Dynamic modelling of a stopped flow fixed bed reactor for gas phase olefin polymerisation-Reference-Cited by-同舟云学术

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Dynamic modelling of a stopped flow fixed bed reactor for gas phase olefin polymerisation

Published:2012-10 Issue: Volume:207-208 Page:635-644
ISSN:1385-8947
Container-title:Chemical Engineering Journal
language:en
Short-container-title:Chemical Engineering Journal

Author:

Browning B.,Pitault I.,Sheibat-Othman N.,Tioni E.,Monteil V.,McKenna T.F.L.

Publisher

Elsevier BV

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,Environmental Chemistry,General Chemistry

Reference31 articles.

1. Polyethylene Market to 2020, GBI Research, 2011.

2. Particle growth during the polmerisation of olefins on supported catalysts, 1 – nascent polymer structures;McKenna;Macromol. React. Eng.,2010

3. Single particle modelling for polyolefins: a review;McKenna;Chem. Eng. Sci.,2001

4. Catalyst fragmentation during polypropylene polymerization: part 1. The effects of grain size and structure;Ferrero;Polym. Eng. Sci.,1987

5. A structural model for the catalytic polymerization of ethylene using chromium catalysts. Part I: Description and solution;Estenoz;Polym. Eng. Sci.,1996

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1. Optimization and safety analysis for CO oxidative coupling reactor with co-current thermal management;Chemical Engineering Science;2024-12

2. Polymerization of ethylene in the gas phase—A new combined hardware and software tool;The Canadian Journal of Chemical Engineering;2022-05-04

3. Modified two-phase model with hybrid control for gas phase propylene copolymerization in fluidized bed reactors;Chemical Engineering Journal;2015-03

4. A 2-D observer to estimate the reaction rate in a stopped flow fixed bed reactor for gas phase olefin polymerization;AIChE Journal;2014-07-05

5. Influence of Reaction Conditions on Catalyst Behavior during the Early Stages of Gas Phase Ethylene Homo- and Copolymerization;Industrial & Engineering Chemistry Research;2012-10-31

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