The influence of catalyst flow rate and superficial gas velocity on the modified two‐phase model for propylene polymerization in a gas‐phase fluidized bed reactor-Reference-Cited by-同舟云学术

The influence of catalyst flow rate and superficial gas velocity on the modified two‐phase model for propylene polymerization in a gas‐phase fluidized bed reactor

Published:2021-03-10 Issue:8 Volume:99 Page:1745-1757
ISSN:0008-4034
Container-title:The Canadian Journal of Chemical Engineering
language:en
Short-container-title:Can J Chem Eng

Author:

Atan Mohd Farid¹²^ORCID,Hussain Mohd Azlan¹,Shamiri Ahmad³

Affiliation:

1. Department of Chemical Engineering Faculty of Engineering, University of Malaya Kuala Lumpur Malaysia

2. Department of Chemical Engineering and Energy Sustainability Faculty of Engineering, Universiti Malaysia Sarawak Kota Samarahan Malaysia

3. Dyno Nobel Moranbah Moranbah QLD Australia

Publisher

Wiley

Subject

General Chemical Engineering

Link

https://onlinelibrary.wiley.com/doi/pdf/10.1002/cjce.24021

Reference52 articles.

1. Advances in Mathematical Modeling of Gas-Phase Olefin Polymerization

2. Dynamic modeling and Molecular Weight Distribution of ethylene copolymerization in an industrial gas-phase Fluidized-Bed Reactor

3. Large-Scale Parameter Estimation in Low-Density Polyethylene Tubular Reactors

4. Mathematical Modeling of the Reactive Modification of High−Density Polyethylene. Effect of Vinyl Content

5. Steady-State and Dynamic Modeling of Gas-Phase Polypropylene Processes Using Stirred-Bed Reactors

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