Atan, MF;
Hussain, MA;
Abbasi, MR;
Khan, MJH;
Patah, MFA;
(2019)
Advances in Mathematical Modeling of Gas-Phase Olefin Polymerization.
Processes
, 7
(2)
, Article 67. 10.3390/pr7020067.
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Abstract
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.
Type: | Article |
---|---|
Title: | Advances in Mathematical Modeling of Gas-Phase Olefin Polymerization |
Open access status: | An open access version is available from UCL Discovery |
DOI: | 10.3390/pr7020067 |
Publisher version: | https://doi.org/10.3390/pr7020067 |
Language: | English |
Additional information: | This is an open access article distributed under the Creative Commons Attribution License (https://creativecommons.org/licenses/by/4.0/) which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited. |
Keywords: | modeling; olefin; gas phase; kinetics |
UCL classification: | UCL UCL > Provost and Vice Provost Offices > UCL BEAMS UCL > Provost and Vice Provost Offices > UCL BEAMS > Faculty of Engineering Science UCL > Provost and Vice Provost Offices > UCL BEAMS > Faculty of Engineering Science > Dept of Chemical Engineering |
URI: | https://discovery.ucl.ac.uk/id/eprint/10116867 |




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