Continuous adiabatic industrial benzene nitration with mixed acid at a pilot plant scale

Detalhes bibliográficos
Autor(a) principal: Quadros, Paulo A.
Data de Publicação: 2005
Outros Autores: Oliveira, Nuno M. C., Baptista, Cristina M. S. G.
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
Texto Completo: http://hdl.handle.net/10316/3804
https://doi.org/10.1016/j.cej.2004.12.022
Resumo: A pilot plant for the continuous adiabatic nitration of benzene was constructed, reproducing the industrial operating conditions, in order to identify the reaction regime prevailing in this industrial process. Important process parameters were tested covering a wide range of operating conditions: reaction temperature (80-135 °C), benzene to nitric acid molar feed ratio (0.96-1.15) and stirring speed (390-1700 rpm). The residence time and the sulphuric acid strength were fixed at 2 min and 68%, respectively. The data from a large number of experiments show a good agreement with the results of a mathematical model of the reactor.
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spelling Continuous adiabatic industrial benzene nitration with mixed acid at a pilot plant scaleBenzene nitrationFilm modelIntermediate reaction regimeLiquid-liquid reactionHeterogeneous reactionMass transferA pilot plant for the continuous adiabatic nitration of benzene was constructed, reproducing the industrial operating conditions, in order to identify the reaction regime prevailing in this industrial process. Important process parameters were tested covering a wide range of operating conditions: reaction temperature (80-135 °C), benzene to nitric acid molar feed ratio (0.96-1.15) and stirring speed (390-1700 rpm). The residence time and the sulphuric acid strength were fixed at 2 min and 68%, respectively. The data from a large number of experiments show a good agreement with the results of a mathematical model of the reactor.http://www.sciencedirect.com/science/article/B6TFJ-4F7S18J-1/1/149c666ae3f7421d65606a679b66a4522005info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleaplication/PDFhttp://hdl.handle.net/10316/3804http://hdl.handle.net/10316/3804https://doi.org/10.1016/j.cej.2004.12.022engChemical Engineering Journal. 108:1-2 (2005) 1-11Quadros, Paulo A.Oliveira, Nuno M. C.Baptista, Cristina M. S. G.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:RCAAP2020-11-06T16:48:52Zoai:estudogeral.uc.pt:10316/3804Portal AgregadorONGhttps://www.rcaap.pt/oai/openaireopendoar:71602024-03-19T20:59:13.431616Repositório 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 Continuous adiabatic industrial benzene nitration with mixed acid at a pilot plant scale
title Continuous adiabatic industrial benzene nitration with mixed acid at a pilot plant scale
spellingShingle Continuous adiabatic industrial benzene nitration with mixed acid at a pilot plant scale
Quadros, Paulo A.
Benzene nitration
Film model
Intermediate reaction regime
Liquid-liquid reaction
Heterogeneous reaction
Mass transfer
title_short Continuous adiabatic industrial benzene nitration with mixed acid at a pilot plant scale
title_full Continuous adiabatic industrial benzene nitration with mixed acid at a pilot plant scale
title_fullStr Continuous adiabatic industrial benzene nitration with mixed acid at a pilot plant scale
title_full_unstemmed Continuous adiabatic industrial benzene nitration with mixed acid at a pilot plant scale
title_sort Continuous adiabatic industrial benzene nitration with mixed acid at a pilot plant scale
author Quadros, Paulo A.
author_facet Quadros, Paulo A.
Oliveira, Nuno M. C.
Baptista, Cristina M. S. G.
author_role author
author2 Oliveira, Nuno M. C.
Baptista, Cristina M. S. G.
author2_role author
author
dc.contributor.author.fl_str_mv Quadros, Paulo A.
Oliveira, Nuno M. C.
Baptista, Cristina M. S. G.
dc.subject.por.fl_str_mv Benzene nitration
Film model
Intermediate reaction regime
Liquid-liquid reaction
Heterogeneous reaction
Mass transfer
topic Benzene nitration
Film model
Intermediate reaction regime
Liquid-liquid reaction
Heterogeneous reaction
Mass transfer
description A pilot plant for the continuous adiabatic nitration of benzene was constructed, reproducing the industrial operating conditions, in order to identify the reaction regime prevailing in this industrial process. Important process parameters were tested covering a wide range of operating conditions: reaction temperature (80-135 °C), benzene to nitric acid molar feed ratio (0.96-1.15) and stirring speed (390-1700 rpm). The residence time and the sulphuric acid strength were fixed at 2 min and 68%, respectively. The data from a large number of experiments show a good agreement with the results of a mathematical model of the reactor.
publishDate 2005
dc.date.none.fl_str_mv 2005
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/article
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dc.identifier.uri.fl_str_mv http://hdl.handle.net/10316/3804
http://hdl.handle.net/10316/3804
https://doi.org/10.1016/j.cej.2004.12.022
url http://hdl.handle.net/10316/3804
https://doi.org/10.1016/j.cej.2004.12.022
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv Chemical Engineering Journal. 108:1-2 (2005) 1-11
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dc.format.none.fl_str_mv aplication/PDF
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