Bioconversion of Sugarcane Bagasse into Value-Added Products by Bioaugmentation of Endogenous Cellulolytic and Fermentative Communities
Abstract The goals of this study were to describe a comprehensive taxonomic profile of bacterial communities endogenous from sugarcane bagasse (SCB) and from a thermophilic sludge formed mainly by Proteobacteria Actinobacteria and Firmicutes phylum and its potential as a bioaugmented inoculum for de...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Soares, Laís Américo [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2018 |
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| Schlagwörter: |
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| Anmerkung: |
© Springer Science+Business Media B.V., part of Springer Nature 2018 |
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| Übergeordnetes Werk: |
Enthalten in: Waste and biomass valorization - [Dordrecht] : Springer Netherlands, 2010, 10(2018), 7 vom: 05. Feb., Seite 1899-1912 |
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| Übergeordnetes Werk: |
volume:10 ; year:2018 ; number:7 ; day:05 ; month:02 ; pages:1899-1912 |
| Links: |
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| DOI / URN: |
10.1007/s12649-018-0201-5 |
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| Katalog-ID: |
SPR026576252 |
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| 100 | 1 | |a Soares, Laís Américo |e verfasserin |4 aut | |
| 245 | 1 | 0 | |a Bioconversion of Sugarcane Bagasse into Value-Added Products by Bioaugmentation of Endogenous Cellulolytic and Fermentative Communities |
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| 520 | |a Abstract The goals of this study were to describe a comprehensive taxonomic profile of bacterial communities endogenous from sugarcane bagasse (SCB) and from a thermophilic sludge formed mainly by Proteobacteria Actinobacteria and Firmicutes phylum and its potential as a bioaugmented inoculum for degradation of lignocellulosic biomass. Batch assays were performed using SCB as substrate at different condition: (RC) 2 g $ L^{−1} $ glucose, (R1i) 2 g $ L^{−1} $ unpretreated SCB, (R2i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min), (R3i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification (NaOH—1 M), (R4i) 1 g $ L^{−1} $ unpretreated SCB plus 1 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification. Hydrogen, methane and organic acids were the main metabolites produced during the fermentation. Maximum hydrogen (2.01 and 1.09 mol $ H_{2} $ $ mol^{−1} $ consumed soluble carbohydrates) were obtained in R1i and R2i, respectively. The highest organic acid (1051 mg $ L^{−1} $) and methane (0.92 mmo $ L^{−1} $) production were obtained in R4i. | ||
| 650 | 4 | |a Alkaline delignification |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Bioenergy |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Hydrothermal pretreatment |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Waste treatment |7 (dpeaa)DE-He213 | |
| 700 | 1 | |a Braga, Juliana Kawanish |4 aut | |
| 700 | 1 | |a Motteran, Fabrício |4 aut | |
| 700 | 1 | |a Sakamoto, Isabel Kimiko |4 aut | |
| 700 | 1 | |a Monteiro, Patrícia Aparecida Santiago |4 aut | |
| 700 | 1 | |a Seleghim, Paulo |4 aut | |
| 700 | 1 | |a Varesche, Maria Bernadete Amâncio |4 aut | |
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10.1007/s12649-018-0201-5 doi (DE-627)SPR026576252 (SPR)s12649-018-0201-5-e DE-627 ger DE-627 rakwb eng Soares, Laís Américo verfasserin aut Bioconversion of Sugarcane Bagasse into Value-Added Products by Bioaugmentation of Endogenous Cellulolytic and Fermentative Communities 2018 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer Science+Business Media B.V., part of Springer Nature 2018 Abstract The goals of this study were to describe a comprehensive taxonomic profile of bacterial communities endogenous from sugarcane bagasse (SCB) and from a thermophilic sludge formed mainly by Proteobacteria Actinobacteria and Firmicutes phylum and its potential as a bioaugmented inoculum for degradation of lignocellulosic biomass. Batch assays were performed using SCB as substrate at different condition: (RC) 2 g $ L^{−1} $ glucose, (R1i) 2 g $ L^{−1} $ unpretreated SCB, (R2i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min), (R3i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification (NaOH—1 M), (R4i) 1 g $ L^{−1} $ unpretreated SCB plus 1 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification. Hydrogen, methane and organic acids were the main metabolites produced during the fermentation. Maximum hydrogen (2.01 and 1.09 mol $ H_{2} $ $ mol^{−1} $ consumed soluble carbohydrates) were obtained in R1i and R2i, respectively. The highest organic acid (1051 mg $ L^{−1} $) and methane (0.92 mmo $ L^{−1} $) production were obtained in R4i. Alkaline delignification (dpeaa)DE-He213 Bioenergy (dpeaa)DE-He213 Hydrothermal pretreatment (dpeaa)DE-He213 Waste treatment (dpeaa)DE-He213 Braga, Juliana Kawanish aut Motteran, Fabrício aut Sakamoto, Isabel Kimiko aut Monteiro, Patrícia Aparecida Santiago aut Seleghim, Paulo aut Varesche, Maria Bernadete Amâncio aut Enthalten in Waste and biomass valorization [Dordrecht] : Springer Netherlands, 2010 10(2018), 7 vom: 05. Feb., Seite 1899-1912 (DE-627)620147245 (DE-600)2541900-6 1877-265X nnns volume:10 year:2018 number:7 day:05 month:02 pages:1899-1912 https://dx.doi.org/10.1007/s12649-018-0201-5 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 10 2018 7 05 02 1899-1912 |
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10.1007/s12649-018-0201-5 doi (DE-627)SPR026576252 (SPR)s12649-018-0201-5-e DE-627 ger DE-627 rakwb eng Soares, Laís Américo verfasserin aut Bioconversion of Sugarcane Bagasse into Value-Added Products by Bioaugmentation of Endogenous Cellulolytic and Fermentative Communities 2018 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer Science+Business Media B.V., part of Springer Nature 2018 Abstract The goals of this study were to describe a comprehensive taxonomic profile of bacterial communities endogenous from sugarcane bagasse (SCB) and from a thermophilic sludge formed mainly by Proteobacteria Actinobacteria and Firmicutes phylum and its potential as a bioaugmented inoculum for degradation of lignocellulosic biomass. Batch assays were performed using SCB as substrate at different condition: (RC) 2 g $ L^{−1} $ glucose, (R1i) 2 g $ L^{−1} $ unpretreated SCB, (R2i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min), (R3i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification (NaOH—1 M), (R4i) 1 g $ L^{−1} $ unpretreated SCB plus 1 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification. Hydrogen, methane and organic acids were the main metabolites produced during the fermentation. Maximum hydrogen (2.01 and 1.09 mol $ H_{2} $ $ mol^{−1} $ consumed soluble carbohydrates) were obtained in R1i and R2i, respectively. The highest organic acid (1051 mg $ L^{−1} $) and methane (0.92 mmo $ L^{−1} $) production were obtained in R4i. Alkaline delignification (dpeaa)DE-He213 Bioenergy (dpeaa)DE-He213 Hydrothermal pretreatment (dpeaa)DE-He213 Waste treatment (dpeaa)DE-He213 Braga, Juliana Kawanish aut Motteran, Fabrício aut Sakamoto, Isabel Kimiko aut Monteiro, Patrícia Aparecida Santiago aut Seleghim, Paulo aut Varesche, Maria Bernadete Amâncio aut Enthalten in Waste and biomass valorization [Dordrecht] : Springer Netherlands, 2010 10(2018), 7 vom: 05. Feb., Seite 1899-1912 (DE-627)620147245 (DE-600)2541900-6 1877-265X nnns volume:10 year:2018 number:7 day:05 month:02 pages:1899-1912 https://dx.doi.org/10.1007/s12649-018-0201-5 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 10 2018 7 05 02 1899-1912 |
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10.1007/s12649-018-0201-5 doi (DE-627)SPR026576252 (SPR)s12649-018-0201-5-e DE-627 ger DE-627 rakwb eng Soares, Laís Américo verfasserin aut Bioconversion of Sugarcane Bagasse into Value-Added Products by Bioaugmentation of Endogenous Cellulolytic and Fermentative Communities 2018 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer Science+Business Media B.V., part of Springer Nature 2018 Abstract The goals of this study were to describe a comprehensive taxonomic profile of bacterial communities endogenous from sugarcane bagasse (SCB) and from a thermophilic sludge formed mainly by Proteobacteria Actinobacteria and Firmicutes phylum and its potential as a bioaugmented inoculum for degradation of lignocellulosic biomass. Batch assays were performed using SCB as substrate at different condition: (RC) 2 g $ L^{−1} $ glucose, (R1i) 2 g $ L^{−1} $ unpretreated SCB, (R2i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min), (R3i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification (NaOH—1 M), (R4i) 1 g $ L^{−1} $ unpretreated SCB plus 1 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification. Hydrogen, methane and organic acids were the main metabolites produced during the fermentation. Maximum hydrogen (2.01 and 1.09 mol $ H_{2} $ $ mol^{−1} $ consumed soluble carbohydrates) were obtained in R1i and R2i, respectively. The highest organic acid (1051 mg $ L^{−1} $) and methane (0.92 mmo $ L^{−1} $) production were obtained in R4i. Alkaline delignification (dpeaa)DE-He213 Bioenergy (dpeaa)DE-He213 Hydrothermal pretreatment (dpeaa)DE-He213 Waste treatment (dpeaa)DE-He213 Braga, Juliana Kawanish aut Motteran, Fabrício aut Sakamoto, Isabel Kimiko aut Monteiro, Patrícia Aparecida Santiago aut Seleghim, Paulo aut Varesche, Maria Bernadete Amâncio aut Enthalten in Waste and biomass valorization [Dordrecht] : Springer Netherlands, 2010 10(2018), 7 vom: 05. Feb., Seite 1899-1912 (DE-627)620147245 (DE-600)2541900-6 1877-265X nnns volume:10 year:2018 number:7 day:05 month:02 pages:1899-1912 https://dx.doi.org/10.1007/s12649-018-0201-5 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 10 2018 7 05 02 1899-1912 |
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10.1007/s12649-018-0201-5 doi (DE-627)SPR026576252 (SPR)s12649-018-0201-5-e DE-627 ger DE-627 rakwb eng Soares, Laís Américo verfasserin aut Bioconversion of Sugarcane Bagasse into Value-Added Products by Bioaugmentation of Endogenous Cellulolytic and Fermentative Communities 2018 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer Science+Business Media B.V., part of Springer Nature 2018 Abstract The goals of this study were to describe a comprehensive taxonomic profile of bacterial communities endogenous from sugarcane bagasse (SCB) and from a thermophilic sludge formed mainly by Proteobacteria Actinobacteria and Firmicutes phylum and its potential as a bioaugmented inoculum for degradation of lignocellulosic biomass. Batch assays were performed using SCB as substrate at different condition: (RC) 2 g $ L^{−1} $ glucose, (R1i) 2 g $ L^{−1} $ unpretreated SCB, (R2i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min), (R3i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification (NaOH—1 M), (R4i) 1 g $ L^{−1} $ unpretreated SCB plus 1 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification. Hydrogen, methane and organic acids were the main metabolites produced during the fermentation. Maximum hydrogen (2.01 and 1.09 mol $ H_{2} $ $ mol^{−1} $ consumed soluble carbohydrates) were obtained in R1i and R2i, respectively. The highest organic acid (1051 mg $ L^{−1} $) and methane (0.92 mmo $ L^{−1} $) production were obtained in R4i. Alkaline delignification (dpeaa)DE-He213 Bioenergy (dpeaa)DE-He213 Hydrothermal pretreatment (dpeaa)DE-He213 Waste treatment (dpeaa)DE-He213 Braga, Juliana Kawanish aut Motteran, Fabrício aut Sakamoto, Isabel Kimiko aut Monteiro, Patrícia Aparecida Santiago aut Seleghim, Paulo aut Varesche, Maria Bernadete Amâncio aut Enthalten in Waste and biomass valorization [Dordrecht] : Springer Netherlands, 2010 10(2018), 7 vom: 05. Feb., Seite 1899-1912 (DE-627)620147245 (DE-600)2541900-6 1877-265X nnns volume:10 year:2018 number:7 day:05 month:02 pages:1899-1912 https://dx.doi.org/10.1007/s12649-018-0201-5 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 10 2018 7 05 02 1899-1912 |
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10.1007/s12649-018-0201-5 doi (DE-627)SPR026576252 (SPR)s12649-018-0201-5-e DE-627 ger DE-627 rakwb eng Soares, Laís Américo verfasserin aut Bioconversion of Sugarcane Bagasse into Value-Added Products by Bioaugmentation of Endogenous Cellulolytic and Fermentative Communities 2018 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Springer Science+Business Media B.V., part of Springer Nature 2018 Abstract The goals of this study were to describe a comprehensive taxonomic profile of bacterial communities endogenous from sugarcane bagasse (SCB) and from a thermophilic sludge formed mainly by Proteobacteria Actinobacteria and Firmicutes phylum and its potential as a bioaugmented inoculum for degradation of lignocellulosic biomass. Batch assays were performed using SCB as substrate at different condition: (RC) 2 g $ L^{−1} $ glucose, (R1i) 2 g $ L^{−1} $ unpretreated SCB, (R2i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min), (R3i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification (NaOH—1 M), (R4i) 1 g $ L^{−1} $ unpretreated SCB plus 1 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification. Hydrogen, methane and organic acids were the main metabolites produced during the fermentation. Maximum hydrogen (2.01 and 1.09 mol $ H_{2} $ $ mol^{−1} $ consumed soluble carbohydrates) were obtained in R1i and R2i, respectively. The highest organic acid (1051 mg $ L^{−1} $) and methane (0.92 mmo $ L^{−1} $) production were obtained in R4i. Alkaline delignification (dpeaa)DE-He213 Bioenergy (dpeaa)DE-He213 Hydrothermal pretreatment (dpeaa)DE-He213 Waste treatment (dpeaa)DE-He213 Braga, Juliana Kawanish aut Motteran, Fabrício aut Sakamoto, Isabel Kimiko aut Monteiro, Patrícia Aparecida Santiago aut Seleghim, Paulo aut Varesche, Maria Bernadete Amâncio aut Enthalten in Waste and biomass valorization [Dordrecht] : Springer Netherlands, 2010 10(2018), 7 vom: 05. Feb., Seite 1899-1912 (DE-627)620147245 (DE-600)2541900-6 1877-265X nnns volume:10 year:2018 number:7 day:05 month:02 pages:1899-1912 https://dx.doi.org/10.1007/s12649-018-0201-5 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 10 2018 7 05 02 1899-1912 |
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Enthalten in Waste and biomass valorization 10(2018), 7 vom: 05. Feb., Seite 1899-1912 volume:10 year:2018 number:7 day:05 month:02 pages:1899-1912 |
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Enthalten in Waste and biomass valorization 10(2018), 7 vom: 05. Feb., Seite 1899-1912 volume:10 year:2018 number:7 day:05 month:02 pages:1899-1912 |
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Alkaline delignification Bioenergy Hydrothermal pretreatment Waste treatment |
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Waste and biomass valorization |
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Soares, Laís Américo @@aut@@ Braga, Juliana Kawanish @@aut@@ Motteran, Fabrício @@aut@@ Sakamoto, Isabel Kimiko @@aut@@ Monteiro, Patrícia Aparecida Santiago @@aut@@ Seleghim, Paulo @@aut@@ Varesche, Maria Bernadete Amâncio @@aut@@ |
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Soares, Laís Américo |
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Soares, Laís Américo misc Alkaline delignification misc Bioenergy misc Hydrothermal pretreatment misc Waste treatment Bioconversion of Sugarcane Bagasse into Value-Added Products by Bioaugmentation of Endogenous Cellulolytic and Fermentative Communities |
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Bioconversion of Sugarcane Bagasse into Value-Added Products by Bioaugmentation of Endogenous Cellulolytic and Fermentative Communities Alkaline delignification (dpeaa)DE-He213 Bioenergy (dpeaa)DE-He213 Hydrothermal pretreatment (dpeaa)DE-He213 Waste treatment (dpeaa)DE-He213 |
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Bioconversion of Sugarcane Bagasse into Value-Added Products by Bioaugmentation of Endogenous Cellulolytic and Fermentative Communities |
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Bioconversion of Sugarcane Bagasse into Value-Added Products by Bioaugmentation of Endogenous Cellulolytic and Fermentative Communities |
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Soares, Laís Américo Braga, Juliana Kawanish Motteran, Fabrício Sakamoto, Isabel Kimiko Monteiro, Patrícia Aparecida Santiago Seleghim, Paulo Varesche, Maria Bernadete Amâncio |
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bioconversion of sugarcane bagasse into value-added products by bioaugmentation of endogenous cellulolytic and fermentative communities |
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Bioconversion of Sugarcane Bagasse into Value-Added Products by Bioaugmentation of Endogenous Cellulolytic and Fermentative Communities |
| abstract |
Abstract The goals of this study were to describe a comprehensive taxonomic profile of bacterial communities endogenous from sugarcane bagasse (SCB) and from a thermophilic sludge formed mainly by Proteobacteria Actinobacteria and Firmicutes phylum and its potential as a bioaugmented inoculum for degradation of lignocellulosic biomass. Batch assays were performed using SCB as substrate at different condition: (RC) 2 g $ L^{−1} $ glucose, (R1i) 2 g $ L^{−1} $ unpretreated SCB, (R2i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min), (R3i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification (NaOH—1 M), (R4i) 1 g $ L^{−1} $ unpretreated SCB plus 1 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification. Hydrogen, methane and organic acids were the main metabolites produced during the fermentation. Maximum hydrogen (2.01 and 1.09 mol $ H_{2} $ $ mol^{−1} $ consumed soluble carbohydrates) were obtained in R1i and R2i, respectively. The highest organic acid (1051 mg $ L^{−1} $) and methane (0.92 mmo $ L^{−1} $) production were obtained in R4i. © Springer Science+Business Media B.V., part of Springer Nature 2018 |
| abstractGer |
Abstract The goals of this study were to describe a comprehensive taxonomic profile of bacterial communities endogenous from sugarcane bagasse (SCB) and from a thermophilic sludge formed mainly by Proteobacteria Actinobacteria and Firmicutes phylum and its potential as a bioaugmented inoculum for degradation of lignocellulosic biomass. Batch assays were performed using SCB as substrate at different condition: (RC) 2 g $ L^{−1} $ glucose, (R1i) 2 g $ L^{−1} $ unpretreated SCB, (R2i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min), (R3i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification (NaOH—1 M), (R4i) 1 g $ L^{−1} $ unpretreated SCB plus 1 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification. Hydrogen, methane and organic acids were the main metabolites produced during the fermentation. Maximum hydrogen (2.01 and 1.09 mol $ H_{2} $ $ mol^{−1} $ consumed soluble carbohydrates) were obtained in R1i and R2i, respectively. The highest organic acid (1051 mg $ L^{−1} $) and methane (0.92 mmo $ L^{−1} $) production were obtained in R4i. © Springer Science+Business Media B.V., part of Springer Nature 2018 |
| abstract_unstemmed |
Abstract The goals of this study were to describe a comprehensive taxonomic profile of bacterial communities endogenous from sugarcane bagasse (SCB) and from a thermophilic sludge formed mainly by Proteobacteria Actinobacteria and Firmicutes phylum and its potential as a bioaugmented inoculum for degradation of lignocellulosic biomass. Batch assays were performed using SCB as substrate at different condition: (RC) 2 g $ L^{−1} $ glucose, (R1i) 2 g $ L^{−1} $ unpretreated SCB, (R2i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min), (R3i) 2 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification (NaOH—1 M), (R4i) 1 g $ L^{−1} $ unpretreated SCB plus 1 g $ L^{−1} $ hydrothermally pretreated SCB (at 210 °C for 15 min) followed by alkaline delignification. Hydrogen, methane and organic acids were the main metabolites produced during the fermentation. Maximum hydrogen (2.01 and 1.09 mol $ H_{2} $ $ mol^{−1} $ consumed soluble carbohydrates) were obtained in R1i and R2i, respectively. The highest organic acid (1051 mg $ L^{−1} $) and methane (0.92 mmo $ L^{−1} $) production were obtained in R4i. © Springer Science+Business Media B.V., part of Springer Nature 2018 |
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| container_issue |
7 |
| title_short |
Bioconversion of Sugarcane Bagasse into Value-Added Products by Bioaugmentation of Endogenous Cellulolytic and Fermentative Communities |
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https://dx.doi.org/10.1007/s12649-018-0201-5 |
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| author2 |
Braga, Juliana Kawanish Motteran, Fabrício Sakamoto, Isabel Kimiko Monteiro, Patrícia Aparecida Santiago Seleghim, Paulo Varesche, Maria Bernadete Amâncio |
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Braga, Juliana Kawanish Motteran, Fabrício Sakamoto, Isabel Kimiko Monteiro, Patrícia Aparecida Santiago Seleghim, Paulo Varesche, Maria Bernadete Amâncio |
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| doi_str |
10.1007/s12649-018-0201-5 |
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2024-07-03T21:37:52.848Z |
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| score |
7.4003086 |