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 |
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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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