Comparison of the performance of integrated and sequential reaction and separation units in terms of recovery of a desired product

Detalhes bibliográficos
Autor(a) principal: Paiva, Ana L.
Data de Publicação: 2000
Outros Autores: Malcata, F. Xavier
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
Texto Completo: http://hdl.handle.net/10400.14/6805
Resumo: Integration of reaction and separation has experienced fast progress in this decade because it provides a convenient way of alleviating kinetic and/or thermodynamic constraints usually present in the more traditional sequential con"guration (where reaction is followed by separation), which limit the extent of reaction and also the purity of the products obtained thereby. The aim of this work was to quantitatively compare the "nal recovery of a desired product in an integrated processing unit and in a sequential one, in the case of a unireactant/uniproduct reaction occuring in an (ideal) liquid phase with separation via liquid/vapor equilibrium. The objective function was set as the local temperature which maximizes the recovery of product in the vapor phase leaving the integrated unit or the separator (as appropriate). It was concluded that (i) the optimum temperature looks as a local maximum for the integrated system and as a global maximum for the sequential one, (ii) it strongly depends on the equilibrium constant of the reaction in question and (iii) it assumes lower (and economically feasible) values only in the case of the integrated unit
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spelling Comparison of the performance of integrated and sequential reaction and separation units in terms of recovery of a desired productMathematical modellingSequential reaction and separationIntegrationIntegration of reaction and separation has experienced fast progress in this decade because it provides a convenient way of alleviating kinetic and/or thermodynamic constraints usually present in the more traditional sequential con"guration (where reaction is followed by separation), which limit the extent of reaction and also the purity of the products obtained thereby. The aim of this work was to quantitatively compare the "nal recovery of a desired product in an integrated processing unit and in a sequential one, in the case of a unireactant/uniproduct reaction occuring in an (ideal) liquid phase with separation via liquid/vapor equilibrium. The objective function was set as the local temperature which maximizes the recovery of product in the vapor phase leaving the integrated unit or the separator (as appropriate). It was concluded that (i) the optimum temperature looks as a local maximum for the integrated system and as a global maximum for the sequential one, (ii) it strongly depends on the equilibrium constant of the reaction in question and (iii) it assumes lower (and economically feasible) values only in the case of the integrated unitElsevierVeritati - Repositório Institucional da Universidade Católica PortuguesaPaiva, Ana L.Malcata, F. Xavier2011-10-22T11:56:56Z20002000-01-01T00:00:00Zinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleapplication/pdfhttp://hdl.handle.net/10400.14/6805engPAIVA, Ana L.; Malcata, F. Xavier - separation units in terms of recovery of a desired product. Chemical Engineering Science. ISSN 0009-2509. Vol. 55 (2000), p. 589-59910.1016/S0009-2509(99)00155-4info: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:RCAAP2023-07-12T17:10:39Zoai:repositorio.ucp.pt:10400.14/6805Portal AgregadorONGhttps://www.rcaap.pt/oai/openaireopendoar:71602024-03-19T18:05:53.160983Repositório 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 Comparison of the performance of integrated and sequential reaction and separation units in terms of recovery of a desired product
title Comparison of the performance of integrated and sequential reaction and separation units in terms of recovery of a desired product
spellingShingle Comparison of the performance of integrated and sequential reaction and separation units in terms of recovery of a desired product
Paiva, Ana L.
Mathematical modelling
Sequential reaction and separation
Integration
title_short Comparison of the performance of integrated and sequential reaction and separation units in terms of recovery of a desired product
title_full Comparison of the performance of integrated and sequential reaction and separation units in terms of recovery of a desired product
title_fullStr Comparison of the performance of integrated and sequential reaction and separation units in terms of recovery of a desired product
title_full_unstemmed Comparison of the performance of integrated and sequential reaction and separation units in terms of recovery of a desired product
title_sort Comparison of the performance of integrated and sequential reaction and separation units in terms of recovery of a desired product
author Paiva, Ana L.
author_facet Paiva, Ana L.
Malcata, F. Xavier
author_role author
author2 Malcata, F. Xavier
author2_role author
dc.contributor.none.fl_str_mv Veritati - Repositório Institucional da Universidade Católica Portuguesa
dc.contributor.author.fl_str_mv Paiva, Ana L.
Malcata, F. Xavier
dc.subject.por.fl_str_mv Mathematical modelling
Sequential reaction and separation
Integration
topic Mathematical modelling
Sequential reaction and separation
Integration
description Integration of reaction and separation has experienced fast progress in this decade because it provides a convenient way of alleviating kinetic and/or thermodynamic constraints usually present in the more traditional sequential con"guration (where reaction is followed by separation), which limit the extent of reaction and also the purity of the products obtained thereby. The aim of this work was to quantitatively compare the "nal recovery of a desired product in an integrated processing unit and in a sequential one, in the case of a unireactant/uniproduct reaction occuring in an (ideal) liquid phase with separation via liquid/vapor equilibrium. The objective function was set as the local temperature which maximizes the recovery of product in the vapor phase leaving the integrated unit or the separator (as appropriate). It was concluded that (i) the optimum temperature looks as a local maximum for the integrated system and as a global maximum for the sequential one, (ii) it strongly depends on the equilibrium constant of the reaction in question and (iii) it assumes lower (and economically feasible) values only in the case of the integrated unit
publishDate 2000
dc.date.none.fl_str_mv 2000
2000-01-01T00:00:00Z
2011-10-22T11:56:56Z
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/10400.14/6805
url http://hdl.handle.net/10400.14/6805
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv PAIVA, Ana L.; Malcata, F. Xavier - separation units in terms of recovery of a desired product. Chemical Engineering Science. ISSN 0009-2509. Vol. 55 (2000), p. 589-599
10.1016/S0009-2509(99)00155-4
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
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dc.publisher.none.fl_str_mv Elsevier
publisher.none.fl_str_mv Elsevier
dc.source.none.fl_str_mv reponame:Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
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reponame_str Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
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