An MPEC formulation for dynamic optimization of distillation operations
- Autores
- Rajendran, Arvind; Díaz, María Soledad; Biegler, Lorenz Theodor
- Año de publicación
- 2004
- Idioma
- inglés
- Tipo de recurso
- artículo
- Estado
- versión publicada
- Descripción
- We consider the dynamic optimization of chemical processes with changes in the number of equilibrium phases. Recent work has shown that transitions in the number of phases can be modeled as a mathematical program with equilibrium constraints (MPEC). This study generalizes the MPEC to consider dynamic characteristics. In particular, we describe a simultaneous discretization and solution strategy for dynamic optimization problems with complementarity constraints. These discretized problems are then solved with IPOPT-C, a recently developed barrier method for MPEC problems. Our approach is applied to two distillation examples. In the first, we consider the optimal startup of a binary batch distillation problem. In the second, we consider the dynamic operation of a cryogenic column for the separation of natural gas liquids. Both cases demonstrate the effectiveness of the approach on large scale MPEC problems.
Fil: Rajendran, Arvind. University of Carnegie Mellon; Estados Unidos
Fil: Díaz, María Soledad. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina
Fil: Biegler, Lorenz Theodor. University of Carnegie Mellon; Estados Unidos - Materia
-
BARRIER METHODS
COMPLEMENTARITY CONDITIONS
DISTILLATION
DYNAMIC OPTIMIZATION
NONLINEAR PROGRAMMING - Nivel de accesibilidad
- acceso abierto
- Condiciones de uso
- https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
- Repositorio
- Institución
- Consejo Nacional de Investigaciones Científicas y Técnicas
- OAI Identificador
- oai:ri.conicet.gov.ar:11336/127014
Ver los metadatos del registro completo
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An MPEC formulation for dynamic optimization of distillation operationsRajendran, ArvindDíaz, María SoledadBiegler, Lorenz TheodorBARRIER METHODSCOMPLEMENTARITY CONDITIONSDISTILLATIONDYNAMIC OPTIMIZATIONNONLINEAR PROGRAMMINGhttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2We consider the dynamic optimization of chemical processes with changes in the number of equilibrium phases. Recent work has shown that transitions in the number of phases can be modeled as a mathematical program with equilibrium constraints (MPEC). This study generalizes the MPEC to consider dynamic characteristics. In particular, we describe a simultaneous discretization and solution strategy for dynamic optimization problems with complementarity constraints. These discretized problems are then solved with IPOPT-C, a recently developed barrier method for MPEC problems. Our approach is applied to two distillation examples. In the first, we consider the optimal startup of a binary batch distillation problem. In the second, we consider the dynamic operation of a cryogenic column for the separation of natural gas liquids. Both cases demonstrate the effectiveness of the approach on large scale MPEC problems.Fil: Rajendran, Arvind. University of Carnegie Mellon; Estados UnidosFil: Díaz, María Soledad. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; ArgentinaFil: Biegler, Lorenz Theodor. University of Carnegie Mellon; Estados UnidosPergamon-Elsevier Science Ltd2004-09info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/127014Rajendran, Arvind; Díaz, María Soledad; Biegler, Lorenz Theodor; An MPEC formulation for dynamic optimization of distillation operations; Pergamon-Elsevier Science Ltd; Computers and Chemical Engineering; 28; 10; 9-2004; 2037-20520098-1354CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/url/https://www.sciencedirect.com/science/article/abs/pii/S0098135404000857#!info:eu-repo/semantics/altIdentifier/doi/10.1016/j.compchemeng.2004.03.015info:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-09-03T10:09:43Zoai:ri.conicet.gov.ar:11336/127014instacron:CONICETInstitucionalhttp://ri.conicet.gov.ar/Organismo científico-tecnológicoNo correspondehttp://ri.conicet.gov.ar/oai/requestdasensio@conicet.gov.ar; lcarlino@conicet.gov.arArgentinaNo correspondeNo correspondeNo correspondeopendoar:34982025-09-03 10:09:43.526CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse |
dc.title.none.fl_str_mv |
An MPEC formulation for dynamic optimization of distillation operations |
title |
An MPEC formulation for dynamic optimization of distillation operations |
spellingShingle |
An MPEC formulation for dynamic optimization of distillation operations Rajendran, Arvind BARRIER METHODS COMPLEMENTARITY CONDITIONS DISTILLATION DYNAMIC OPTIMIZATION NONLINEAR PROGRAMMING |
title_short |
An MPEC formulation for dynamic optimization of distillation operations |
title_full |
An MPEC formulation for dynamic optimization of distillation operations |
title_fullStr |
An MPEC formulation for dynamic optimization of distillation operations |
title_full_unstemmed |
An MPEC formulation for dynamic optimization of distillation operations |
title_sort |
An MPEC formulation for dynamic optimization of distillation operations |
dc.creator.none.fl_str_mv |
Rajendran, Arvind Díaz, María Soledad Biegler, Lorenz Theodor |
author |
Rajendran, Arvind |
author_facet |
Rajendran, Arvind Díaz, María Soledad Biegler, Lorenz Theodor |
author_role |
author |
author2 |
Díaz, María Soledad Biegler, Lorenz Theodor |
author2_role |
author author |
dc.subject.none.fl_str_mv |
BARRIER METHODS COMPLEMENTARITY CONDITIONS DISTILLATION DYNAMIC OPTIMIZATION NONLINEAR PROGRAMMING |
topic |
BARRIER METHODS COMPLEMENTARITY CONDITIONS DISTILLATION DYNAMIC OPTIMIZATION NONLINEAR PROGRAMMING |
purl_subject.fl_str_mv |
https://purl.org/becyt/ford/2.4 https://purl.org/becyt/ford/2 |
dc.description.none.fl_txt_mv |
We consider the dynamic optimization of chemical processes with changes in the number of equilibrium phases. Recent work has shown that transitions in the number of phases can be modeled as a mathematical program with equilibrium constraints (MPEC). This study generalizes the MPEC to consider dynamic characteristics. In particular, we describe a simultaneous discretization and solution strategy for dynamic optimization problems with complementarity constraints. These discretized problems are then solved with IPOPT-C, a recently developed barrier method for MPEC problems. Our approach is applied to two distillation examples. In the first, we consider the optimal startup of a binary batch distillation problem. In the second, we consider the dynamic operation of a cryogenic column for the separation of natural gas liquids. Both cases demonstrate the effectiveness of the approach on large scale MPEC problems. Fil: Rajendran, Arvind. University of Carnegie Mellon; Estados Unidos Fil: Díaz, María Soledad. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina Fil: Biegler, Lorenz Theodor. University of Carnegie Mellon; Estados Unidos |
description |
We consider the dynamic optimization of chemical processes with changes in the number of equilibrium phases. Recent work has shown that transitions in the number of phases can be modeled as a mathematical program with equilibrium constraints (MPEC). This study generalizes the MPEC to consider dynamic characteristics. In particular, we describe a simultaneous discretization and solution strategy for dynamic optimization problems with complementarity constraints. These discretized problems are then solved with IPOPT-C, a recently developed barrier method for MPEC problems. Our approach is applied to two distillation examples. In the first, we consider the optimal startup of a binary batch distillation problem. In the second, we consider the dynamic operation of a cryogenic column for the separation of natural gas liquids. Both cases demonstrate the effectiveness of the approach on large scale MPEC problems. |
publishDate |
2004 |
dc.date.none.fl_str_mv |
2004-09 |
dc.type.none.fl_str_mv |
info:eu-repo/semantics/article info:eu-repo/semantics/publishedVersion http://purl.org/coar/resource_type/c_6501 info:ar-repo/semantics/articulo |
format |
article |
status_str |
publishedVersion |
dc.identifier.none.fl_str_mv |
http://hdl.handle.net/11336/127014 Rajendran, Arvind; Díaz, María Soledad; Biegler, Lorenz Theodor; An MPEC formulation for dynamic optimization of distillation operations; Pergamon-Elsevier Science Ltd; Computers and Chemical Engineering; 28; 10; 9-2004; 2037-2052 0098-1354 CONICET Digital CONICET |
url |
http://hdl.handle.net/11336/127014 |
identifier_str_mv |
Rajendran, Arvind; Díaz, María Soledad; Biegler, Lorenz Theodor; An MPEC formulation for dynamic optimization of distillation operations; Pergamon-Elsevier Science Ltd; Computers and Chemical Engineering; 28; 10; 9-2004; 2037-2052 0098-1354 CONICET Digital CONICET |
dc.language.none.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
info:eu-repo/semantics/altIdentifier/url/https://www.sciencedirect.com/science/article/abs/pii/S0098135404000857#! info:eu-repo/semantics/altIdentifier/doi/10.1016/j.compchemeng.2004.03.015 |
dc.rights.none.fl_str_mv |
info:eu-repo/semantics/openAccess https://creativecommons.org/licenses/by-nc-sa/2.5/ar/ |
eu_rights_str_mv |
openAccess |
rights_invalid_str_mv |
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/ |
dc.format.none.fl_str_mv |
application/pdf application/pdf |
dc.publisher.none.fl_str_mv |
Pergamon-Elsevier Science Ltd |
publisher.none.fl_str_mv |
Pergamon-Elsevier Science Ltd |
dc.source.none.fl_str_mv |
reponame:CONICET Digital (CONICET) instname:Consejo Nacional de Investigaciones Científicas y Técnicas |
reponame_str |
CONICET Digital (CONICET) |
collection |
CONICET Digital (CONICET) |
instname_str |
Consejo Nacional de Investigaciones Científicas y Técnicas |
repository.name.fl_str_mv |
CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicas |
repository.mail.fl_str_mv |
dasensio@conicet.gov.ar; lcarlino@conicet.gov.ar |
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1842270092605259776 |
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13.13397 |