Simulation of membrane separations using a modified Maxwell-Stefan model
Autor(a) principal: | |
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Data de Publicação: | 2009 |
Outros Autores: | , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) |
Texto Completo: | http://hdl.handle.net/10198/1265 |
Resumo: | In this work, a modified Maxwell-Stefan model, which considers both the concentration polarization and the transport through the membrane, is tested for the simulation of Dextran T70 aqueous solutions filtration. Numerical simulations by solving the model equations with an adaptive resolution algorithm, based on the Adaptive Method of Lines, determined the concentration profiles in the polarization layer and inside the membrane pore. It is shown that the formation of significant solute accumulation at the membrane/polarization interface leads to high levels of apparent rejection. A tubular cross-flow ultrafiltration module, containing a tubular polysulfone membrane with a molecular weight cut-off of 50 kDa, was used to perform the experiments. The model is able to successfully simulate data in the high rejection/low flux region using an equilibrium constant Keq of 0.25, but does not reproduce the observed rejection drop/pressure build-up which occurs for increased fluxes, which may be due to limitations of the model itself. |
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Simulation of membrane separations using a modified Maxwell-Stefan modelModelingUltrafiltrationMaxwell Stefan equationApparent rejectionAdaptive methodsIn this work, a modified Maxwell-Stefan model, which considers both the concentration polarization and the transport through the membrane, is tested for the simulation of Dextran T70 aqueous solutions filtration. Numerical simulations by solving the model equations with an adaptive resolution algorithm, based on the Adaptive Method of Lines, determined the concentration profiles in the polarization layer and inside the membrane pore. It is shown that the formation of significant solute accumulation at the membrane/polarization interface leads to high levels of apparent rejection. A tubular cross-flow ultrafiltration module, containing a tubular polysulfone membrane with a molecular weight cut-off of 50 kDa, was used to perform the experiments. The model is able to successfully simulate data in the high rejection/low flux region using an equilibrium constant Keq of 0.25, but does not reproduce the observed rejection drop/pressure build-up which occurs for increased fluxes, which may be due to limitations of the model itself.The Berkeley Electronic PressBiblioteca Digital do IPBBrito, PauloGando-Ferreira, Licínio M.Portugal, António2010-01-12T12:02:13Z20092009-01-01T00:00:00Zinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleapplication/pdfhttp://hdl.handle.net/10198/1265engBrito, Paulo; Gando-Ferreira, Licínio M.; Portugal, António (2009). Simulation of membrane separations using a modified Maxwell-Stefan model. Chemical Product and Process Modeling. ISSN 1538-0645. 4:4, p.1-121934-2659info:eu-repo/semantics/openAccessreponame:Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)instname:Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informaçãoinstacron:RCAAP2023-11-21T10:04:44Zoai:bibliotecadigital.ipb.pt:10198/1265Portal AgregadorONGhttps://www.rcaap.pt/oai/openaireopendoar:71602024-03-19T22:54:47.794108Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) - Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informaçãofalse |
dc.title.none.fl_str_mv |
Simulation of membrane separations using a modified Maxwell-Stefan model |
title |
Simulation of membrane separations using a modified Maxwell-Stefan model |
spellingShingle |
Simulation of membrane separations using a modified Maxwell-Stefan model Brito, Paulo Modeling Ultrafiltration Maxwell Stefan equation Apparent rejection Adaptive methods |
title_short |
Simulation of membrane separations using a modified Maxwell-Stefan model |
title_full |
Simulation of membrane separations using a modified Maxwell-Stefan model |
title_fullStr |
Simulation of membrane separations using a modified Maxwell-Stefan model |
title_full_unstemmed |
Simulation of membrane separations using a modified Maxwell-Stefan model |
title_sort |
Simulation of membrane separations using a modified Maxwell-Stefan model |
author |
Brito, Paulo |
author_facet |
Brito, Paulo Gando-Ferreira, Licínio M. Portugal, António |
author_role |
author |
author2 |
Gando-Ferreira, Licínio M. Portugal, António |
author2_role |
author author |
dc.contributor.none.fl_str_mv |
Biblioteca Digital do IPB |
dc.contributor.author.fl_str_mv |
Brito, Paulo Gando-Ferreira, Licínio M. Portugal, António |
dc.subject.por.fl_str_mv |
Modeling Ultrafiltration Maxwell Stefan equation Apparent rejection Adaptive methods |
topic |
Modeling Ultrafiltration Maxwell Stefan equation Apparent rejection Adaptive methods |
description |
In this work, a modified Maxwell-Stefan model, which considers both the concentration polarization and the transport through the membrane, is tested for the simulation of Dextran T70 aqueous solutions filtration. Numerical simulations by solving the model equations with an adaptive resolution algorithm, based on the Adaptive Method of Lines, determined the concentration profiles in the polarization layer and inside the membrane pore. It is shown that the formation of significant solute accumulation at the membrane/polarization interface leads to high levels of apparent rejection. A tubular cross-flow ultrafiltration module, containing a tubular polysulfone membrane with a molecular weight cut-off of 50 kDa, was used to perform the experiments. The model is able to successfully simulate data in the high rejection/low flux region using an equilibrium constant Keq of 0.25, but does not reproduce the observed rejection drop/pressure build-up which occurs for increased fluxes, which may be due to limitations of the model itself. |
publishDate |
2009 |
dc.date.none.fl_str_mv |
2009 2009-01-01T00:00:00Z 2010-01-12T12:02:13Z |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article |
format |
article |
status_str |
publishedVersion |
dc.identifier.uri.fl_str_mv |
http://hdl.handle.net/10198/1265 |
url |
http://hdl.handle.net/10198/1265 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
Brito, Paulo; Gando-Ferreira, Licínio M.; Portugal, António (2009). Simulation of membrane separations using a modified Maxwell-Stefan model. Chemical Product and Process Modeling. ISSN 1538-0645. 4:4, p.1-12 1934-2659 |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
application/pdf |
dc.publisher.none.fl_str_mv |
The Berkeley Electronic Press |
publisher.none.fl_str_mv |
The Berkeley Electronic Press |
dc.source.none.fl_str_mv |
reponame:Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) instname:Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação instacron:RCAAP |
instname_str |
Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação |
instacron_str |
RCAAP |
institution |
RCAAP |
reponame_str |
Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) |
collection |
Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) |
repository.name.fl_str_mv |
Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) - Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação |
repository.mail.fl_str_mv |
|
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1799135147872747520 |