Prediction of Minimum Fluidisation Velocity Using a CFD-PBM Coupled Model in an Industrial Gas Phase Polymerisation Reactor

The objective of this paper is to develop computational fluid dynamic (CFD)- population balance model (PBM) coupled model to predict a minimum fluidisation velocity in industrial polydisperse gas phase linear low-density polyethylene (LLDPE) polymerisation reactor. The population balance model (P...

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Main Authors: Akbari , Vahid, Hamid, Mohd. Kamaruddin Abd.
Format: Article
Language:English
Published: Taylor's University 2014
Subjects:
Online Access:http://eprints.usm.my/42733/1/JES_Vol._10_2014-Art._10-%2895-105%29.pdf
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author Akbari , Vahid
Hamid, Mohd. Kamaruddin Abd.
author_facet Akbari , Vahid
Hamid, Mohd. Kamaruddin Abd.
author_sort Akbari , Vahid
collection USM
description The objective of this paper is to develop computational fluid dynamic (CFD)- population balance model (PBM) coupled model to predict a minimum fluidisation velocity in industrial polydisperse gas phase linear low-density polyethylene (LLDPE) polymerisation reactor. The population balance model (PBM) by direct quadrature method of moment (DQMOM) implemented in CFD framework was used to predict the minimum fluidisation velocity. The simulation results were validated by the operational data in terms of bed height and pressure drop. This CFD-PBM coupled model can be extended to investigate the flow field and particle kinetic through the reactor.
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spelling usm.eprints-427332018-10-25T08:33:57Z http://eprints.usm.my/42733/ Prediction of Minimum Fluidisation Velocity Using a CFD-PBM Coupled Model in an Industrial Gas Phase Polymerisation Reactor Akbari , Vahid Hamid, Mohd. Kamaruddin Abd. TA1-2040 Engineering (General). Civil engineering (General) The objective of this paper is to develop computational fluid dynamic (CFD)- population balance model (PBM) coupled model to predict a minimum fluidisation velocity in industrial polydisperse gas phase linear low-density polyethylene (LLDPE) polymerisation reactor. The population balance model (PBM) by direct quadrature method of moment (DQMOM) implemented in CFD framework was used to predict the minimum fluidisation velocity. The simulation results were validated by the operational data in terms of bed height and pressure drop. This CFD-PBM coupled model can be extended to investigate the flow field and particle kinetic through the reactor. Taylor's University 2014 Article PeerReviewed application/pdf en http://eprints.usm.my/42733/1/JES_Vol._10_2014-Art._10-%2895-105%29.pdf Akbari , Vahid and Hamid, Mohd. Kamaruddin Abd. (2014) Prediction of Minimum Fluidisation Velocity Using a CFD-PBM Coupled Model in an Industrial Gas Phase Polymerisation Reactor. Journal of Engineering Science and Technology, 10. pp. 95-105. ISSN 1823-4690 http://web.usm.my/jes/10_2014/JES%20Vol.%2010%202014-Art.%2010-(95-105).pdf
spellingShingle TA1-2040 Engineering (General). Civil engineering (General)
Akbari , Vahid
Hamid, Mohd. Kamaruddin Abd.
Prediction of Minimum Fluidisation Velocity Using a CFD-PBM Coupled Model in an Industrial Gas Phase Polymerisation Reactor
title Prediction of Minimum Fluidisation Velocity Using a CFD-PBM Coupled Model in an Industrial Gas Phase Polymerisation Reactor
title_full Prediction of Minimum Fluidisation Velocity Using a CFD-PBM Coupled Model in an Industrial Gas Phase Polymerisation Reactor
title_fullStr Prediction of Minimum Fluidisation Velocity Using a CFD-PBM Coupled Model in an Industrial Gas Phase Polymerisation Reactor
title_full_unstemmed Prediction of Minimum Fluidisation Velocity Using a CFD-PBM Coupled Model in an Industrial Gas Phase Polymerisation Reactor
title_short Prediction of Minimum Fluidisation Velocity Using a CFD-PBM Coupled Model in an Industrial Gas Phase Polymerisation Reactor
title_sort prediction of minimum fluidisation velocity using a cfd pbm coupled model in an industrial gas phase polymerisation reactor
topic TA1-2040 Engineering (General). Civil engineering (General)
url http://eprints.usm.my/42733/1/JES_Vol._10_2014-Art._10-%2895-105%29.pdf
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