Abbasi, M.R. and Shamiri, Ahmad and Hussain, Mohd Azlan (2016) Dynamic modeling and Molecular Weight Distribution of ethylene copolymerization in an industrial gas-phase Fluidized-Bed Reactor. Advanced Powder Technology, 27 (4). pp. 1526-1538. ISSN 0921-8831, DOI https://doi.org/10.1016/j.apt.2016.05.014.
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Abstract
A dynamic model for ethylene copolymerization in an industrial Fluidized-Bed Reactor (FBR) is developed to describe its behavior and calculate the properties of polyethylene. The presented model considers particle entrainment and polymerization reaction in two phases. Two-site kinetic and hydrodynamic models in combination, provide a comprehensive model for the gas phase fluidized-bed polyethylene production reactor. The governing moment and hydrodynamic differential equations were solved simultaneously and the results compared with a similar work, as well as industrial data. The dynamic model showed accurate results for predicting Polydispersity Index (PDI), Molecular Weight Distribution (MWD), reactor temperature and polymer production rate.
Item Type: | Article |
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Funders: | High Impact Research Grant, Postgraduate Research Grant (PPP) |
Additional Information: | Dynamic modeling Molecular Weight Distribution ethylene copolymerization industrial gas phase Fluidized Bed Reactor model FBR polyethylene particle entrainment polymerization reaction two phases Two site kinetic hydrodynamic models moment hydrodynamic differential equations Polydispersity Index PDI MWD |
Uncontrolled Keywords: | Polyethylene; Molecular Weight Distribution; Fluidized-Bed Reactor; Dynamic modeling; Solid elutriation |
Subjects: | T Technology > TP Chemical technology |
Divisions: | Faculty of Engineering > School of Engineering Sciences |
Depositing User: | Mr Mohammad Reza Abbasi |
Date Deposited: | 07 Aug 2017 02:37 |
Last Modified: | 10 Feb 2021 03:59 |
URI: | http://eprints.um.edu.my/id/eprint/17640 |
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