Optimizing modeling the multilayer coextrusion flow of non-newtonian fluids through rectangular ducts: appropriate shear rate definition for a local power law formulation
The accuracy of viscosity predictions is a crucial aspect of polymer melt flow modeling and essential for the design of coextrusion die systems. In the field of non-Newtonian fluid modeling for coextrusion flows through rectangular ducts, significant progress has been made in understanding multilaye...
- Autores:
-
Naderer, Thomas
Hammer, Alexander
Roland, Wolfgang
Zacher, Maximilian
Berger-Weber, Gerald
- Tipo de recurso:
- Conferencia (Ponencia)
- Fecha de publicación:
- 2024
- Institución:
- Universidad de los Andes
- Repositorio:
- Séneca: repositorio Uniandes
- Idioma:
- eng
- OAI Identifier:
- oai:repositorio.uniandes.edu.co:1992/76061
- Acceso en línea:
- https://hdl.handle.net/1992/76061
https://doi.org/10.51573/Andes.PPS39.GS.MS.4
https://repositorio.uniandes.edu.co/
- Palabra clave:
- Coextrusion
Polymeric multilayer structures
CFD
Ingeniería
- Rights
- openAccess
- License
- https://repositorio.uniandes.edu.co/static/pdf/aceptacion_uso_es.pdf
id |
UNIANDES2_b7a4d94af0d212e15c5baf9290eaf256 |
---|---|
oai_identifier_str |
oai:repositorio.uniandes.edu.co:1992/76061 |
network_acronym_str |
UNIANDES2 |
network_name_str |
Séneca: repositorio Uniandes |
repository_id_str |
|
dc.title.eng.fl_str_mv |
Optimizing modeling the multilayer coextrusion flow of non-newtonian fluids through rectangular ducts: appropriate shear rate definition for a local power law formulation |
title |
Optimizing modeling the multilayer coextrusion flow of non-newtonian fluids through rectangular ducts: appropriate shear rate definition for a local power law formulation |
spellingShingle |
Optimizing modeling the multilayer coextrusion flow of non-newtonian fluids through rectangular ducts: appropriate shear rate definition for a local power law formulation Coextrusion Polymeric multilayer structures CFD Ingeniería |
title_short |
Optimizing modeling the multilayer coextrusion flow of non-newtonian fluids through rectangular ducts: appropriate shear rate definition for a local power law formulation |
title_full |
Optimizing modeling the multilayer coextrusion flow of non-newtonian fluids through rectangular ducts: appropriate shear rate definition for a local power law formulation |
title_fullStr |
Optimizing modeling the multilayer coextrusion flow of non-newtonian fluids through rectangular ducts: appropriate shear rate definition for a local power law formulation |
title_full_unstemmed |
Optimizing modeling the multilayer coextrusion flow of non-newtonian fluids through rectangular ducts: appropriate shear rate definition for a local power law formulation |
title_sort |
Optimizing modeling the multilayer coextrusion flow of non-newtonian fluids through rectangular ducts: appropriate shear rate definition for a local power law formulation |
dc.creator.fl_str_mv |
Naderer, Thomas Hammer, Alexander Roland, Wolfgang Zacher, Maximilian Berger-Weber, Gerald |
dc.contributor.author.none.fl_str_mv |
Naderer, Thomas Hammer, Alexander Roland, Wolfgang Zacher, Maximilian Berger-Weber, Gerald |
dc.contributor.editor.none.fl_str_mv |
Salcedo, Felipe Perilla, Jairo Ernesto Sierra, Cesar Medina, Jorge Alberto |
dc.subject.keyword.none.fl_str_mv |
Coextrusion Polymeric multilayer structures CFD |
topic |
Coextrusion Polymeric multilayer structures CFD Ingeniería |
dc.subject.themes.none.fl_str_mv |
Ingeniería |
description |
The accuracy of viscosity predictions is a crucial aspect of polymer melt flow modeling and essential for the design of coextrusion die systems. In the field of non-Newtonian fluid modeling for coextrusion flows through rectangular ducts, significant progress has been made in understanding multilayer flow dynamics. Our fundamental research, employing numerical techniques such as the shooting method, finite element method, and finite difference method for flow evaluation, has established a critical base for the field. Our current research advances fluid dynamics by refining our existing numerical solver, specifically developed for multilayer coextrusion flows. We aim to enhance the solver’s performance by implementing more sophisticated calculations of shear rates that go beyond the traditional approach. The traditional approach often relies on average flow velocities and channel heights, which can underrepresent the complexity of experimentally studied polymer multilayer flows. Our study systematically compares various definitions for characteristic shear rates to describe the local shear rate dependent viscosity behavior using, for instance, a local power law model. A thorough error analysis quantifies the accuracy of each model and its predictive limitations for industrially relevant material combinations and operating conditions. This includes CFD simulations and experimental data comparisons, employing methods aligned with our fundamental research in this area. Furthermore, our work paves the way for integrating these advanced fluid dynamics models into the evolving field of process digitalization, thereby contributing to the development of more efficient, digitally integrated manufacturing processes. |
publishDate |
2024 |
dc.date.issued.none.fl_str_mv |
2024-12 |
dc.date.accessioned.none.fl_str_mv |
2025-02-07T20:24:29Z |
dc.date.available.none.fl_str_mv |
2025-02-07T20:24:29Z |
dc.type.none.fl_str_mv |
Documento de Conferencia |
dc.type.coar.fl_str_mv |
http://purl.org/coar/resource_type/c_c94f |
dc.type.driver.none.fl_str_mv |
info:eu-repo/semantics/conferenceObject |
dc.type.version.none.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
dc.type.coar.none.fl_str_mv |
http://purl.org/coar/resource_type/c_8544 |
dc.type.coarversion.none.fl_str_mv |
http://purl.org/coar/version/c_970fb48d4fbd8a85 |
dc.type.content.none.fl_str_mv |
Text |
format |
http://purl.org/coar/resource_type/c_8544 |
status_str |
publishedVersion |
dc.identifier.isbn.none.fl_str_mv |
978-958-798-779-9 |
dc.identifier.uri.none.fl_str_mv |
https://hdl.handle.net/1992/76061 |
dc.identifier.doi.none.fl_str_mv |
https://doi.org/10.51573/Andes.PPS39.GS.MS.4 |
dc.identifier.instname.none.fl_str_mv |
Universidad de los Andes |
dc.identifier.reponame.none.fl_str_mv |
Repositorio Institucional Séneca |
dc.identifier.repourl.none.fl_str_mv |
https://repositorio.uniandes.edu.co/ |
identifier_str_mv |
978-958-798-779-9 Universidad de los Andes Repositorio Institucional Séneca |
url |
https://hdl.handle.net/1992/76061 https://doi.org/10.51573/Andes.PPS39.GS.MS.4 https://repositorio.uniandes.edu.co/ |
dc.language.iso.none.fl_str_mv |
eng |
language |
eng |
dc.relation.conferencedate.none.fl_str_mv |
05-19-2024/05-23-2024 |
dc.relation.conferenceplace.none.fl_str_mv |
Cartagena de Indias, Colombia |
dc.relation.ispartofconference.none.fl_str_mv |
Proceedings of the 39th International Conference of the Polymer Processing Society (PPS-39) |
dc.rights.uri.none.fl_str_mv |
https://repositorio.uniandes.edu.co/static/pdf/aceptacion_uso_es.pdf |
dc.rights.accessrights.none.fl_str_mv |
info:eu-repo/semantics/openAccess |
dc.rights.coar.none.fl_str_mv |
http://purl.org/coar/access_right/c_abf2 |
rights_invalid_str_mv |
https://repositorio.uniandes.edu.co/static/pdf/aceptacion_uso_es.pdf http://purl.org/coar/access_right/c_abf2 |
eu_rights_str_mv |
openAccess |
dc.format.extent.none.fl_str_mv |
11 páginas |
dc.format.mimetype.none.fl_str_mv |
application/pdf |
dc.publisher.none.fl_str_mv |
Ediciones Uniandes |
dc.publisher.faculty.none.fl_str_mv |
Facultad de Ingeniería |
dc.publisher.place.none.fl_str_mv |
Bogotá |
publisher.none.fl_str_mv |
Ediciones Uniandes |
institution |
Universidad de los Andes |
bitstream.url.fl_str_mv |
https://repositorio.uniandes.edu.co/bitstreams/cf61bc81-97b2-4b18-9a27-eb2f6614d3cd/download https://repositorio.uniandes.edu.co/bitstreams/9ba547a5-7566-4b12-b6fe-2aa210a5ed45/download https://repositorio.uniandes.edu.co/bitstreams/b9024351-4415-44d1-b3a0-e522622e6c36/download https://repositorio.uniandes.edu.co/bitstreams/cff7124a-0be9-4eb7-9a9b-d3ce0b52e632/download https://repositorio.uniandes.edu.co/bitstreams/5ed32177-5fa5-4d50-87bf-05ae26e1277b/download https://repositorio.uniandes.edu.co/bitstreams/5e1f06ff-cbd5-42a2-8034-1f2ddb0cd09f/download https://repositorio.uniandes.edu.co/bitstreams/6f21d96c-09ae-4f1a-8637-cc6617876c47/download |
bitstream.checksum.fl_str_mv |
1f01e9b104fe4e32a3b29903b6fffb42 1a4167320c0649ec0cdfce2160710932 ae9e573a68e7f92501b6913cc846c39f 1cc709e9e0a6c2cccdbce4cb3a46d005 69174b600c2dcdb5a80d73e8333510b8 82ab762f5398241a90a3e81b57bdafbb 3a1b51cc2a69de96dd989b0ef9042f8a |
bitstream.checksumAlgorithm.fl_str_mv |
MD5 MD5 MD5 MD5 MD5 MD5 MD5 |
repository.name.fl_str_mv |
Repositorio institucional Séneca |
repository.mail.fl_str_mv |
adminrepositorio@uniandes.edu.co |
_version_ |
1831927737096339456 |
spelling |
Naderer, ThomasHammer, AlexanderRoland, WolfgangZacher, MaximilianBerger-Weber, GeraldSalcedo, FelipePerilla, Jairo ErnestoSierra, CesarMedina, Jorge Alberto2025-02-07T20:24:29Z2025-02-07T20:24:29Z2024-12978-958-798-779-9https://hdl.handle.net/1992/76061https://doi.org/10.51573/Andes.PPS39.GS.MS.4Universidad de los AndesRepositorio Institucional Sénecahttps://repositorio.uniandes.edu.co/The accuracy of viscosity predictions is a crucial aspect of polymer melt flow modeling and essential for the design of coextrusion die systems. In the field of non-Newtonian fluid modeling for coextrusion flows through rectangular ducts, significant progress has been made in understanding multilayer flow dynamics. Our fundamental research, employing numerical techniques such as the shooting method, finite element method, and finite difference method for flow evaluation, has established a critical base for the field. Our current research advances fluid dynamics by refining our existing numerical solver, specifically developed for multilayer coextrusion flows. We aim to enhance the solver’s performance by implementing more sophisticated calculations of shear rates that go beyond the traditional approach. The traditional approach often relies on average flow velocities and channel heights, which can underrepresent the complexity of experimentally studied polymer multilayer flows. Our study systematically compares various definitions for characteristic shear rates to describe the local shear rate dependent viscosity behavior using, for instance, a local power law model. A thorough error analysis quantifies the accuracy of each model and its predictive limitations for industrially relevant material combinations and operating conditions. This includes CFD simulations and experimental data comparisons, employing methods aligned with our fundamental research in this area. Furthermore, our work paves the way for integrating these advanced fluid dynamics models into the evolving field of process digitalization, thereby contributing to the development of more efficient, digitally integrated manufacturing processes.11 páginasapplication/pdfengEdiciones UniandesFacultad de IngenieríaBogotáhttps://repositorio.uniandes.edu.co/static/pdf/aceptacion_uso_es.pdfinfo:eu-repo/semantics/openAccesshttp://purl.org/coar/access_right/c_abf2Optimizing modeling the multilayer coextrusion flow of non-newtonian fluids through rectangular ducts: appropriate shear rate definition for a local power law formulationDocumento de Conferenciainfo:eu-repo/semantics/conferenceObjectinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_8544http://purl.org/coar/resource_type/c_c94fhttp://purl.org/coar/version/c_970fb48d4fbd8a85TextCoextrusionPolymeric multilayer structuresCFDIngeniería05-19-2024/05-23-2024Cartagena de Indias, ColombiaProceedings of the 39th International Conference of the Polymer Processing Society (PPS-39)ORIGINALPPS-39 - Optimizing Modeling the Multilayer Coextrusion Flow of Non-Newtonian Fluids Through Rectangular Ducts Appropriate Shear Rate Definition fo.pdfPPS-39 - Optimizing Modeling the Multilayer Coextrusion Flow of Non-Newtonian Fluids Through Rectangular Ducts Appropriate Shear Rate Definition fo.pdfapplication/pdf706139https://repositorio.uniandes.edu.co/bitstreams/cf61bc81-97b2-4b18-9a27-eb2f6614d3cd/download1f01e9b104fe4e32a3b29903b6fffb42MD51S14-90_LICENCIA Optimizing modeling the multilayer coextrusion flow.pdfHIDEapplication/pdf99290https://repositorio.uniandes.edu.co/bitstreams/9ba547a5-7566-4b12-b6fe-2aa210a5ed45/download1a4167320c0649ec0cdfce2160710932MD55LICENSElicense.txtlicense.txttext/plain; charset=utf-82535https://repositorio.uniandes.edu.co/bitstreams/b9024351-4415-44d1-b3a0-e522622e6c36/downloadae9e573a68e7f92501b6913cc846c39fMD52TEXTPPS-39 - Optimizing Modeling the Multilayer Coextrusion Flow of Non-Newtonian Fluids Through Rectangular Ducts Appropriate Shear Rate Definition fo.pdf.txtPPS-39 - Optimizing Modeling the Multilayer Coextrusion Flow of Non-Newtonian Fluids Through Rectangular Ducts Appropriate Shear Rate Definition fo.pdf.txtExtracted texttext/plain22523https://repositorio.uniandes.edu.co/bitstreams/cff7124a-0be9-4eb7-9a9b-d3ce0b52e632/download1cc709e9e0a6c2cccdbce4cb3a46d005MD53S14-90_LICENCIA Optimizing modeling the multilayer coextrusion flow.pdf.txtS14-90_LICENCIA Optimizing modeling the multilayer coextrusion flow.pdf.txtExtracted texttext/plain2230https://repositorio.uniandes.edu.co/bitstreams/5ed32177-5fa5-4d50-87bf-05ae26e1277b/download69174b600c2dcdb5a80d73e8333510b8MD56THUMBNAILPPS-39 - Optimizing Modeling the Multilayer Coextrusion Flow of Non-Newtonian Fluids Through Rectangular Ducts Appropriate Shear Rate Definition fo.pdf.jpgPPS-39 - Optimizing Modeling the Multilayer Coextrusion Flow of Non-Newtonian Fluids Through Rectangular Ducts Appropriate Shear Rate Definition fo.pdf.jpgGenerated Thumbnailimage/jpeg8848https://repositorio.uniandes.edu.co/bitstreams/5e1f06ff-cbd5-42a2-8034-1f2ddb0cd09f/download82ab762f5398241a90a3e81b57bdafbbMD54S14-90_LICENCIA Optimizing modeling the multilayer coextrusion flow.pdf.jpgS14-90_LICENCIA Optimizing modeling the multilayer coextrusion flow.pdf.jpgGenerated Thumbnailimage/jpeg13355https://repositorio.uniandes.edu.co/bitstreams/6f21d96c-09ae-4f1a-8637-cc6617876c47/download3a1b51cc2a69de96dd989b0ef9042f8aMD571992/76061oai:repositorio.uniandes.edu.co:1992/760612025-03-05 10:12:09.382https://repositorio.uniandes.edu.co/static/pdf/aceptacion_uso_es.pdfopen.accesshttps://repositorio.uniandes.edu.coRepositorio institucional Sénecaadminrepositorio@uniandes.edu.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 |