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

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dc.contributor.authorHilares, Ruly Teranko
dc.contributor.authorKamoei, Douglas Vianako
dc.contributor.authorAhmed, Muhammad Ajazko
dc.contributor.authorda Silva, Silvio Silverioko
dc.contributor.authorHan, Jong-Inko
dc.contributor.authordos Santos, Julio Cesarko
dc.date.accessioned2018-05-24T01:32:28Z-
dc.date.available2018-05-24T01:32:28Z-
dc.date.created2018-04-30-
dc.date.created2018-04-30-
dc.date.created2018-04-30-
dc.date.issued2018-05-
dc.identifier.citationULTRASONICS SONOCHEMISTRY, v.43, pp.219 - 226-
dc.identifier.issn1350-4177-
dc.identifier.urihttp://hdl.handle.net/10203/242178-
dc.description.abstractHydrodynamic 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.-
dc.languageEnglish-
dc.publisherELSEVIER SCIENCE BV-
dc.titleA new approach for bioethanol production from sugarcane bagasse using hydrodynamic cavitation assisted-pretreatment and column reactors-
dc.typeArticle-
dc.identifier.wosid000429511800025-
dc.identifier.scopusid2-s2.0-85041483520-
dc.type.rimsART-
dc.citation.volume43-
dc.citation.beginningpage219-
dc.citation.endingpage226-
dc.citation.publicationnameULTRASONICS SONOCHEMISTRY-
dc.identifier.doi10.1016/j.ultsonch.2018.01.016-
dc.contributor.localauthorHan, Jong-In-
dc.contributor.nonIdAuthorHilares, Ruly Teran-
dc.contributor.nonIdAuthorKamoei, Douglas Viana-
dc.contributor.nonIdAuthorda Silva, Silvio Silverio-
dc.contributor.nonIdAuthordos Santos, Julio Cesar-
dc.description.isOpenAccessN-
dc.type.journalArticleArticle-
dc.subject.keywordAuthorHydrodynamic cavitation-
dc.subject.keywordAuthorProcess intensification-
dc.subject.keywordAuthorHydrogen peroxide-
dc.subject.keywordAuthorAlkaline pretreatment-
dc.subject.keywordAuthorSugarcane bagasse-
dc.subject.keywordAuthorEthanol production-
dc.subject.keywordPlusHYDROGEN-PEROXIDE PRETREATMENT-
dc.subject.keywordPlusHIGH-SOLIDS LOADINGS-
dc.subject.keywordPlusALKALINE PRETREATMENT-
dc.subject.keywordPlusENZYMATIC-HYDROLYSIS-
dc.subject.keywordPlusLIGNOCELLULOSIC BIOMASS-
dc.subject.keywordPlusEFFICIENT PRETREATMENT-
dc.subject.keywordPlusETHANOL-PRODUCTION-
dc.subject.keywordPlusNMR-SPECTROSCOPY-
dc.subject.keywordPlusPICHIA-STIPITIS-
dc.subject.keywordPlusFLOW-THROUGH-
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