Fractional control of an industrial furnace - doi: 10.4025/actascitechnol.v32i3.6552
Autor(a) principal: | |
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Data de Publicação: | 2010 |
Outros Autores: | , , |
Tipo de documento: | Artigo |
Idioma: | por eng |
Título da fonte: | Acta scientiarum. Technology (Online) |
Texto Completo: | http://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/article/view/6552 |
Resumo: | The requirements of high production allied with product quality, process safety and environmental regulation, lead control systems to play a key role in the operation of chemical and biochemical plants. In petrochemical plants, furnaces are essential equipments for process operation and due to energy costs, adequate operation and control are of extreme importance for process economics. The search for new and more efficient control laws led to the development of fractional PID control algorithm, which is based on the use of fractional differential equations. In this work, a previously identified mathematical model of an actual industrial furnace is used for fractional PID control studies. Feedback loop in servo control was analyzed, focusing on the study of the influence of the controller parameters over control loop performance. Particularly, P, fractional PI and fractional PD controller were considered in this study. Simulations were carried out showing that the fractional controllers were able to perform set-point transitions. The control loop performance was evaluated by ITAE and ISE criteria, showing that, in this study, fractional PI is the best algorithm. |
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Fractional control of an industrial furnace - doi: 10.4025/actascitechnol.v32i3.6552Fractional control of an industrial furnace - doi: 10.4025/actascitechnol.v32i3.6552process controlfractional differential equationfractional controlfurnaceprocess controlfractional differential equationfractional controlfurnace3.06.02.00-9The requirements of high production allied with product quality, process safety and environmental regulation, lead control systems to play a key role in the operation of chemical and biochemical plants. In petrochemical plants, furnaces are essential equipments for process operation and due to energy costs, adequate operation and control are of extreme importance for process economics. The search for new and more efficient control laws led to the development of fractional PID control algorithm, which is based on the use of fractional differential equations. In this work, a previously identified mathematical model of an actual industrial furnace is used for fractional PID control studies. Feedback loop in servo control was analyzed, focusing on the study of the influence of the controller parameters over control loop performance. Particularly, P, fractional PI and fractional PD controller were considered in this study. Simulations were carried out showing that the fractional controllers were able to perform set-point transitions. The control loop performance was evaluated by ITAE and ISE criteria, showing that, in this study, fractional PI is the best algorithm.The requirements of high production allied with product quality, process safety and environmental regulation, lead control systems to play a key role in the operation of chemical and biochemical plants. In petrochemical plants, furnaces are essential equipments for process operation and due to energy costs, adequate operation and control are of extreme importance for process economics. The search for new and more efficient control laws led to the development of fractional PID control algorithm, which is based on the use of fractional differential equations. In this work, a previously identified mathematical model of an actual industrial furnace is used for fractional PID control studies. Feedback loop in servo control was analyzed, focusing on the study of the influence of the controller parameters over control loop performance. Particularly, P, fractional PI and fractional PD controller were considered in this study. Simulations were carried out showing that the fractional controllers were able to perform set-point transitions. The control loop performance was evaluated by ITAE and ISE criteria, showing that, in this study, fractional PI is the best algorithm.Universidade Estadual De Maringá2010-11-09info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionSimulationapplication/pdfapplication/pdfhttp://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/article/view/655210.4025/actascitechnol.v32i3.6552Acta Scientiarum. Technology; Vol 32 No 3 (2010); 279-285Acta Scientiarum. Technology; v. 32 n. 3 (2010); 279-2851806-25631807-8664reponame:Acta scientiarum. Technology (Online)instname:Universidade Estadual de Maringá (UEM)instacron:UEMporenghttp://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/article/view/6552/6552http://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/article/view/6552/6552AIsfer, Luis Antonio DuarteLenzi, Ervin KaminskiTeixeira, Giovani MarceloLenzi, Marcelo Kaminskiinfo:eu-repo/semantics/openAccess2024-05-17T13:03:06Zoai:periodicos.uem.br/ojs:article/6552Revistahttps://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/indexPUBhttps://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/oai||actatech@uem.br1807-86641806-2563opendoar:2024-05-17T13:03:06Acta scientiarum. Technology (Online) - Universidade Estadual de Maringá (UEM)false |
dc.title.none.fl_str_mv |
Fractional control of an industrial furnace - doi: 10.4025/actascitechnol.v32i3.6552 Fractional control of an industrial furnace - doi: 10.4025/actascitechnol.v32i3.6552 |
title |
Fractional control of an industrial furnace - doi: 10.4025/actascitechnol.v32i3.6552 |
spellingShingle |
Fractional control of an industrial furnace - doi: 10.4025/actascitechnol.v32i3.6552 Isfer, Luis Antonio Duarte process control fractional differential equation fractional control furnace process control fractional differential equation fractional control furnace 3.06.02.00-9 |
title_short |
Fractional control of an industrial furnace - doi: 10.4025/actascitechnol.v32i3.6552 |
title_full |
Fractional control of an industrial furnace - doi: 10.4025/actascitechnol.v32i3.6552 |
title_fullStr |
Fractional control of an industrial furnace - doi: 10.4025/actascitechnol.v32i3.6552 |
title_full_unstemmed |
Fractional control of an industrial furnace - doi: 10.4025/actascitechnol.v32i3.6552 |
title_sort |
Fractional control of an industrial furnace - doi: 10.4025/actascitechnol.v32i3.6552 |
author |
Isfer, Luis Antonio Duarte |
author_facet |
Isfer, Luis Antonio Duarte Lenzi, Ervin Kaminski Teixeira, Giovani Marcelo Lenzi, Marcelo Kaminski |
author_role |
author |
author2 |
Lenzi, Ervin Kaminski Teixeira, Giovani Marcelo Lenzi, Marcelo Kaminski |
author2_role |
author author author |
dc.contributor.author.fl_str_mv |
Isfer, Luis Antonio Duarte Lenzi, Ervin Kaminski Teixeira, Giovani Marcelo Lenzi, Marcelo Kaminski |
dc.subject.por.fl_str_mv |
process control fractional differential equation fractional control furnace process control fractional differential equation fractional control furnace 3.06.02.00-9 |
topic |
process control fractional differential equation fractional control furnace process control fractional differential equation fractional control furnace 3.06.02.00-9 |
description |
The requirements of high production allied with product quality, process safety and environmental regulation, lead control systems to play a key role in the operation of chemical and biochemical plants. In petrochemical plants, furnaces are essential equipments for process operation and due to energy costs, adequate operation and control are of extreme importance for process economics. The search for new and more efficient control laws led to the development of fractional PID control algorithm, which is based on the use of fractional differential equations. In this work, a previously identified mathematical model of an actual industrial furnace is used for fractional PID control studies. Feedback loop in servo control was analyzed, focusing on the study of the influence of the controller parameters over control loop performance. Particularly, P, fractional PI and fractional PD controller were considered in this study. Simulations were carried out showing that the fractional controllers were able to perform set-point transitions. The control loop performance was evaluated by ITAE and ISE criteria, showing that, in this study, fractional PI is the best algorithm. |
publishDate |
2010 |
dc.date.none.fl_str_mv |
2010-11-09 |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article info:eu-repo/semantics/publishedVersion Simulation |
format |
article |
status_str |
publishedVersion |
dc.identifier.uri.fl_str_mv |
http://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/article/view/6552 10.4025/actascitechnol.v32i3.6552 |
url |
http://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/article/view/6552 |
identifier_str_mv |
10.4025/actascitechnol.v32i3.6552 |
dc.language.iso.fl_str_mv |
por eng |
language |
por eng |
dc.relation.none.fl_str_mv |
http://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/article/view/6552/6552 http://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/article/view/6552/6552A |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
application/pdf application/pdf |
dc.publisher.none.fl_str_mv |
Universidade Estadual De Maringá |
publisher.none.fl_str_mv |
Universidade Estadual De Maringá |
dc.source.none.fl_str_mv |
Acta Scientiarum. Technology; Vol 32 No 3 (2010); 279-285 Acta Scientiarum. Technology; v. 32 n. 3 (2010); 279-285 1806-2563 1807-8664 reponame:Acta scientiarum. Technology (Online) instname:Universidade Estadual de Maringá (UEM) instacron:UEM |
instname_str |
Universidade Estadual de Maringá (UEM) |
instacron_str |
UEM |
institution |
UEM |
reponame_str |
Acta scientiarum. Technology (Online) |
collection |
Acta scientiarum. Technology (Online) |
repository.name.fl_str_mv |
Acta scientiarum. Technology (Online) - Universidade Estadual de Maringá (UEM) |
repository.mail.fl_str_mv |
||actatech@uem.br |
_version_ |
1799315333285150720 |