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Fractionation of sugarcane bagasse using hydrothermal and advanced oxidative pretreatments for bioethanol and biogas production in lignocellulose biorefineries.
Bittencourt, Gustavo Amaro; Barreto, Elisa da Silva; Brandão, Rogélio Lopes; Baêta, Bruno Eduardo Lobo; Gurgel, Leandro Vinícius Alves.
Affiliation
  • Bittencourt GA; Laboratory of Technological and Environmental Chemistry, Department of Chemistry, Institute of Exact and Biological Sciences (ICEB), Federal University of Ouro Preto, Campus Universitário Morro do Cruzeiro, Bauxita, Ouro Preto 35400-000, Minas Gerais, Brazil.
  • Barreto EDS; Department of Biochemistry and Molecular Biology, Institute of Applied Biotechnology to Agriculture (BIOAGRO), Federal University of Viçosa, Viçosa 36570-000, Minas Gerais, Brazil.
  • Brandão RL; Laboratory of Cellular and Molecular Biology, Nucleus of Research in Biological Sciences (NUPEB), School of Pharmacy, Federal University of Ouro Preto, Campus Universitário Morro do Cruzeiro, Bauxita Ouro Preto 35400-000, Minas Gerais, Brazil.
  • Baêta BEL; Laboratory of Technological and Environmental Chemistry, Department of Chemistry, Institute of Exact and Biological Sciences (ICEB), Federal University of Ouro Preto, Campus Universitário Morro do Cruzeiro, Bauxita, Ouro Preto 35400-000, Minas Gerais, Brazil.
  • Gurgel LVA; Laboratory of Technological and Environmental Chemistry, Department of Chemistry, Institute of Exact and Biological Sciences (ICEB), Federal University of Ouro Preto, Campus Universitário Morro do Cruzeiro, Bauxita, Ouro Preto 35400-000, Minas Gerais, Brazil. Electronic address: legurgel@ufop.edu.br
Bioresour Technol ; 292: 121963, 2019 Nov.
Article in En | MEDLINE | ID: mdl-31442832
The fractionation of sugarcane bagasse (SB) by hydrothermal pretreatment (HP, autohydrolysis) followed by alkaline extraction (AE) and advanced oxidative pretreatment (AOP) for production of second-generation ethanol and biogas was investigated. The AOP of SB was optimized using a Doehlert design, varying the applied H2O2 load, liquid-to-solid ratio (LSR), and time. The responses evaluated were yield (Y), residual cellulose (RC), delignification (DE), and enzymatic conversion (EC). The AE of SB pretreated by HP led to 61.8% DE (using 0.2 mol L-1 NaOH). This high lignin removal enabled substantial savings of H2O2 in the AOP. The optimized AOP conditions led to 78% Y, 82.2% RC, 42.7% DE, and 88.9% EC (overall glucose yield of 60.9%). Fermentation of the enzymatic hydrolysate with Saccharomyces cerevisiae yielded 190.8 Lethanol tonSB-1. Biogas production by anaerobic digestion of residual liquid streams of the pretreatment steps yielded 27.46 NLCH4 kgSB-1. An energy balance was estimated for the SB fractionation.
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Full text: 1 Collection: 01-internacional Database: MEDLINE Main subject: Saccharum Language: En Journal: Bioresour Technol Journal subject: ENGENHARIA BIOMEDICA Year: 2019 Document type: Article Affiliation country: Brazil Country of publication: United kingdom

Full text: 1 Collection: 01-internacional Database: MEDLINE Main subject: Saccharum Language: En Journal: Bioresour Technol Journal subject: ENGENHARIA BIOMEDICA Year: 2019 Document type: Article Affiliation country: Brazil Country of publication: United kingdom