Second-generation ethanol process for integral use of hemicellulosic and cellulosic hydrolysates from diluted sulfuric acid pretreatment of sugarcane bagasse

dc.contributor.authorDionísio, S. R.
dc.contributor.authorSantoro, D. C.J.
dc.contributor.authorBonan, C. I.D.G.
dc.contributor.authorSoares, L. B.
dc.contributor.authorBiazi, L. E.
dc.contributor.authorRabelo, S. C. [UNESP]
dc.contributor.authorIenczak, J. L.
dc.contributor.institutionBrazilian Biorenewables National Laboratory - LNBR/CNPEM
dc.contributor.institutionUniversidade Estadual de Campinas (UNICAMP)
dc.contributor.institutionUniversidade Federal de Santa Catarina (UFSC)
dc.contributor.institutionUniversidade Estadual Paulista (UNESP)
dc.date.accessioned2022-04-28T19:41:33Z
dc.date.available2022-04-28T19:41:33Z
dc.date.issued2021-11-15
dc.description.abstractIn this work, a strategy to promote ethanol fermentation through the complete utilization of fermentable sugars released from sugarcane bagasse was proposed. Initially, the sugarcane bagasse was subjected to a diluted sulfuric acid pretreatment, leading to 89.5% of hemicellulose solubilization, in which 82% was recovered as monomeric sugars (xylose and arabinose) in the liquid stream. The cellulignin obtained was subjected to enzymatic hydrolysis, resulting in 51.2 and 95.08% of cellulose and hemicellulose yields, respectively. The C5-rich hemicellulosic hydrolysate was fermented to ethanol by the pentose-fermenting yeast Spathaspora passalidarum NRRL Y-27907, achieving an ethanol yield of 86.11%. The C6-rich enzymatic hydrolysate, on the other hand, was fermented by Saccharomyces cerevisiae CAT-1 through the application of a cell-recycle batch fermentation system. This strategy improved the overall fermentation performance throughout the cycles, with a substantial increase in the ethanol productivity of 361% from the first to the last batch. Based on a mass balance with input of 1000 kg of sugarcane bagasse and taking into account a complete pentose and hexose fermentation, 191.96 kg of ethanol could be produced from this integrated platform, which corresponded to 243.3 L of ethanol.en
dc.description.affiliationBrazilian Biorenewables National Laboratory - LNBR/CNPEM, 10000 Giuseppe Máximo Scolfaro St
dc.description.affiliationSchool of Chemical Engineering State University of Campinas - UNICAMP, 500 Albert Einstein Av
dc.description.affiliationChemical Engineering and Food Engineering Department Santa Catarina Federal University – UFSC
dc.description.affiliationDepartment of Bioprocess and Biotechnology College of Agricultural Sciences São Paulo State University (UNESP), Botucatu
dc.description.affiliationUnespDepartment of Bioprocess and Biotechnology College of Agricultural Sciences São Paulo State University (UNESP), Botucatu
dc.identifierhttp://dx.doi.org/10.1016/j.fuel.2021.121290
dc.identifier.citationFuel, v. 304.
dc.identifier.doi10.1016/j.fuel.2021.121290
dc.identifier.issn0016-2361
dc.identifier.scopus2-s2.0-85110158460
dc.identifier.urihttp://hdl.handle.net/11449/221958
dc.language.isoeng
dc.relation.ispartofFuel
dc.sourceScopus
dc.subjectC5+C6 separated fermentation
dc.subjectCell recycle
dc.subjectDiluted acid pretreatment
dc.subjectSugarcane bagasse
dc.titleSecond-generation ethanol process for integral use of hemicellulosic and cellulosic hydrolysates from diluted sulfuric acid pretreatment of sugarcane bagasseen
dc.typeArtigo
unesp.author.orcid0000-0003-4087-8339[7]

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