Low-density polyethylene simulated production in high pressure tubular reactor

Low-density polyethylene simulated production in high pressure tubular reactor

The importance of the LDPE polymerization process has spawned a slew of LDPE tubular reactor modelling and simulation projects. Through adjusting input parameters, the sensitivity study of input parameters in an industrial low density polyethylene tube reactor was addressed in this paper. This work&...

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Published in:Materials Today: Proceedings
Main Author: Mohd Supion N.; Idris I.; Md Som A.; Sholahudin Rahman F.; Ahmad Ilyas R.; Azmi A.
Format: Article
Language:English
Published: Elsevier Ltd 2023
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-85146123503&doi=10.1016%2fj.matpr.2022.12.155&partnerID=40&md5=7c782825d696b41a9028a4e8a28fb8c6
id 2-s2.0-85146123503
spelling 2-s2.0-85146123503
Mohd Supion N.; Idris I.; Md Som A.; Sholahudin Rahman F.; Ahmad Ilyas R.; Azmi A.
Low-density polyethylene simulated production in high pressure tubular reactor
2023
Materials Today: Proceedings


10.1016/j.matpr.2022.12.155
https://www.scopus.com/inward/record.uri?eid=2-s2.0-85146123503&doi=10.1016%2fj.matpr.2022.12.155&partnerID=40&md5=7c782825d696b41a9028a4e8a28fb8c6
The importance of the LDPE polymerization process has spawned a slew of LDPE tubular reactor modelling and simulation projects. Through adjusting input parameters, the sensitivity study of input parameters in an industrial low density polyethylene tube reactor was addressed in this paper. This work's innovation was highlighted with the incorporation of the LDPE melt flow index in the reactor output. The highest temperature peak and monomer conversion were obtained when initiator concentration were increased by 1.06 factor, whereas the highest melt flow index was obtained when the inlet temperature was increased by 1.07 factor. The monomer flow rate, initiator flow rate, and solvent flow rate all had a substantial impact on the LDPE process performance in a tubular reactor. © 2023
Elsevier Ltd
22147853
English
Article
author Mohd Supion N.; Idris I.; Md Som A.; Sholahudin Rahman F.; Ahmad Ilyas R.; Azmi A.
spellingShingle Mohd Supion N.; Idris I.; Md Som A.; Sholahudin Rahman F.; Ahmad Ilyas R.; Azmi A.
Low-density polyethylene simulated production in high pressure tubular reactor
author_facet Mohd Supion N.; Idris I.; Md Som A.; Sholahudin Rahman F.; Ahmad Ilyas R.; Azmi A.
author_sort Mohd Supion N.; Idris I.; Md Som A.; Sholahudin Rahman F.; Ahmad Ilyas R.; Azmi A.
title Low-density polyethylene simulated production in high pressure tubular reactor
title_short Low-density polyethylene simulated production in high pressure tubular reactor
title_full Low-density polyethylene simulated production in high pressure tubular reactor
title_fullStr Low-density polyethylene simulated production in high pressure tubular reactor
title_full_unstemmed Low-density polyethylene simulated production in high pressure tubular reactor
title_sort Low-density polyethylene simulated production in high pressure tubular reactor
publishDate 2023
container_title Materials Today: Proceedings
container_volume
container_issue
doi_str_mv 10.1016/j.matpr.2022.12.155
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-85146123503&doi=10.1016%2fj.matpr.2022.12.155&partnerID=40&md5=7c782825d696b41a9028a4e8a28fb8c6
description The importance of the LDPE polymerization process has spawned a slew of LDPE tubular reactor modelling and simulation projects. Through adjusting input parameters, the sensitivity study of input parameters in an industrial low density polyethylene tube reactor was addressed in this paper. This work's innovation was highlighted with the incorporation of the LDPE melt flow index in the reactor output. The highest temperature peak and monomer conversion were obtained when initiator concentration were increased by 1.06 factor, whereas the highest melt flow index was obtained when the inlet temperature was increased by 1.07 factor. The monomer flow rate, initiator flow rate, and solvent flow rate all had a substantial impact on the LDPE process performance in a tubular reactor. © 2023
publisher Elsevier Ltd
issn 22147853
language English
format Article
accesstype
record_format scopus
collection Scopus
_version_ 1823296159918063616

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