A new approach for bioethanol production from sugarcane bagasse using hydrodynamic cavitation assisted-pretreatment and column reactors

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Hydrodynamic cavitation (HC) was adopted to assist alkaline-hydrogen peroxide pretreatment of sugarcane bagasse (SCB). In the following condition: 0.29 M of NaOH, 0.78% (v/v) of H2O2, 9.95 min of process time and 3 bar of inlet pressure, 95.4% of digestibility of cellulosic fraction was achieved. To...

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Detalles Bibliográficos
Autores: Terán Hilares, Ruly, Kamoei, Douglas Viana, Ahmed, Muhammad Ajaz, da Silva, Silvio Silvério, Han, Jong-In, Santos, Júlio César Dos
Formato: artículo
Fecha de Publicación:2018
Institución:Consejo Nacional de Ciencia Tecnología e Innovación
Repositorio:CONCYTEC-Institucional
Lenguaje:inglés
OAI Identifier:oai:repositorio.concytec.gob.pe:20.500.12390/442
Enlace del recurso:https://hdl.handle.net/20.500.12390/442
https://doi.org/10.1016/j.ultsonch.2018.01.016
Nivel de acceso:acceso abierto
Materia:Sugarcane bagasse
Alkaline pretreatment
Ethanol production
Hydrodynamic cavitation
Hydrogen peroxide
Process intensification
http://purl.org/pe-repo/ocde/ford#1.04.01
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dc.title.none.fl_str_mv A new approach for bioethanol production from sugarcane bagasse using hydrodynamic cavitation assisted-pretreatment and column reactors
title A new approach for bioethanol production from sugarcane bagasse using hydrodynamic cavitation assisted-pretreatment and column reactors
spellingShingle A new approach for bioethanol production from sugarcane bagasse using hydrodynamic cavitation assisted-pretreatment and column reactors
Terán Hilares, Ruly
Sugarcane bagasse
Alkaline pretreatment
Ethanol production
Hydrodynamic cavitation
Hydrogen peroxide
Process intensification
http://purl.org/pe-repo/ocde/ford#1.04.01
title_short A new approach for bioethanol production from sugarcane bagasse using hydrodynamic cavitation assisted-pretreatment and column reactors
title_full A new approach for bioethanol production from sugarcane bagasse using hydrodynamic cavitation assisted-pretreatment and column reactors
title_fullStr A new approach for bioethanol production from sugarcane bagasse using hydrodynamic cavitation assisted-pretreatment and column reactors
title_full_unstemmed A new approach for bioethanol production from sugarcane bagasse using hydrodynamic cavitation assisted-pretreatment and column reactors
title_sort A new approach for bioethanol production from sugarcane bagasse using hydrodynamic cavitation assisted-pretreatment and column reactors
author Terán Hilares, Ruly
author_facet Terán Hilares, Ruly
Kamoei, Douglas Viana
Ahmed, Muhammad Ajaz
da Silva, Silvio Silvério
Han, Jong-In
Santos, Júlio César Dos
author_role author
author2 Kamoei, Douglas Viana
Ahmed, Muhammad Ajaz
da Silva, Silvio Silvério
Han, Jong-In
Santos, Júlio César Dos
author2_role author
author
author
author
author
dc.contributor.author.fl_str_mv Terán Hilares, Ruly
Kamoei, Douglas Viana
Ahmed, Muhammad Ajaz
da Silva, Silvio Silvério
Han, Jong-In
Santos, Júlio César Dos
dc.subject.none.fl_str_mv Sugarcane bagasse
topic Sugarcane bagasse
Alkaline pretreatment
Ethanol production
Hydrodynamic cavitation
Hydrogen peroxide
Process intensification
http://purl.org/pe-repo/ocde/ford#1.04.01
dc.subject.es_PE.fl_str_mv Alkaline pretreatment
Ethanol production
Hydrodynamic cavitation
Hydrogen peroxide
Process intensification
dc.subject.ocde.none.fl_str_mv http://purl.org/pe-repo/ocde/ford#1.04.01
description Hydrodynamic cavitation (HC) was adopted to assist alkaline-hydrogen peroxide pretreatment of sugarcane bagasse (SCB). In the following condition: 0.29 M of NaOH, 0.78% (v/v) of H2O2, 9.95 min of process time and 3 bar of inlet pressure, 95.4% of digestibility of cellulosic fraction was achieved. To take the best use of the pretreated biomass, the overall process was intensified by way of employing a packed bed flow-through column reactor and thus enabling to handle a high solid loading of 20%, thereby leading to cellulose and hemicellulose conversions to 74.7% and 75%, respectively. In the fermentation step, a bubble column reactor was introduced to maximize ethanol production from the pretreated SCB by Scheffersomyces stipitis NRRL-Y7124, resulting in 31.50 g/L of ethanol, 0.49 g/g of ethanol yield and 0.68 g/L.h of productivity. All this showed that our HC-assisted NaOH-H2O2 pretreatment strategy along with the process intensification approach might offer an option for SCB-based biorefineries.
publishDate 2018
dc.date.accessioned.none.fl_str_mv 2024-05-30T23:13:38Z
dc.date.available.none.fl_str_mv 2024-05-30T23:13:38Z
dc.date.issued.fl_str_mv 2018-05
dc.type.none.fl_str_mv info:eu-repo/semantics/article
format article
dc.identifier.uri.none.fl_str_mv https://hdl.handle.net/20.500.12390/442
dc.identifier.doi.none.fl_str_mv https://doi.org/10.1016/j.ultsonch.2018.01.016
dc.identifier.scopus.none.fl_str_mv 2-s2.0-85041483520
dc.identifier.pmid.none.fl_str_mv 29555278
url https://hdl.handle.net/20.500.12390/442
https://doi.org/10.1016/j.ultsonch.2018.01.016
identifier_str_mv 2-s2.0-85041483520
29555278
dc.language.iso.none.fl_str_mv eng
language eng
dc.relation.ispartof.none.fl_str_mv Ultrasonics sonochemistry
dc.rights.none.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.publisher.none.fl_str_mv Elsevier
publisher.none.fl_str_mv Elsevier
dc.source.none.fl_str_mv reponame:CONCYTEC-Institucional
instname:Consejo Nacional de Ciencia Tecnología e Innovación
instacron:CONCYTEC
instname_str Consejo Nacional de Ciencia Tecnología e Innovación
instacron_str CONCYTEC
institution CONCYTEC
reponame_str CONCYTEC-Institucional
collection CONCYTEC-Institucional
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bitstream.checksum.fl_str_mv 8a4605be74aa9ea9d79846c1fba20a33
bitstream.checksumAlgorithm.fl_str_mv MD5
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spelling Publicationrp00388600rp00386600rp00390600rp00387600rp00385600rp00389600Terán Hilares, RulyKamoei, Douglas VianaAhmed, Muhammad Ajazda Silva, Silvio SilvérioHan, Jong-InSantos, Júlio César Dos2024-05-30T23:13:38Z2024-05-30T23:13:38Z2018-05https://hdl.handle.net/20.500.12390/442https://doi.org/10.1016/j.ultsonch.2018.01.0162-s2.0-8504148352029555278Hydrodynamic cavitation (HC) was adopted to assist alkaline-hydrogen peroxide pretreatment of sugarcane bagasse (SCB). In the following condition: 0.29 M of NaOH, 0.78% (v/v) of H2O2, 9.95 min of process time and 3 bar of inlet pressure, 95.4% of digestibility of cellulosic fraction was achieved. To take the best use of the pretreated biomass, the overall process was intensified by way of employing a packed bed flow-through column reactor and thus enabling to handle a high solid loading of 20%, thereby leading to cellulose and hemicellulose conversions to 74.7% and 75%, respectively. In the fermentation step, a bubble column reactor was introduced to maximize ethanol production from the pretreated SCB by Scheffersomyces stipitis NRRL-Y7124, resulting in 31.50 g/L of ethanol, 0.49 g/g of ethanol yield and 0.68 g/L.h of productivity. All this showed that our HC-assisted NaOH-H2O2 pretreatment strategy along with the process intensification approach might offer an option for SCB-based biorefineries.Consejo Nacional de Ciencia, Tecnología e Innovación Tecnológica - ConcytecengElsevierUltrasonics sonochemistryinfo:eu-repo/semantics/openAccessSugarcane bagasseAlkaline pretreatment-1Ethanol production-1Hydrodynamic cavitation-1Hydrogen peroxide-1Process intensification-1http://purl.org/pe-repo/ocde/ford#1.04.01-1A new approach for bioethanol production from sugarcane bagasse using hydrodynamic cavitation assisted-pretreatment and column reactorsinfo:eu-repo/semantics/articlereponame:CONCYTEC-Institucionalinstname:Consejo Nacional de Ciencia Tecnología e Innovacióninstacron:CONCYTEC#PLACEHOLDER_PARENT_METADATA_VALUE##PLACEHOLDER_PARENT_METADATA_VALUE##PLACEHOLDER_PARENT_METADATA_VALUE##PLACEHOLDER_PARENT_METADATA_VALUE#LICENSElicense.txtlicense.txttext/plain; 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xmlns="https://www.openaire.eu/cerif-profile/1.1/" id="2bfa7cf5-29f0-4d61-a358-d9547584c543"> <Type xmlns="https://www.openaire.eu/cerif-profile/vocab/COAR_Publication_Types">http://purl.org/coar/resource_type/c_1843</Type> <Language>eng</Language> <Title>A new approach for bioethanol production from sugarcane bagasse using hydrodynamic cavitation assisted-pretreatment and column reactors</Title> <PublishedIn> <Publication> <Title>Ultrasonics sonochemistry</Title> </Publication> </PublishedIn> <PublicationDate>2018-05</PublicationDate> <DOI>https://doi.org/10.1016/j.ultsonch.2018.01.016</DOI> <PMCID>29555278</PMCID> <SCP-Number>2-s2.0-85041483520</SCP-Number> <Authors> <Author> <DisplayName>Terán Hilares, Ruly</DisplayName> <Person id="rp00388" /> <Affiliation> <OrgUnit> </OrgUnit> </Affiliation> </Author> <Author> <DisplayName>Kamoei, Douglas Viana</DisplayName> <Person id="rp00386" /> <Affiliation> <OrgUnit> </OrgUnit> </Affiliation> </Author> <Author> <DisplayName>Ahmed, Muhammad Ajaz</DisplayName> <Person id="rp00390" /> <Affiliation> <OrgUnit> </OrgUnit> </Affiliation> </Author> <Author> <DisplayName>da Silva, Silvio Silvério</DisplayName> <Person id="rp00387" /> <Affiliation> <OrgUnit> </OrgUnit> </Affiliation> </Author> <Author> <DisplayName>Han, Jong-In</DisplayName> <Person id="rp00385" /> <Affiliation> <OrgUnit> </OrgUnit> </Affiliation> </Author> <Author> <DisplayName>Santos, Júlio César Dos</DisplayName> <Person id="rp00389" /> <Affiliation> <OrgUnit> </OrgUnit> </Affiliation> </Author> </Authors> <Editors> </Editors> <Publishers> <Publisher> <DisplayName>Elsevier</DisplayName> <OrgUnit /> </Publisher> </Publishers> <Keyword>Sugarcane bagasse</Keyword> <Keyword>Alkaline pretreatment</Keyword> <Keyword>Ethanol production</Keyword> <Keyword>Hydrodynamic cavitation</Keyword> <Keyword>Hydrogen peroxide</Keyword> <Keyword>Process intensification</Keyword> <Abstract>Hydrodynamic cavitation (HC) was adopted to assist alkaline-hydrogen peroxide pretreatment of sugarcane bagasse (SCB). In the following condition: 0.29 M of NaOH, 0.78% (v/v) of H2O2, 9.95 min of process time and 3 bar of inlet pressure, 95.4% of digestibility of cellulosic fraction was achieved. To take the best use of the pretreated biomass, the overall process was intensified by way of employing a packed bed flow-through column reactor and thus enabling to handle a high solid loading of 20%, thereby leading to cellulose and hemicellulose conversions to 74.7% and 75%, respectively. In the fermentation step, a bubble column reactor was introduced to maximize ethanol production from the pretreated SCB by Scheffersomyces stipitis NRRL-Y7124, resulting in 31.50 g/L of ethanol, 0.49 g/g of ethanol yield and 0.68 g/L.h of productivity. All this showed that our HC-assisted NaOH-H2O2 pretreatment strategy along with the process intensification approach might offer an option for SCB-based biorefineries.</Abstract> <Access xmlns="http://purl.org/coar/access_right" > </Access> </Publication> -1
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