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Advances in Mathematical Modeling of Gas-Phase Olefin Polymerization

1
Department of Chemical Engineering, Faculty of Engineering, University of Malaya, 50603 Kuala Lumpur, Malaysia
2
Department of Chemical Engineering and Energy Sustainability, Faculty of Engineering, Universiti Malaysia Sarawak, 94300 Kota Samarahan, Malaysia
*
Author to whom correspondence should be addressed.
Processes 2019, 7(2), 67; https://doi.org/10.3390/pr7020067
Received: 31 December 2018 / Revised: 25 January 2019 / Accepted: 26 January 2019 / Published: 30 January 2019
(This article belongs to the Special Issue Computational Methods for Polymers)
Mathematical modeling of olefin polymerization processes has advanced significantly, driven by factors such as the need for higher-quality end products and more environmentally-friendly processes. The modeling studies have had a wide scope, from reactant and catalyst characterization and polymer synthesis to model validation with plant data. This article reviews mathematical models developed for olefin polymerization processes. Coordination and free-radical mechanisms occurring in different types of reactors, such as fluidized bed reactor (FBR), horizontal-stirred-bed reactor (HSBR), vertical-stirred-bed reactor (VSBR), and tubular reactor are reviewed. A guideline for the development of mathematical models of gas-phase olefin polymerization processes is presented. View Full-Text
Keywords: modeling; olefin; gas phase; kinetics modeling; olefin; gas phase; kinetics
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Atan, M.F.; Hussain, M.A.; Abbasi, M.R.; Khan, M.J.H.; Fazly Abdul Patah, M. Advances in Mathematical Modeling of Gas-Phase Olefin Polymerization. Processes 2019, 7, 67.

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