Advances in Mathematical Modeling of Gas-Phase Olefin Polymerization

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 syn...

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Veröffentlicht in:Processes 2019-02, Vol.7 (2), p.67
Hauptverfasser: Atan, Mohd Farid, Hussain, Mohd Azlan, Abbasi, Mohammad Reza, Khan, Mohammad Jakir Hossain, Fazly Abdul Patah, Muhamad
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container_issue 2
container_start_page 67
container_title Processes
container_volume 7
creator Atan, Mohd Farid
Hussain, Mohd Azlan
Abbasi, Mohammad Reza
Khan, Mohammad Jakir Hossain
Fazly Abdul Patah, Muhamad
description 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.
doi_str_mv 10.3390/pr7020067
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title Advances in Mathematical Modeling of Gas-Phase Olefin Polymerization
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