Interplay of Acid-Base Ratio and Recycling on the Pretreatment Performance of the Protic Ionic Liquid Monoethanolammonium Acetate

Detalhes bibliográficos
Autor(a) principal: Nakasu, Pedro Y. S.
Data de Publicação: 2020
Outros Autores: Clarke, Coby J., Rabelo, Sarita C. [UNESP], Costa, Aline C., Brandt-Talbot, Agnieszka, Hallett, Jason P.
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Institucional da UNESP
Texto Completo: http://dx.doi.org/10.1021/acssuschemeng.0c01311
http://hdl.handle.net/11449/198919
Resumo: The use of protic ammonium ionic liquids (PILs) in the pretreatment of lignocellulosic biomass is a promising alternative to using expensive aprotic ionic liquids such as 1-ethyl-3-methylimidazolium acetate, [Emim][OAc]. In this work, the PIL monoethanolammonium acetate, [MEA][OAc], was used for the pretreatment of sugar cane bagasse. The study investigated changing the acid base ratio (ABR) from 0.1 to 10 and recycling of the solvent. We determined the lignin extraction, lignin recovery, solvent recovery, and enzymatic saccharification yield and compared the performance to that of the pure amine base, monoethanolamine. We found that lignin extraction and glucose release during enzymatic saccharification increased with base (amine) content, reaching up to 84% and 96%, respectively, after 72 h of saccharification for the 0.1 ABR. Up to 97% of the solvent was recovered for the 1.0 ABR. A higher acid content led to increased hemicellulose extraction into the liquid phase and reduced ionic liquid recovery. A partial conversion of the PIL into N-(hydroxyethyl) acetamide was observed after pretreatment, with up to 86% of conversion after the sixth use for the 1.0 ABR. A negative correlation (R2 = 0.96) was found between the acetamide content in the solvent and the saccharification yield. The drop in pretreatment performance was also correlated with a decrease in accumulated lignin recovery and the molecular weight of the isolated lignins. Acetamide formation was reduced when excess base was present. Recycling of the mixture with 0.5 ABR showed that the performance was unchanged (97% saccharification yield) after three uses, although 28% of the mixture was converted into the acetamide. The study shows that protic acetate ILs made from primary amines form an equilibrium with their amide and a low ABR is required in order to maintain high pretreatment efficiency when the PIL is reused.
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spelling Interplay of Acid-Base Ratio and Recycling on the Pretreatment Performance of the Protic Ionic Liquid Monoethanolammonium AcetateAcid base ratioPretreatmentProtic ionic liquidSolvent recyclingSugar cane bagasseThe use of protic ammonium ionic liquids (PILs) in the pretreatment of lignocellulosic biomass is a promising alternative to using expensive aprotic ionic liquids such as 1-ethyl-3-methylimidazolium acetate, [Emim][OAc]. In this work, the PIL monoethanolammonium acetate, [MEA][OAc], was used for the pretreatment of sugar cane bagasse. The study investigated changing the acid base ratio (ABR) from 0.1 to 10 and recycling of the solvent. We determined the lignin extraction, lignin recovery, solvent recovery, and enzymatic saccharification yield and compared the performance to that of the pure amine base, monoethanolamine. We found that lignin extraction and glucose release during enzymatic saccharification increased with base (amine) content, reaching up to 84% and 96%, respectively, after 72 h of saccharification for the 0.1 ABR. Up to 97% of the solvent was recovered for the 1.0 ABR. A higher acid content led to increased hemicellulose extraction into the liquid phase and reduced ionic liquid recovery. A partial conversion of the PIL into N-(hydroxyethyl) acetamide was observed after pretreatment, with up to 86% of conversion after the sixth use for the 1.0 ABR. A negative correlation (R2 = 0.96) was found between the acetamide content in the solvent and the saccharification yield. The drop in pretreatment performance was also correlated with a decrease in accumulated lignin recovery and the molecular weight of the isolated lignins. Acetamide formation was reduced when excess base was present. Recycling of the mixture with 0.5 ABR showed that the performance was unchanged (97% saccharification yield) after three uses, although 28% of the mixture was converted into the acetamide. The study shows that protic acetate ILs made from primary amines form an equilibrium with their amide and a low ABR is required in order to maintain high pretreatment efficiency when the PIL is reused.Process and Products Development Department Faculty of Chemical Engineering State University of Campinas (UNICAMP), Av. Albert Einstein, 500Department of Chemical Engineering Imperial College LondonDepartment of Bioprocess and Biotechnology College of Agricultural Sciences São Paulo State University (UNESP), Av. Universitária, 3780Department of Bioprocess and Biotechnology College of Agricultural Sciences São Paulo State University (UNESP), Av. Universitária, 3780Universidade Estadual de Campinas (UNICAMP)Imperial College LondonUniversidade Estadual Paulista (Unesp)Nakasu, Pedro Y. S.Clarke, Coby J.Rabelo, Sarita C. [UNESP]Costa, Aline C.Brandt-Talbot, AgnieszkaHallett, Jason P.2020-12-12T01:25:34Z2020-12-12T01:25:34Z2020-06-01info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/article7952-7961http://dx.doi.org/10.1021/acssuschemeng.0c01311ACS Sustainable Chemistry and Engineering, v. 8, n. 21, p. 7952-7961, 2020.2168-0485http://hdl.handle.net/11449/19891910.1021/acssuschemeng.0c013112-s2.0-85085772110Scopusreponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPengACS Sustainable Chemistry and Engineeringinfo:eu-repo/semantics/openAccess2021-10-22T21:03:00Zoai:repositorio.unesp.br:11449/198919Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462024-08-05T18:03:29.613656Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false
dc.title.none.fl_str_mv Interplay of Acid-Base Ratio and Recycling on the Pretreatment Performance of the Protic Ionic Liquid Monoethanolammonium Acetate
title Interplay of Acid-Base Ratio and Recycling on the Pretreatment Performance of the Protic Ionic Liquid Monoethanolammonium Acetate
spellingShingle Interplay of Acid-Base Ratio and Recycling on the Pretreatment Performance of the Protic Ionic Liquid Monoethanolammonium Acetate
Nakasu, Pedro Y. S.
Acid base ratio
Pretreatment
Protic ionic liquid
Solvent recycling
Sugar cane bagasse
title_short Interplay of Acid-Base Ratio and Recycling on the Pretreatment Performance of the Protic Ionic Liquid Monoethanolammonium Acetate
title_full Interplay of Acid-Base Ratio and Recycling on the Pretreatment Performance of the Protic Ionic Liquid Monoethanolammonium Acetate
title_fullStr Interplay of Acid-Base Ratio and Recycling on the Pretreatment Performance of the Protic Ionic Liquid Monoethanolammonium Acetate
title_full_unstemmed Interplay of Acid-Base Ratio and Recycling on the Pretreatment Performance of the Protic Ionic Liquid Monoethanolammonium Acetate
title_sort Interplay of Acid-Base Ratio and Recycling on the Pretreatment Performance of the Protic Ionic Liquid Monoethanolammonium Acetate
author Nakasu, Pedro Y. S.
author_facet Nakasu, Pedro Y. S.
Clarke, Coby J.
Rabelo, Sarita C. [UNESP]
Costa, Aline C.
Brandt-Talbot, Agnieszka
Hallett, Jason P.
author_role author
author2 Clarke, Coby J.
Rabelo, Sarita C. [UNESP]
Costa, Aline C.
Brandt-Talbot, Agnieszka
Hallett, Jason P.
author2_role author
author
author
author
author
dc.contributor.none.fl_str_mv Universidade Estadual de Campinas (UNICAMP)
Imperial College London
Universidade Estadual Paulista (Unesp)
dc.contributor.author.fl_str_mv Nakasu, Pedro Y. S.
Clarke, Coby J.
Rabelo, Sarita C. [UNESP]
Costa, Aline C.
Brandt-Talbot, Agnieszka
Hallett, Jason P.
dc.subject.por.fl_str_mv Acid base ratio
Pretreatment
Protic ionic liquid
Solvent recycling
Sugar cane bagasse
topic Acid base ratio
Pretreatment
Protic ionic liquid
Solvent recycling
Sugar cane bagasse
description The use of protic ammonium ionic liquids (PILs) in the pretreatment of lignocellulosic biomass is a promising alternative to using expensive aprotic ionic liquids such as 1-ethyl-3-methylimidazolium acetate, [Emim][OAc]. In this work, the PIL monoethanolammonium acetate, [MEA][OAc], was used for the pretreatment of sugar cane bagasse. The study investigated changing the acid base ratio (ABR) from 0.1 to 10 and recycling of the solvent. We determined the lignin extraction, lignin recovery, solvent recovery, and enzymatic saccharification yield and compared the performance to that of the pure amine base, monoethanolamine. We found that lignin extraction and glucose release during enzymatic saccharification increased with base (amine) content, reaching up to 84% and 96%, respectively, after 72 h of saccharification for the 0.1 ABR. Up to 97% of the solvent was recovered for the 1.0 ABR. A higher acid content led to increased hemicellulose extraction into the liquid phase and reduced ionic liquid recovery. A partial conversion of the PIL into N-(hydroxyethyl) acetamide was observed after pretreatment, with up to 86% of conversion after the sixth use for the 1.0 ABR. A negative correlation (R2 = 0.96) was found between the acetamide content in the solvent and the saccharification yield. The drop in pretreatment performance was also correlated with a decrease in accumulated lignin recovery and the molecular weight of the isolated lignins. Acetamide formation was reduced when excess base was present. Recycling of the mixture with 0.5 ABR showed that the performance was unchanged (97% saccharification yield) after three uses, although 28% of the mixture was converted into the acetamide. The study shows that protic acetate ILs made from primary amines form an equilibrium with their amide and a low ABR is required in order to maintain high pretreatment efficiency when the PIL is reused.
publishDate 2020
dc.date.none.fl_str_mv 2020-12-12T01:25:34Z
2020-12-12T01:25:34Z
2020-06-01
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/article
format article
status_str publishedVersion
dc.identifier.uri.fl_str_mv http://dx.doi.org/10.1021/acssuschemeng.0c01311
ACS Sustainable Chemistry and Engineering, v. 8, n. 21, p. 7952-7961, 2020.
2168-0485
http://hdl.handle.net/11449/198919
10.1021/acssuschemeng.0c01311
2-s2.0-85085772110
url http://dx.doi.org/10.1021/acssuschemeng.0c01311
http://hdl.handle.net/11449/198919
identifier_str_mv ACS Sustainable Chemistry and Engineering, v. 8, n. 21, p. 7952-7961, 2020.
2168-0485
10.1021/acssuschemeng.0c01311
2-s2.0-85085772110
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv ACS Sustainable Chemistry and Engineering
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv 7952-7961
dc.source.none.fl_str_mv Scopus
reponame:Repositório Institucional da UNESP
instname:Universidade Estadual Paulista (UNESP)
instacron:UNESP
instname_str Universidade Estadual Paulista (UNESP)
instacron_str UNESP
institution UNESP
reponame_str Repositório Institucional da UNESP
collection Repositório Institucional da UNESP
repository.name.fl_str_mv Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)
repository.mail.fl_str_mv
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