Optimal process operation for the production of linear polyethylene resins with tailored molecular weight distribution

An optimization model is presented to determine optimal operating policies for tailoring high density polyethylene in a continuous polymerization process. Shaping the whole molecular weight distribution (MWD) by adopting an appropriate choice of operating conditions is of great interest when designi...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Veröffentlicht in:AIChE journal 2011-08, Vol.57 (8), p.2149-2163
Hauptverfasser: Pontes, K. V., Embiruçu, M., Maciel, R., Hartwich, A., Marquardt, W.
Format: Artikel
Sprache:eng
Schlagworte:
Online-Zugang:Volltext
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
container_end_page 2163
container_issue 8
container_start_page 2149
container_title AIChE journal
container_volume 57
creator Pontes, K. V.
Embiruçu, M.
Maciel, R.
Hartwich, A.
Marquardt, W.
description An optimization model is presented to determine optimal operating policies for tailoring high density polyethylene in a continuous polymerization process. Shaping the whole molecular weight distribution (MWD) by adopting an appropriate choice of operating conditions is of great interest when designing new polymers or when improving quality. The continuous tubular and stirred tank reactors are modeled in steady state by a set of differential‐algebraic equations with the spatial coordinate as independent variable. A novel formulation of the optimization problem is introduced. It comprises a multi‐stage optimization model with differential‐algebraic equality constraints along the process path and inequality end‐point constraints on product quality. The resulting optimal control problem is solved at high computational efficiency by means of a shooting method. The results show the efficiency of the proposed approach and the benefit of predicting and controlling the complete MWD as well as the interplay between operating conditions and polymer properties. © 2010 American Institute of Chemical Engineers AIChE J, 2011
doi_str_mv 10.1002/aic.12438
format Article
fullrecord <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_907957084</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>907957084</sourcerecordid><originalsourceid>FETCH-LOGICAL-c4688-34f6520e57b3b633c4d2a8c61505ccac48efe6a970729b2a5afd821dc81f24fd3</originalsourceid><addsrcrecordid>eNp1kF1rFDEUhoMouFYv_AdBEPFi2nxOMpdltbVQrIhS8CZkMyduanYyTWbc7r832629ELwKOXneh5MXodeUHFNC2IkN7pgywfUTtKBSqEZ2RD5FC0IIbeqAPkcvSrmpN6Y0W6DfV-MUNjbiMScHpeA0QrZTSAP2KeNpDfuXfnb3o-RxDAPYjMcUdzCtdxEGwBlKGArehmmNJxtiytDjTYrg5ljZLYSf6wn3oUw5rOa96SV65m0s8OrhPELfzz5-W35qLq_OL5anl40TrdYNF76VjIBUK75qOXeiZ1a7lkoinbNOaPDQ2k4RxboVs9L6XjPaO009E77nR-jdwVs_cTtDmcwmFAcx2gHSXExHVCcV0aKSb_4hb9Kch7qc0UqTlkkhK_T-ALmcSsngzZhre3lnKDH7_k3t39z3X9m3D0JbnI0-28GF8hjYM4LxrnInB24bIuz-LzSnF8u_5uaQqIXC3WPC5l-mVVxJc_353Hz58PV6yYUyP_gfMl-lbg</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>878062545</pqid></control><display><type>article</type><title>Optimal process operation for the production of linear polyethylene resins with tailored molecular weight distribution</title><source>Wiley Online Library All Journals</source><creator>Pontes, K. V. ; Embiruçu, M. ; Maciel, R. ; Hartwich, A. ; Marquardt, W.</creator><creatorcontrib>Pontes, K. V. ; Embiruçu, M. ; Maciel, R. ; Hartwich, A. ; Marquardt, W.</creatorcontrib><description>An optimization model is presented to determine optimal operating policies for tailoring high density polyethylene in a continuous polymerization process. Shaping the whole molecular weight distribution (MWD) by adopting an appropriate choice of operating conditions is of great interest when designing new polymers or when improving quality. The continuous tubular and stirred tank reactors are modeled in steady state by a set of differential‐algebraic equations with the spatial coordinate as independent variable. A novel formulation of the optimization problem is introduced. It comprises a multi‐stage optimization model with differential‐algebraic equality constraints along the process path and inequality end‐point constraints on product quality. The resulting optimal control problem is solved at high computational efficiency by means of a shooting method. The results show the efficiency of the proposed approach and the benefit of predicting and controlling the complete MWD as well as the interplay between operating conditions and polymer properties. © 2010 American Institute of Chemical Engineers AIChE J, 2011</description><identifier>ISSN: 0001-1541</identifier><identifier>EISSN: 1547-5905</identifier><identifier>DOI: 10.1002/aic.12438</identifier><identifier>CODEN: AICEAC</identifier><language>eng</language><publisher>Hoboken: Wiley Subscription Services, Inc., A Wiley Company</publisher><subject>Algebra ; Applied sciences ; Chemical engineering ; Computational efficiency ; Exact sciences and technology ; mathematical modeling ; Mathematical models ; Molecular weight ; Molecular weight distribution ; multi-stage optimization ; Optimization ; Policies ; Polyethylene ; Polyethylenes ; Polymerization ; reaction engineering ; Reactors ; Tanks</subject><ispartof>AIChE journal, 2011-08, Vol.57 (8), p.2149-2163</ispartof><rights>Copyright © 2010 American Institute of Chemical Engineers (AIChE)</rights><rights>2015 INIST-CNRS</rights><rights>Copyright American Institute of Chemical Engineers Aug 2011</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c4688-34f6520e57b3b633c4d2a8c61505ccac48efe6a970729b2a5afd821dc81f24fd3</citedby><cites>FETCH-LOGICAL-c4688-34f6520e57b3b633c4d2a8c61505ccac48efe6a970729b2a5afd821dc81f24fd3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1002%2Faic.12438$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Faic.12438$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,780,784,1417,27924,27925,45574,45575</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&amp;idt=24384239$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Pontes, K. V.</creatorcontrib><creatorcontrib>Embiruçu, M.</creatorcontrib><creatorcontrib>Maciel, R.</creatorcontrib><creatorcontrib>Hartwich, A.</creatorcontrib><creatorcontrib>Marquardt, W.</creatorcontrib><title>Optimal process operation for the production of linear polyethylene resins with tailored molecular weight distribution</title><title>AIChE journal</title><addtitle>AIChE J</addtitle><description>An optimization model is presented to determine optimal operating policies for tailoring high density polyethylene in a continuous polymerization process. Shaping the whole molecular weight distribution (MWD) by adopting an appropriate choice of operating conditions is of great interest when designing new polymers or when improving quality. The continuous tubular and stirred tank reactors are modeled in steady state by a set of differential‐algebraic equations with the spatial coordinate as independent variable. A novel formulation of the optimization problem is introduced. It comprises a multi‐stage optimization model with differential‐algebraic equality constraints along the process path and inequality end‐point constraints on product quality. The resulting optimal control problem is solved at high computational efficiency by means of a shooting method. The results show the efficiency of the proposed approach and the benefit of predicting and controlling the complete MWD as well as the interplay between operating conditions and polymer properties. © 2010 American Institute of Chemical Engineers AIChE J, 2011</description><subject>Algebra</subject><subject>Applied sciences</subject><subject>Chemical engineering</subject><subject>Computational efficiency</subject><subject>Exact sciences and technology</subject><subject>mathematical modeling</subject><subject>Mathematical models</subject><subject>Molecular weight</subject><subject>Molecular weight distribution</subject><subject>multi-stage optimization</subject><subject>Optimization</subject><subject>Policies</subject><subject>Polyethylene</subject><subject>Polyethylenes</subject><subject>Polymerization</subject><subject>reaction engineering</subject><subject>Reactors</subject><subject>Tanks</subject><issn>0001-1541</issn><issn>1547-5905</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2011</creationdate><recordtype>article</recordtype><recordid>eNp1kF1rFDEUhoMouFYv_AdBEPFi2nxOMpdltbVQrIhS8CZkMyduanYyTWbc7r832629ELwKOXneh5MXodeUHFNC2IkN7pgywfUTtKBSqEZ2RD5FC0IIbeqAPkcvSrmpN6Y0W6DfV-MUNjbiMScHpeA0QrZTSAP2KeNpDfuXfnb3o-RxDAPYjMcUdzCtdxEGwBlKGArehmmNJxtiytDjTYrg5ljZLYSf6wn3oUw5rOa96SV65m0s8OrhPELfzz5-W35qLq_OL5anl40TrdYNF76VjIBUK75qOXeiZ1a7lkoinbNOaPDQ2k4RxboVs9L6XjPaO009E77nR-jdwVs_cTtDmcwmFAcx2gHSXExHVCcV0aKSb_4hb9Kch7qc0UqTlkkhK_T-ALmcSsngzZhre3lnKDH7_k3t39z3X9m3D0JbnI0-28GF8hjYM4LxrnInB24bIuz-LzSnF8u_5uaQqIXC3WPC5l-mVVxJc_353Hz58PV6yYUyP_gfMl-lbg</recordid><startdate>201108</startdate><enddate>201108</enddate><creator>Pontes, K. V.</creator><creator>Embiruçu, M.</creator><creator>Maciel, R.</creator><creator>Hartwich, A.</creator><creator>Marquardt, W.</creator><general>Wiley Subscription Services, Inc., A Wiley Company</general><general>Wiley</general><general>American Institute of Chemical Engineers</general><scope>BSCLL</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>7U5</scope><scope>8FD</scope><scope>C1K</scope><scope>L7M</scope><scope>SOI</scope></search><sort><creationdate>201108</creationdate><title>Optimal process operation for the production of linear polyethylene resins with tailored molecular weight distribution</title><author>Pontes, K. V. ; Embiruçu, M. ; Maciel, R. ; Hartwich, A. ; Marquardt, W.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c4688-34f6520e57b3b633c4d2a8c61505ccac48efe6a970729b2a5afd821dc81f24fd3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2011</creationdate><topic>Algebra</topic><topic>Applied sciences</topic><topic>Chemical engineering</topic><topic>Computational efficiency</topic><topic>Exact sciences and technology</topic><topic>mathematical modeling</topic><topic>Mathematical models</topic><topic>Molecular weight</topic><topic>Molecular weight distribution</topic><topic>multi-stage optimization</topic><topic>Optimization</topic><topic>Policies</topic><topic>Polyethylene</topic><topic>Polyethylenes</topic><topic>Polymerization</topic><topic>reaction engineering</topic><topic>Reactors</topic><topic>Tanks</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Pontes, K. V.</creatorcontrib><creatorcontrib>Embiruçu, M.</creatorcontrib><creatorcontrib>Maciel, R.</creatorcontrib><creatorcontrib>Hartwich, A.</creatorcontrib><creatorcontrib>Marquardt, W.</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Environment Abstracts</collection><jtitle>AIChE journal</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Pontes, K. V.</au><au>Embiruçu, M.</au><au>Maciel, R.</au><au>Hartwich, A.</au><au>Marquardt, W.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Optimal process operation for the production of linear polyethylene resins with tailored molecular weight distribution</atitle><jtitle>AIChE journal</jtitle><addtitle>AIChE J</addtitle><date>2011-08</date><risdate>2011</risdate><volume>57</volume><issue>8</issue><spage>2149</spage><epage>2163</epage><pages>2149-2163</pages><issn>0001-1541</issn><eissn>1547-5905</eissn><coden>AICEAC</coden><abstract>An optimization model is presented to determine optimal operating policies for tailoring high density polyethylene in a continuous polymerization process. Shaping the whole molecular weight distribution (MWD) by adopting an appropriate choice of operating conditions is of great interest when designing new polymers or when improving quality. The continuous tubular and stirred tank reactors are modeled in steady state by a set of differential‐algebraic equations with the spatial coordinate as independent variable. A novel formulation of the optimization problem is introduced. It comprises a multi‐stage optimization model with differential‐algebraic equality constraints along the process path and inequality end‐point constraints on product quality. The resulting optimal control problem is solved at high computational efficiency by means of a shooting method. The results show the efficiency of the proposed approach and the benefit of predicting and controlling the complete MWD as well as the interplay between operating conditions and polymer properties. © 2010 American Institute of Chemical Engineers AIChE J, 2011</abstract><cop>Hoboken</cop><pub>Wiley Subscription Services, Inc., A Wiley Company</pub><doi>10.1002/aic.12438</doi><tpages>15</tpages><oa>free_for_read</oa></addata></record>
fulltext fulltext
identifier ISSN: 0001-1541
ispartof AIChE journal, 2011-08, Vol.57 (8), p.2149-2163
issn 0001-1541
1547-5905
language eng
recordid cdi_proquest_miscellaneous_907957084
source Wiley Online Library All Journals
subjects Algebra
Applied sciences
Chemical engineering
Computational efficiency
Exact sciences and technology
mathematical modeling
Mathematical models
Molecular weight
Molecular weight distribution
multi-stage optimization
Optimization
Policies
Polyethylene
Polyethylenes
Polymerization
reaction engineering
Reactors
Tanks
title Optimal process operation for the production of linear polyethylene resins with tailored molecular weight distribution
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-28T10%3A19%3A59IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Optimal%20process%20operation%20for%20the%20production%20of%20linear%20polyethylene%20resins%20with%20tailored%20molecular%20weight%20distribution&rft.jtitle=AIChE%20journal&rft.au=Pontes,%20K.%20V.&rft.date=2011-08&rft.volume=57&rft.issue=8&rft.spage=2149&rft.epage=2163&rft.pages=2149-2163&rft.issn=0001-1541&rft.eissn=1547-5905&rft.coden=AICEAC&rft_id=info:doi/10.1002/aic.12438&rft_dat=%3Cproquest_cross%3E907957084%3C/proquest_cross%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=878062545&rft_id=info:pmid/&rfr_iscdi=true