.S.; Mostoufi, N. (2010) Different hydrodynamic model for gas-phase propylene polymemation in a catalytic fluidized bed reactor. In: 2nd International Conference on Chemical, Biological and Environmental Engineering, ICBEE 2010, 2010, Cairo. http://eprints.um.edu.my/7024/
repository_type	Digital Repository
institution_category	Local University
institution	University Malaya
building	UM Research Repository
collection	Online Access
topic	TA Engineering (General). Civil engineering (General) TP Chemical technology
spellingShingle	TA Engineering (General). Civil engineering (General) TP Chemical technology Shamiri, A. Hussain, M.A. Mjalli, F.S. Mostoufi, N. Different hydrodynamic model for gas-phase propylene polymemation in a catalytic fluidized bed reactor
description	A comparative simulation study was carried out using the improved well-mixed, constant bubble size and well mixed models. These fluidized bed reactor models, combined with comprehensive kinetics for propylene homo-polymerization in the presence of a multiple active site Ziegler-Natta catalyst. In the improved model, the effect of the presence of particles in the bubbles and the excess gas in the emulsion phase was taken into account to improve the quantitative understanding of the actual fluidized bed process. The superficial gas velocity and catalyst feed rate have a strong effect on the hydrodynamics and reaction rate, which results in a greater variation in the polymer production rate and reactor temperature. At typical operating conditions the improved well mixed and well mixed models were in good agreement. While the COO!ICU bubble size model was found to over-predict the emulsion phase temperature and underpredict propylene concentration.
format	Conference or Workshop Item
author	Shamiri, A. Hussain, M.A. Mjalli, F.S. Mostoufi, N.
author_facet	Shamiri, A. Hussain, M.A. Mjalli, F.S. Mostoufi, N.
author_sort	Shamiri, A.
title	Different hydrodynamic model for gas-phase propylene polymemation in a catalytic fluidized bed reactor
title_short	Different hydrodynamic model for gas-phase propylene polymemation in a catalytic fluidized bed reactor
title_full	Different hydrodynamic model for gas-phase propylene polymemation in a catalytic fluidized bed reactor
title_fullStr	Different hydrodynamic model for gas-phase propylene polymemation in a catalytic fluidized bed reactor
title_full_unstemmed	Different hydrodynamic model for gas-phase propylene polymemation in a catalytic fluidized bed reactor
title_sort	different hydrodynamic model for gas-phase propylene polymemation in a catalytic fluidized bed reactor
publishDate	2010
url	http://www.scopus.com/inward/record.url?eid=2-s2.0-78651418585&partnerID=40&md5=c6f9d7f0c2f456aa71fbd795ba0e6dfe http://www.scopus.com/inward/record.url?eid=2-s2.0-78651418585&partnerID=40&md5=c6f9d7f0c2f456aa71fbd795ba0e6dfe http://eprints.um.edu.my/7024/1/Different_hydrodynamic_model_for_gas%2Dphase_propylene_polymemation_in_a_catalytic_fluidized_bed_reactor.pdf
first_indexed	2018-09-06T05:23:23Z
last_indexed	2018-09-06T05:23:23Z
_version_	1610834409449062400

Different hydrodynamic model for gas-phase propylene polymemation in a catalytic fluidized bed reactor

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