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2. |  | BRONDI, M. G.; ELIAS, A. M.; FURLAN, F. F.; GIORDANO, R. C.; FARINAS, C. S. Uso da proteína de soja na sacarificação do bagaço de cana-de-açúcar no contexto de uma biorrefinaria integrada: análise tecno-econômica do processo. In: SIMPÓSIO NACIONAL DE INSTRUMENTAÇÃO AGROPECUÁRIA, 4., 2019, São Carlos, SP. Ciência, inovação e mercado: anais. São Carlos, SP: Embrapa Instrumentação, 2019. Editores: Paulino Ribeiro Villas-Boas, Maria Alice Martins, Débora Marcondes Bastos Pereira Milori, Ladislau Martin Neto. SIAGRO 2019. 280-283 Biblioteca(s): Embrapa Instrumentação. |
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Registros recuperados : 3 | |
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Registro Completo
Biblioteca(s): |
Embrapa Instrumentação. |
Data corrente: |
23/06/2021 |
Data da última atualização: |
10/06/2022 |
Tipo da produção científica: |
Artigo em Periódico Indexado |
Circulação/Nível: |
A - 1 |
Autoria: |
PINTO, A. S. S.; BRONDI, M. G.; FREITAS, J. V. de; FURLAN, F. F.; RIBEIRO, M. P. A.; GIORDANO, R. C.; FARINAS, C. S. |
Afiliação: |
CRISTIANE SANCHEZ FARINAS, CNPDIA. |
Título: |
Mitigating the negative impact of soluble and insoluble lignin in biorefineries. |
Ano de publicação: |
2021 |
Fonte/Imprenta: |
Renewable Energy, v. 173, 2021. |
Páginas: |
1017-1026 |
ISSN: |
0960-1481 |
DOI: |
https://doi.org/10.1016/j.renene.2021.03.137 |
Idioma: |
Inglês |
Conteúdo: |
The presence of inhibitors is still an economic bottleneck that needs to be resolved in order to make the biorefineries feasible, requiring the development of technologies capable of improving their competitiveness in the biofuel marketplace. Soluble and insoluble lignin can impair the enzymatic hydrolysis process by inhibition, deactivation, and unproductive adsorption of enzymes. Washing the pretreated biomass or using lignin-blocking additives during saccharification could mitigate these negative effects in future biorefineries. Here, an investigation was performed of the combined mitigation processes, in terms of their technical and economic feasibility in an integrated first and second generation (1G2G) sugarcane biorefinery. Evaluation was made of the impacts of biomass washing and soybean protein addition, separately or in combination, on glucose yields for enzymatic hydrolysis in the presence of high (liquor) and low (buffer) concentrations of soluble inhibitors/deactivators. Combining washing and soybean protein addition provided the highest glucose yields, with an increase of up to 50%. The effect of the mitigation processes could be explained by a combination of catalytic mechanisms acting on both soluble and insoluble lignin. In an industrial context, biomass washing (90 C, 15% (w/w) solids, 3 steps) followed by soybean protein addition (12% (w/v) solids) provided a cost-competitive methodology for bioethanol production, with an estimated net present value of US$ 9.16 107 , optimizing hydrolysis process in the 1G2G sugarcane biorefinery. MenosThe presence of inhibitors is still an economic bottleneck that needs to be resolved in order to make the biorefineries feasible, requiring the development of technologies capable of improving their competitiveness in the biofuel marketplace. Soluble and insoluble lignin can impair the enzymatic hydrolysis process by inhibition, deactivation, and unproductive adsorption of enzymes. Washing the pretreated biomass or using lignin-blocking additives during saccharification could mitigate these negative effects in future biorefineries. Here, an investigation was performed of the combined mitigation processes, in terms of their technical and economic feasibility in an integrated first and second generation (1G2G) sugarcane biorefinery. Evaluation was made of the impacts of biomass washing and soybean protein addition, separately or in combination, on glucose yields for enzymatic hydrolysis in the presence of high (liquor) and low (buffer) concentrations of soluble inhibitors/deactivators. Combining washing and soybean protein addition provided the highest glucose yields, with an increase of up to 50%. The effect of the mitigation processes could be explained by a combination of catalytic mechanisms acting on both soluble and insoluble lignin. In an industrial context, biomass washing (90 C, 15% (w/w) solids, 3 steps) followed by soybean protein addition (12% (w/v) solids) provided a cost-competitive methodology for bioethanol production, with an estimated net present value of US$... Mostrar Tudo |
Palavras-Chave: |
1G2G ethanol; Pretreatment byproducts; Soybean protein addition; Techno-economic assessment; Washing process. |
Categoria do assunto: |
-- |
Marc: |
LEADER 02429naa a2200289 a 4500 001 2132515 005 2022-06-10 008 2021 bl uuuu u00u1 u #d 022 $a0960-1481 024 7 $ahttps://doi.org/10.1016/j.renene.2021.03.137$2DOI 100 1 $aPINTO, A. S. S. 245 $aMitigating the negative impact of soluble and insoluble lignin in biorefineries.$h[electronic resource] 260 $c2021 300 $a1017-1026 520 $aThe presence of inhibitors is still an economic bottleneck that needs to be resolved in order to make the biorefineries feasible, requiring the development of technologies capable of improving their competitiveness in the biofuel marketplace. Soluble and insoluble lignin can impair the enzymatic hydrolysis process by inhibition, deactivation, and unproductive adsorption of enzymes. Washing the pretreated biomass or using lignin-blocking additives during saccharification could mitigate these negative effects in future biorefineries. Here, an investigation was performed of the combined mitigation processes, in terms of their technical and economic feasibility in an integrated first and second generation (1G2G) sugarcane biorefinery. Evaluation was made of the impacts of biomass washing and soybean protein addition, separately or in combination, on glucose yields for enzymatic hydrolysis in the presence of high (liquor) and low (buffer) concentrations of soluble inhibitors/deactivators. Combining washing and soybean protein addition provided the highest glucose yields, with an increase of up to 50%. The effect of the mitigation processes could be explained by a combination of catalytic mechanisms acting on both soluble and insoluble lignin. In an industrial context, biomass washing (90 C, 15% (w/w) solids, 3 steps) followed by soybean protein addition (12% (w/v) solids) provided a cost-competitive methodology for bioethanol production, with an estimated net present value of US$ 9.16 107 , optimizing hydrolysis process in the 1G2G sugarcane biorefinery. 653 $a1G2G ethanol 653 $aPretreatment byproducts 653 $aSoybean protein addition 653 $aTechno-economic assessment 653 $aWashing process 700 1 $aBRONDI, M. G. 700 1 $aFREITAS, J. V. de 700 1 $aFURLAN, F. F. 700 1 $aRIBEIRO, M. P. A. 700 1 $aGIORDANO, R. C. 700 1 $aFARINAS, C. S. 773 $tRenewable Energy$gv. 173, 2021.
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