Dynamic model for polyethylene production in a multizone circulating reactor

The multizone circulating reactor (MZCR) technology is a newly announced reactor design for solid-catalyzed gas-phase polymerization. The process is characterized by two hydrodynamically distinct but interconnecting polymerization zones, thus forming a continuous loop of polymer flow between the sai...

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Main Authors: Ghasem, N.M., Ang, W.L., Hussain, Mohd Azlan
Format: Article
Published: Chemical Product and Process Modeling 2008
Subjects:
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author Ghasem, N.M.
Ang, W.L.
Hussain, Mohd Azlan
author_facet Ghasem, N.M.
Ang, W.L.
Hussain, Mohd Azlan
author_sort Ghasem, N.M.
collection UM
description The multizone circulating reactor (MZCR) technology is a newly announced reactor design for solid-catalyzed gas-phase polymerization. The process is characterized by two hydrodynamically distinct but interconnecting polymerization zones, thus forming a continuous loop of polymer flow between the said zones. In the present study, a dynamic model for the MZCR reactor is developed to illustrate the basic dynamic behavior of the new reactor design; the model is used to study the copolymerization of ethylene with butene. Several parameter sensitivity analyses are performed to show the computer-simulated time responses for reactor temperature, number-average molecular weight, weight-average molecular weight, catalyst feed rate and the monomer concentration along the reactor length.
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spelling um.eprints-70432021-02-10T03:47:03Z http://eprints.um.edu.my/7043/ Dynamic model for polyethylene production in a multizone circulating reactor Ghasem, N.M. Ang, W.L. Hussain, Mohd Azlan TA Engineering (General). Civil engineering (General) TP Chemical technology The multizone circulating reactor (MZCR) technology is a newly announced reactor design for solid-catalyzed gas-phase polymerization. The process is characterized by two hydrodynamically distinct but interconnecting polymerization zones, thus forming a continuous loop of polymer flow between the said zones. In the present study, a dynamic model for the MZCR reactor is developed to illustrate the basic dynamic behavior of the new reactor design; the model is used to study the copolymerization of ethylene with butene. Several parameter sensitivity analyses are performed to show the computer-simulated time responses for reactor temperature, number-average molecular weight, weight-average molecular weight, catalyst feed rate and the monomer concentration along the reactor length. Chemical Product and Process Modeling 2008 Article PeerReviewed Ghasem, N.M. and Ang, W.L. and Hussain, Mohd Azlan (2008) Dynamic model for polyethylene production in a multizone circulating reactor. Chemical Product and Process Modeling, 3 (1). ISSN 19342659, http://www.scopus.com/inward/record.url?eid=2-s2.0-43449135603&partnerID=40&md5=db701b5d9a13a91a17a460afda90b71f
spellingShingle TA Engineering (General). Civil engineering (General)
TP Chemical technology
Ghasem, N.M.
Ang, W.L.
Hussain, Mohd Azlan
Dynamic model for polyethylene production in a multizone circulating reactor
title Dynamic model for polyethylene production in a multizone circulating reactor
title_full Dynamic model for polyethylene production in a multizone circulating reactor
title_fullStr Dynamic model for polyethylene production in a multizone circulating reactor
title_full_unstemmed Dynamic model for polyethylene production in a multizone circulating reactor
title_short Dynamic model for polyethylene production in a multizone circulating reactor
title_sort dynamic model for polyethylene production in a multizone circulating reactor
topic TA Engineering (General). Civil engineering (General)
TP Chemical technology
work_keys_str_mv AT ghasemnm dynamicmodelforpolyethyleneproductioninamultizonecirculatingreactor
AT angwl dynamicmodelforpolyethyleneproductioninamultizonecirculatingreactor
AT hussainmohdazlan dynamicmodelforpolyethyleneproductioninamultizonecirculatingreactor