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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Chemical Product and Process Modeling
2008
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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. |
first_indexed | 2024-03-06T05:17:48Z |
format | Article |
id | um.eprints-7043 |
institution | Universiti Malaya |
last_indexed | 2024-03-06T05:17:48Z |
publishDate | 2008 |
publisher | Chemical Product and Process Modeling |
record_format | dspace |
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 |