Structured catalysts for partial oxidations

Detalhes bibliográficos
Autor(a) principal: Campos, Victor J. M. de
Data de Publicação: 2001
Outros Autores: Quinta-Ferreira, Rosa M.
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
Texto Completo: http://hdl.handle.net/10316/3825
https://doi.org/10.1016/S0920-5861(01)00362-5
Resumo: The objective of the present work is centred on the analysis of the behaviour of fixed-bed reactors packed with structured catalysts when a partial oxidation takes place. The fluid flow within an element, formed by the intersection of two adjacent corrugated plates, was mathematically modelled and numerical simulations were performed in order to study possible optimising of the catalyst structure. A simple model, involving the continuous stirred tank approach, was used to simulate the performance of the catalyst in an industrial reactor. The profiles of temperature, concentration, velocity and pressure along the reactor were obtained through the global mass balance, partial molar balances, conservation of moment, energy balance and mechanical energy balance. These equations were applied to an exothermic reactional system, the selective oxidation of methanol to formaldehyde, in order to evaluate the possibility of application of these catalysts in industry. Various parameters specific to the catalyst and the reactional system were tested in order to achieve a better understanding of the behaviour of these structured packing. The comparison with the heterogeneous model predictions for a random packing and with industrial values pointed out that the choice of parameters is fundamental to the performance of the catalyst. The adjustments to the parameters allows for significant improvements in some of the more troublesome aspects of the reactional system. Lowering the hot-spot, reducing the progress of the secondary reaction and reducing the pressure drop are the main enhancements that these structured catalysts can offer.
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spelling Structured catalysts for partial oxidationsPartial oxidationsFixed-bed reactorsStructured catalystsThe objective of the present work is centred on the analysis of the behaviour of fixed-bed reactors packed with structured catalysts when a partial oxidation takes place. The fluid flow within an element, formed by the intersection of two adjacent corrugated plates, was mathematically modelled and numerical simulations were performed in order to study possible optimising of the catalyst structure. A simple model, involving the continuous stirred tank approach, was used to simulate the performance of the catalyst in an industrial reactor. The profiles of temperature, concentration, velocity and pressure along the reactor were obtained through the global mass balance, partial molar balances, conservation of moment, energy balance and mechanical energy balance. These equations were applied to an exothermic reactional system, the selective oxidation of methanol to formaldehyde, in order to evaluate the possibility of application of these catalysts in industry. Various parameters specific to the catalyst and the reactional system were tested in order to achieve a better understanding of the behaviour of these structured packing. The comparison with the heterogeneous model predictions for a random packing and with industrial values pointed out that the choice of parameters is fundamental to the performance of the catalyst. The adjustments to the parameters allows for significant improvements in some of the more troublesome aspects of the reactional system. Lowering the hot-spot, reducing the progress of the secondary reaction and reducing the pressure drop are the main enhancements that these structured catalysts can offer.http://www.sciencedirect.com/science/article/B6TFG-441R2VP-J/1/a53f1742755818c07b0e6fa5435238432001info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleaplication/PDFhttp://hdl.handle.net/10316/3825http://hdl.handle.net/10316/3825https://doi.org/10.1016/S0920-5861(01)00362-5engCatalysis Today. 69:1-4 (2001) 121-129Campos, Victor J. M. deQuinta-Ferreira, Rosa M.info: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:RCAAP2020-11-06T16:59:53Zoai:estudogeral.uc.pt:10316/3825Portal AgregadorONGhttps://www.rcaap.pt/oai/openaireopendoar:71602024-03-19T20:59:20.333243Repositório 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 Structured catalysts for partial oxidations
title Structured catalysts for partial oxidations
spellingShingle Structured catalysts for partial oxidations
Campos, Victor J. M. de
Partial oxidations
Fixed-bed reactors
Structured catalysts
title_short Structured catalysts for partial oxidations
title_full Structured catalysts for partial oxidations
title_fullStr Structured catalysts for partial oxidations
title_full_unstemmed Structured catalysts for partial oxidations
title_sort Structured catalysts for partial oxidations
author Campos, Victor J. M. de
author_facet Campos, Victor J. M. de
Quinta-Ferreira, Rosa M.
author_role author
author2 Quinta-Ferreira, Rosa M.
author2_role author
dc.contributor.author.fl_str_mv Campos, Victor J. M. de
Quinta-Ferreira, Rosa M.
dc.subject.por.fl_str_mv Partial oxidations
Fixed-bed reactors
Structured catalysts
topic Partial oxidations
Fixed-bed reactors
Structured catalysts
description The objective of the present work is centred on the analysis of the behaviour of fixed-bed reactors packed with structured catalysts when a partial oxidation takes place. The fluid flow within an element, formed by the intersection of two adjacent corrugated plates, was mathematically modelled and numerical simulations were performed in order to study possible optimising of the catalyst structure. A simple model, involving the continuous stirred tank approach, was used to simulate the performance of the catalyst in an industrial reactor. The profiles of temperature, concentration, velocity and pressure along the reactor were obtained through the global mass balance, partial molar balances, conservation of moment, energy balance and mechanical energy balance. These equations were applied to an exothermic reactional system, the selective oxidation of methanol to formaldehyde, in order to evaluate the possibility of application of these catalysts in industry. Various parameters specific to the catalyst and the reactional system were tested in order to achieve a better understanding of the behaviour of these structured packing. The comparison with the heterogeneous model predictions for a random packing and with industrial values pointed out that the choice of parameters is fundamental to the performance of the catalyst. The adjustments to the parameters allows for significant improvements in some of the more troublesome aspects of the reactional system. Lowering the hot-spot, reducing the progress of the secondary reaction and reducing the pressure drop are the main enhancements that these structured catalysts can offer.
publishDate 2001
dc.date.none.fl_str_mv 2001
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dc.type.driver.fl_str_mv info:eu-repo/semantics/article
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status_str publishedVersion
dc.identifier.uri.fl_str_mv http://hdl.handle.net/10316/3825
http://hdl.handle.net/10316/3825
https://doi.org/10.1016/S0920-5861(01)00362-5
url http://hdl.handle.net/10316/3825
https://doi.org/10.1016/S0920-5861(01)00362-5
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv Catalysis Today. 69:1-4 (2001) 121-129
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eu_rights_str_mv openAccess
dc.format.none.fl_str_mv aplication/PDF
dc.source.none.fl_str_mv reponame:Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
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