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...
| Main Authors: | , , , |
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| Format: | Conference or Workshop Item |
| Published: |
2010
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| Subjects: | |
| 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 |
Internet
http://www.scopus.com/inward/record.url?eid=2-s2.0-78651418585&partnerID=40&md5=c6f9d7f0c2f456aa71fbd795ba0e6dfehttp://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