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Successive pretreatment and enzymatic saccharification of sugarcane bagasse in a packed bed flow-through column reactor aiming to support biorefineries
Successive pretreatment and enzymatic saccharification of sugarcane bagasse in a packed bed flow-through column reactor aiming to support biorefineries
dc.contributor.author | Terán-Hilares R. | es_PE |
dc.contributor.author | Reséndiz A.L. | es_PE |
dc.contributor.author | Martínez R.T. | es_PE |
dc.contributor.author | Silva S.S. | es_PE |
dc.contributor.author | Santos J.C. | es_PE |
dc.date.accessioned | 2024-05-30T23:13:38Z | |
dc.date.available | 2024-05-30T23:13:38Z | |
dc.date.issued | 2016 | |
dc.description | The authors gratefully acknowledge the Consejo Nacional de Ciencia, Tecnología e Innovación Tecnológica (CONCyTEC-Perú, process number 219-2014) and Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq-Brazil, process number 449609/2014-6) for financial support. | |
dc.description.abstract | A packed bed flow-through column reactor (PBFTCR) was used for pretreatment and subsequent enzymatic hydrolysis of sugarcane bagasse (SCB). Alkaline pretreatment was performed at 70 °C for 4 h with fresh 0.3 M NaOH solution or with liquor recycled from a previous pretreatment batch. Scheffersomyces stipitis NRRL-Y7124 was used for fermentation of sugars released after enzymatic hydrolysis (20 FPU g−1 of dry SCB). The highest results for lignin removal were 61% and 52%, respectively, observed when using fresh NaOH or the first reuse of the liquor. About 50% of cellulosic and 57% of hemicellulosic fractions of pretreated SCBs were enzymatically hydrolyzed and the maximum ethanol production was 23.4 g L−1 (ethanol yield of 0.4 gp gs−1), with near complete consumption of both pentoses and hexoses present in the hydrolysate during the fermentation. PBFTCR as a new alternative for SCB-biorefineries is presented, mainly considering its simple configuration and efficiency for operating with a high solid:liquid ratio. | |
dc.description.sponsorship | Consejo Nacional de Ciencia, Tecnología e Innovación Tecnológica - Concytec | |
dc.identifier.doi | https://doi.org/10.1016/j.biortech.2015.12.026 | |
dc.identifier.scopus | 2-s2.0-84952006686 | |
dc.identifier.uri | https://hdl.handle.net/20.500.12390/786 | |
dc.language.iso | eng | |
dc.publisher | Elsevier Ltd | |
dc.relation.ispartof | Bioresource Technology | |
dc.rights | info:eu-repo/semantics/openAccess | |
dc.subject | xylose | |
dc.subject | Bagasse | es_PE |
dc.subject | Bioethanol | es_PE |
dc.subject | Ethanol | es_PE |
dc.subject | Fermentation | es_PE |
dc.subject | Hydrolysis | es_PE |
dc.subject | Packed beds | es_PE |
dc.subject | Refining | es_PE |
dc.subject | Saccharification | es_PE |
dc.subject | Bio-ethanol production | es_PE |
dc.subject | Enzymatic saccharification | es_PE |
dc.subject | Packed bed reactor | es_PE |
dc.subject | Reuse of alkaline liquor | es_PE |
dc.subject | Sugar-cane bagasse | es_PE |
dc.subject | Enzymatic hydrolysis | es_PE |
dc.subject | alcohol | es_PE |
dc.subject | bagasse | es_PE |
dc.subject | cellobiose | es_PE |
dc.subject | cellulose | es_PE |
dc.subject | glucose | es_PE |
dc.subject | hemicellulose | es_PE |
dc.subject | hexose | es_PE |
dc.subject | ionic liquid | es_PE |
dc.subject | lignin | es_PE |
dc.subject | pentose | es_PE |
dc.subject | alcohol | es_PE |
dc.subject | bagasse | es_PE |
dc.subject | biofuel | es_PE |
dc.subject | bioreactor | es_PE |
dc.subject | cellulose | es_PE |
dc.subject | enzyme activity | es_PE |
dc.subject | ethanol | es_PE |
dc.subject | fermentation | es_PE |
dc.subject | hydrolysis | es_PE |
dc.subject | lignin | es_PE |
dc.subject | sugar cane | es_PE |
dc.subject | temperature effect | es_PE |
dc.subject | alcohol production | es_PE |
dc.subject | alkalinity | es_PE |
dc.subject | Article | es_PE |
dc.subject | biomass | es_PE |
dc.subject | cell growth | es_PE |
dc.subject | enzyme activity | es_PE |
dc.subject | fermentation | es_PE |
dc.subject | hydrolysis | es_PE |
dc.subject | infrared spectroscopy | es_PE |
dc.subject | liquid | es_PE |
dc.subject | nonhuman | es_PE |
dc.subject | packed bed flow through column reactor | es_PE |
dc.subject | priority journal | es_PE |
dc.subject | reactor | es_PE |
dc.subject | saccharification | es_PE |
dc.subject | scanning electron microscopy | es_PE |
dc.subject | Scheffersomyces stipitis | es_PE |
dc.subject | sugar intake | es_PE |
dc.subject | sugarcane | es_PE |
dc.subject | water content | es_PE |
dc.subject | X ray diffraction | es_PE |
dc.subject | budding yeast | es_PE |
dc.subject | evaluation study | es_PE |
dc.subject | fermentation | es_PE |
dc.subject | metabolism | es_PE |
dc.subject | sugarcane | es_PE |
dc.subject | ultrastructure | es_PE |
dc.subject | Biofuels | es_PE |
dc.subject | Cellulose | es_PE |
dc.subject | Ethanol | es_PE |
dc.subject | Fermentation | es_PE |
dc.subject | Hydrolysis | es_PE |
dc.subject | Lignin | es_PE |
dc.subject | Saccharomycetales | es_PE |
dc.subject | Saccharum | es_PE |
dc.subject.ocde | https://purl.org/pe-repo/ocde/ford#2.08.01 | |
dc.title | Successive pretreatment and enzymatic saccharification of sugarcane bagasse in a packed bed flow-through column reactor aiming to support biorefineries | |
dc.type | info:eu-repo/semantics/article | |
dspace.entity.type | Publication | |
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oairecerif.author.affiliation | #PLACEHOLDER_PARENT_METADATA_VALUE# | |
oairecerif.author.affiliation | #PLACEHOLDER_PARENT_METADATA_VALUE# | |
oairecerif.author.affiliation | #PLACEHOLDER_PARENT_METADATA_VALUE# | |
oairecerif.author.affiliation | #PLACEHOLDER_PARENT_METADATA_VALUE# |