APPLICATION OF MODEL PREDICTIVE CONTROL TO BATCH POLYMERIZATION REACTOR
The absence of a stable operational state in polymerization reactors that operates in batches is factor that determine the need of a special control system. In this study, advanced control methodology is implemented for controlling the operation of a batch polymerization reactor for polystyrene prod...
- Autores:
- Tipo de recurso:
- article
- Fecha de publicación:
- 2006
- Institución:
- Pontificia Universidad Javeriana
- Repositorio:
- Repositorio Universidad Javeriana
- Idioma:
- eng
- OAI Identifier:
- oai:repository.javeriana.edu.co:10554/31947
- Acceso en línea:
- http://revistas.javeriana.edu.co/index.php/scientarium/article/view/4946
http://hdl.handle.net/10554/31947
- Palabra clave:
- null
control; MPC; polymerization; polystyrene; modeling
null
- Rights
- openAccess
- License
- Atribución-NoComercial-SinDerivadas 4.0 Internacional
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APPLICATION OF MODEL PREDICTIVE CONTROL TO BATCH POLYMERIZATION REACTORGhasem, N. M.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, MalaysiaHussain, M. A.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, MalaysiaSata, S. A.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, Malaysianullcontrol; MPC; polymerization; polystyrene; modelingnullThe absence of a stable operational state in polymerization reactors that operates in batches is factor that determine the need of a special control system. In this study, advanced control methodology is implemented for controlling the operation of a batch polymerization reactor for polystyrene production utilizing model predictive control. By utilizing a model of the polymerization process, the necessary operational conditions were determined for producing the polymer within the desired characteristics. The main control objective is to bring the reactor temperature to its target temperature as rapidly as possible with minimal temperature overshoot. Control performance for the proposed method is encouraging. It has been observed that temperature overshoot can be minimized by the proposed method with the use of both reactor and jacket energy balance for reactor temperature control.Pontificia Universidad Javeriananull2018-02-24T16:01:01Z2020-04-15T18:08:46Z2018-02-24T16:01:01Z2020-04-15T18:08:46Z2006-01-10http://purl.org/coar/version/c_970fb48d4fbd8a85Artículo de revistahttp://purl.org/coar/resource_type/c_6501info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionPDFapplication/pdfhttp://revistas.javeriana.edu.co/index.php/scientarium/article/view/49462027-13520122-7483http://hdl.handle.net/10554/31947enghttp://revistas.javeriana.edu.co/index.php/scientarium/article/view/4946/3820Universitas Scientiarum; Vol 11, No 1 (2006); 49-58Universitas Scientiarum; Vol 11, No 1 (2006); 49-58Universitas Scientiarum; Vol 11, No 1 (2006); 49-58nullnullnullAtribución-NoComercial-SinDerivadas 4.0 Internacionalinfo:eu-repo/semantics/openAccesshttp://purl.org/coar/access_right/c_abf2reponame:Repositorio Universidad Javerianainstname:Pontificia Universidad Javerianainstacron:Pontificia Universidad Javeriana2023-03-28T21:15:16Z |
dc.title.none.fl_str_mv |
APPLICATION OF MODEL PREDICTIVE CONTROL TO BATCH POLYMERIZATION REACTOR |
title |
APPLICATION OF MODEL PREDICTIVE CONTROL TO BATCH POLYMERIZATION REACTOR |
spellingShingle |
APPLICATION OF MODEL PREDICTIVE CONTROL TO BATCH POLYMERIZATION REACTOR Ghasem, N. M.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, Malaysia null control; MPC; polymerization; polystyrene; modeling null |
title_short |
APPLICATION OF MODEL PREDICTIVE CONTROL TO BATCH POLYMERIZATION REACTOR |
title_full |
APPLICATION OF MODEL PREDICTIVE CONTROL TO BATCH POLYMERIZATION REACTOR |
title_fullStr |
APPLICATION OF MODEL PREDICTIVE CONTROL TO BATCH POLYMERIZATION REACTOR |
title_full_unstemmed |
APPLICATION OF MODEL PREDICTIVE CONTROL TO BATCH POLYMERIZATION REACTOR |
title_sort |
APPLICATION OF MODEL PREDICTIVE CONTROL TO BATCH POLYMERIZATION REACTOR |
dc.creator.none.fl_str_mv |
Ghasem, N. M.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, Malaysia Hussain, M. A.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, Malaysia Sata, S. A.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, Malaysia |
author |
Ghasem, N. M.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, Malaysia |
author_facet |
Ghasem, N. M.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, Malaysia Hussain, M. A.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, Malaysia Sata, S. A.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, Malaysia |
author_role |
author |
author2 |
Hussain, M. A.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, Malaysia Sata, S. A.; Department of Chemical Engineering, University of Malaya, Kuala Lumpur, Malaysia |
author2_role |
author author |
dc.contributor.none.fl_str_mv |
null |
dc.subject.none.fl_str_mv |
null control; MPC; polymerization; polystyrene; modeling null |
topic |
null control; MPC; polymerization; polystyrene; modeling null |
description |
The absence of a stable operational state in polymerization reactors that operates in batches is factor that determine the need of a special control system. In this study, advanced control methodology is implemented for controlling the operation of a batch polymerization reactor for polystyrene production utilizing model predictive control. By utilizing a model of the polymerization process, the necessary operational conditions were determined for producing the polymer within the desired characteristics. The main control objective is to bring the reactor temperature to its target temperature as rapidly as possible with minimal temperature overshoot. Control performance for the proposed method is encouraging. It has been observed that temperature overshoot can be minimized by the proposed method with the use of both reactor and jacket energy balance for reactor temperature control. |
publishDate |
2006 |
dc.date.none.fl_str_mv |
2006-01-10 2018-02-24T16:01:01Z 2018-02-24T16:01:01Z 2020-04-15T18:08:46Z 2020-04-15T18:08:46Z |
dc.type.none.fl_str_mv |
http://purl.org/coar/version/c_970fb48d4fbd8a85 Artículo de revista http://purl.org/coar/resource_type/c_6501 info:eu-repo/semantics/article info:eu-repo/semantics/publishedVersion |
format |
article |
status_str |
publishedVersion |
dc.identifier.none.fl_str_mv |
http://revistas.javeriana.edu.co/index.php/scientarium/article/view/4946 2027-1352 0122-7483 http://hdl.handle.net/10554/31947 |
url |
http://revistas.javeriana.edu.co/index.php/scientarium/article/view/4946 http://hdl.handle.net/10554/31947 |
identifier_str_mv |
2027-1352 0122-7483 |
dc.language.none.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
http://revistas.javeriana.edu.co/index.php/scientarium/article/view/4946/3820 Universitas Scientiarum; Vol 11, No 1 (2006); 49-58 Universitas Scientiarum; Vol 11, No 1 (2006); 49-58 Universitas Scientiarum; Vol 11, No 1 (2006); 49-58 |
dc.rights.none.fl_str_mv |
Atribución-NoComercial-SinDerivadas 4.0 Internacional info:eu-repo/semantics/openAccess http://purl.org/coar/access_right/c_abf2 |
rights_invalid_str_mv |
Atribución-NoComercial-SinDerivadas 4.0 Internacional http://purl.org/coar/access_right/c_abf2 |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
PDF application/pdf |
dc.coverage.none.fl_str_mv |
null null null |
dc.publisher.none.fl_str_mv |
Pontificia Universidad Javeriana |
publisher.none.fl_str_mv |
Pontificia Universidad Javeriana |
dc.source.none.fl_str_mv |
reponame:Repositorio Universidad Javeriana instname:Pontificia Universidad Javeriana instacron:Pontificia Universidad Javeriana |
instname_str |
Pontificia Universidad Javeriana |
instacron_str |
Pontificia Universidad Javeriana |
institution |
Pontificia Universidad Javeriana |
reponame_str |
Repositorio Universidad Javeriana |
collection |
Repositorio Universidad Javeriana |
_version_ |
1803712809919315968 |