Integrated furfural and first generation bioethanol production: process simulation and techno-economic analysis
Autor(a) principal: | |
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Data de Publicação: | 2017 |
Outros Autores: | , , , , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Brazilian Journal of Chemical Engineering |
Texto Completo: | http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322017000300623 |
Resumo: | Abstract Furfural is a base chemical with a wide range of applications and with a great opportunity for market growth in the near term. Derived from biomass, its production may be incorporated to the Brazilian chemical industry using sugarcane bagasse as feedstock. In this context, the integration of a furfural plant to a first generation bioethanol facility, within the biorefinery concept, was simulated considering different scenarios compared to an autonomous bioethanol distillery. The economic analysis of the different scenarios showed that the revenues from furfural commercialization increase the internal rate of return of the project for maximum furfural production (22.0%) in comparison to a conventional ethanol distillery (13.5%), despite the decrease in electricity output. Moreover, the economic analysis of the results pointed out the possibility of lowering furfural prices to levels that could lead to its use as a precursor for biofuels. |
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Integrated furfural and first generation bioethanol production: process simulation and techno-economic analysisBiorefineryFurfuralBioethanolSugarcaneBagasseAbstract Furfural is a base chemical with a wide range of applications and with a great opportunity for market growth in the near term. Derived from biomass, its production may be incorporated to the Brazilian chemical industry using sugarcane bagasse as feedstock. In this context, the integration of a furfural plant to a first generation bioethanol facility, within the biorefinery concept, was simulated considering different scenarios compared to an autonomous bioethanol distillery. The economic analysis of the different scenarios showed that the revenues from furfural commercialization increase the internal rate of return of the project for maximum furfural production (22.0%) in comparison to a conventional ethanol distillery (13.5%), despite the decrease in electricity output. Moreover, the economic analysis of the results pointed out the possibility of lowering furfural prices to levels that could lead to its use as a precursor for biofuels.Brazilian Society of Chemical Engineering2017-07-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322017000300623Brazilian Journal of Chemical Engineering v.34 n.3 2017reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/0104-6632.20170343s20150643info:eu-repo/semantics/openAccessSilva,J. F. L.Selicani,M. A.Junqueira,T. L.Klein,B. C.Vaz Júnior,S.Bonomi,A.eng2018-02-01T00:00:00Zoai:scielo:S0104-66322017000300623Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2018-02-01T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false |
dc.title.none.fl_str_mv |
Integrated furfural and first generation bioethanol production: process simulation and techno-economic analysis |
title |
Integrated furfural and first generation bioethanol production: process simulation and techno-economic analysis |
spellingShingle |
Integrated furfural and first generation bioethanol production: process simulation and techno-economic analysis Silva,J. F. L. Biorefinery Furfural Bioethanol Sugarcane Bagasse |
title_short |
Integrated furfural and first generation bioethanol production: process simulation and techno-economic analysis |
title_full |
Integrated furfural and first generation bioethanol production: process simulation and techno-economic analysis |
title_fullStr |
Integrated furfural and first generation bioethanol production: process simulation and techno-economic analysis |
title_full_unstemmed |
Integrated furfural and first generation bioethanol production: process simulation and techno-economic analysis |
title_sort |
Integrated furfural and first generation bioethanol production: process simulation and techno-economic analysis |
author |
Silva,J. F. L. |
author_facet |
Silva,J. F. L. Selicani,M. A. Junqueira,T. L. Klein,B. C. Vaz Júnior,S. Bonomi,A. |
author_role |
author |
author2 |
Selicani,M. A. Junqueira,T. L. Klein,B. C. Vaz Júnior,S. Bonomi,A. |
author2_role |
author author author author author |
dc.contributor.author.fl_str_mv |
Silva,J. F. L. Selicani,M. A. Junqueira,T. L. Klein,B. C. Vaz Júnior,S. Bonomi,A. |
dc.subject.por.fl_str_mv |
Biorefinery Furfural Bioethanol Sugarcane Bagasse |
topic |
Biorefinery Furfural Bioethanol Sugarcane Bagasse |
description |
Abstract Furfural is a base chemical with a wide range of applications and with a great opportunity for market growth in the near term. Derived from biomass, its production may be incorporated to the Brazilian chemical industry using sugarcane bagasse as feedstock. In this context, the integration of a furfural plant to a first generation bioethanol facility, within the biorefinery concept, was simulated considering different scenarios compared to an autonomous bioethanol distillery. The economic analysis of the different scenarios showed that the revenues from furfural commercialization increase the internal rate of return of the project for maximum furfural production (22.0%) in comparison to a conventional ethanol distillery (13.5%), despite the decrease in electricity output. Moreover, the economic analysis of the results pointed out the possibility of lowering furfural prices to levels that could lead to its use as a precursor for biofuels. |
publishDate |
2017 |
dc.date.none.fl_str_mv |
2017-07-01 |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
format |
article |
status_str |
publishedVersion |
dc.identifier.uri.fl_str_mv |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322017000300623 |
url |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322017000300623 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
10.1590/0104-6632.20170343s20150643 |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
text/html |
dc.publisher.none.fl_str_mv |
Brazilian Society of Chemical Engineering |
publisher.none.fl_str_mv |
Brazilian Society of Chemical Engineering |
dc.source.none.fl_str_mv |
Brazilian Journal of Chemical Engineering v.34 n.3 2017 reponame:Brazilian Journal of Chemical Engineering instname:Associação Brasileira de Engenharia Química (ABEQ) instacron:ABEQ |
instname_str |
Associação Brasileira de Engenharia Química (ABEQ) |
instacron_str |
ABEQ |
institution |
ABEQ |
reponame_str |
Brazilian Journal of Chemical Engineering |
collection |
Brazilian Journal of Chemical Engineering |
repository.name.fl_str_mv |
Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ) |
repository.mail.fl_str_mv |
rgiudici@usp.br||rgiudici@usp.br |
_version_ |
1754213175513841664 |