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Sugarcane bagasse pretreatment using three imidazolium-based ionic liquids; mass balances and enzyme kinetics

BACKGROUND: Effective pretreatment is key to achieving high enzymatic saccharification efficiency in processing lignocellulosic biomass to fermentable sugars, biofuels and value-added products. Ionic liquids (ILs), still relatively new class of solvents, are attractive for biomass pretreatment becau...

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Autores principales: Karatzos, Sergios Kimon, Edye, Leslie Alan, Doherty, William Orlando Sinclair
Formato: Online Artículo Texto
Lenguaje:English
Publicado: BioMed Central 2012
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC3495841/
https://www.ncbi.nlm.nih.gov/pubmed/22920045
http://dx.doi.org/10.1186/1754-6834-5-62
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author Karatzos, Sergios Kimon
Edye, Leslie Alan
Doherty, William Orlando Sinclair
author_facet Karatzos, Sergios Kimon
Edye, Leslie Alan
Doherty, William Orlando Sinclair
author_sort Karatzos, Sergios Kimon
collection PubMed
description BACKGROUND: Effective pretreatment is key to achieving high enzymatic saccharification efficiency in processing lignocellulosic biomass to fermentable sugars, biofuels and value-added products. Ionic liquids (ILs), still relatively new class of solvents, are attractive for biomass pretreatment because some demonstrate the rare ability to dissolve all components of lignocellulosic biomass including highly ordered (crystalline) cellulose. In the present study, three ILs, 1-butyl-3-methylimidazolium chloride ([C4mim]Cl), 1-ethyl-3-methylimidazolium chloride ([C2mim]Cl), 1-ethyl-3-methylimidazolium acetate ([C2mim]OAc) are used to dissolve/pretreat and fractionate sugarcane bagasse. In these IL-based pretreatments the biomass is completely or partially dissolved in ILs at temperatures greater than 130°C and then precipitated by the addition of an antisolvent to the IL biomass mixture. For the first time mass balances of IL-based pretreatments are reported. Such mass balances, along with kinetics data, can be used in process modelling and design. RESULTS: Lignin removals of 10% mass of lignin in bagasse with [C4mim]Cl, 50% mass with [C2mim]Cl and 60% mass with [C2mim]OAc, are achieved by limiting the amount of water added as antisolvent to 0.5 water:IL mass ratio thus minimising lignin precipitation. Enzyme saccharification (24 h, 15FPU) yields (% cellulose mass in starting bagasse) from the recovered solids rank as: [C2mim]OAc(83%) > >[C2mim]Cl(53%) = [C4mim]Cl(53%). Composition of [C2mim]OAc-treated solids such as low lignin, low acetyl group content and preservation of arabinosyl groups are characteristic of aqueous alkali pretreatments while those of chloride IL-treated solids resemble aqueous acid pretreatments. All ILs are fully recovered after use (100% mass as determined by ion chromatography). CONCLUSIONS: In all three ILs regulated addition of water as an antisolvent effected a polysaccharide enriched precipitate since some of the lignin remained dissolved in the aqueous IL solution. Of the three IL studied [C2mim]OAc gave the best saccharification yield, material recovery and delignification. The effects of [C2mim]OAc pretreatment resemble those of aqueous alkali pretreatments while those of [C2mim]Cl and [C4mim]Cl resemble aqueous acid pretreatments. The use of imidazolium IL solvents with shorter alkyl chains results in accelerated dissolution, pretreatment and degradation.
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spelling pubmed-34958412012-11-13 Sugarcane bagasse pretreatment using three imidazolium-based ionic liquids; mass balances and enzyme kinetics Karatzos, Sergios Kimon Edye, Leslie Alan Doherty, William Orlando Sinclair Biotechnol Biofuels Research BACKGROUND: Effective pretreatment is key to achieving high enzymatic saccharification efficiency in processing lignocellulosic biomass to fermentable sugars, biofuels and value-added products. Ionic liquids (ILs), still relatively new class of solvents, are attractive for biomass pretreatment because some demonstrate the rare ability to dissolve all components of lignocellulosic biomass including highly ordered (crystalline) cellulose. In the present study, three ILs, 1-butyl-3-methylimidazolium chloride ([C4mim]Cl), 1-ethyl-3-methylimidazolium chloride ([C2mim]Cl), 1-ethyl-3-methylimidazolium acetate ([C2mim]OAc) are used to dissolve/pretreat and fractionate sugarcane bagasse. In these IL-based pretreatments the biomass is completely or partially dissolved in ILs at temperatures greater than 130°C and then precipitated by the addition of an antisolvent to the IL biomass mixture. For the first time mass balances of IL-based pretreatments are reported. Such mass balances, along with kinetics data, can be used in process modelling and design. RESULTS: Lignin removals of 10% mass of lignin in bagasse with [C4mim]Cl, 50% mass with [C2mim]Cl and 60% mass with [C2mim]OAc, are achieved by limiting the amount of water added as antisolvent to 0.5 water:IL mass ratio thus minimising lignin precipitation. Enzyme saccharification (24 h, 15FPU) yields (% cellulose mass in starting bagasse) from the recovered solids rank as: [C2mim]OAc(83%) > >[C2mim]Cl(53%) = [C4mim]Cl(53%). Composition of [C2mim]OAc-treated solids such as low lignin, low acetyl group content and preservation of arabinosyl groups are characteristic of aqueous alkali pretreatments while those of chloride IL-treated solids resemble aqueous acid pretreatments. All ILs are fully recovered after use (100% mass as determined by ion chromatography). CONCLUSIONS: In all three ILs regulated addition of water as an antisolvent effected a polysaccharide enriched precipitate since some of the lignin remained dissolved in the aqueous IL solution. Of the three IL studied [C2mim]OAc gave the best saccharification yield, material recovery and delignification. The effects of [C2mim]OAc pretreatment resemble those of aqueous alkali pretreatments while those of [C2mim]Cl and [C4mim]Cl resemble aqueous acid pretreatments. The use of imidazolium IL solvents with shorter alkyl chains results in accelerated dissolution, pretreatment and degradation. BioMed Central 2012-08-24 /pmc/articles/PMC3495841/ /pubmed/22920045 http://dx.doi.org/10.1186/1754-6834-5-62 Text en Copyright ©2012 Karatzos et al.; licensee BioMed Central Ltd. http://creativecommons.org/licenses/by/2.0 This is an Open Access article distributed under the terms of the Creative Commons Attribution License (http://creativecommons.org/licenses/by/2.0), which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.
spellingShingle Research
Karatzos, Sergios Kimon
Edye, Leslie Alan
Doherty, William Orlando Sinclair
Sugarcane bagasse pretreatment using three imidazolium-based ionic liquids; mass balances and enzyme kinetics
title Sugarcane bagasse pretreatment using three imidazolium-based ionic liquids; mass balances and enzyme kinetics
title_full Sugarcane bagasse pretreatment using three imidazolium-based ionic liquids; mass balances and enzyme kinetics
title_fullStr Sugarcane bagasse pretreatment using three imidazolium-based ionic liquids; mass balances and enzyme kinetics
title_full_unstemmed Sugarcane bagasse pretreatment using three imidazolium-based ionic liquids; mass balances and enzyme kinetics
title_short Sugarcane bagasse pretreatment using three imidazolium-based ionic liquids; mass balances and enzyme kinetics
title_sort sugarcane bagasse pretreatment using three imidazolium-based ionic liquids; mass balances and enzyme kinetics
topic Research
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC3495841/
https://www.ncbi.nlm.nih.gov/pubmed/22920045
http://dx.doi.org/10.1186/1754-6834-5-62
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