Kinetic modeling of hemicellulose-derived biomass hydrolysis under high pressure CO2–H2O mixture technology

Detalhes bibliográficos
Autor(a) principal: Relvas, F.
Data de Publicação: 2015
Outros Autores: Morais, Ana Rita C., Lukasik, Rafal M.
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
Texto Completo: http://hdl.handle.net/10400.9/2878
Resumo: This work is focused on the development of kinetic models of hydrolysis of hemicellulose-derived wheat straw under high-pressure CO2.H2O technology. The experiments were performed at fixed temperature (180.C), varying pressure from 0 (water-only reaction), 20, 35 to 50 bar of initial CO2 pressure and reaction times varied from 0 to 45 min. The three accurate kinetic models allowed to describe the effect of reaction conditions mainly hitherto not studied CO2 pressure and reaction time on the concentration of intermediate compounds such as xylose and arabinose in both oligomer and monomer form as well as final compounds e.g. acetic acid, furfural and other degradation products. Modeling demonstrated that addition of CO2 plays an important role in kinetics study of hemicellulose fraction hydrolysis being the fastest step the polysaccharides f hydrolysis into sugars in oligomer form. Even negligible amount of CO2 (20 bar of initial pressure) improves the initial kinetic constant of aforementioned reaction by almost 40% in comparison to water-only process. Depletion of oligosaccharides ' concentration and counterbalanced production of monomer sugars were found for longer reaction times, achieving maximum faster for CO2 assisted than CO2 free processes. Moreover, the increase of initial CO2 pressure demonstrated to be highly efficient in enhancement of the kinetic constants of all reactions occurring in the liquors. The developed models demonstrated a good fitting to the experimental data albeit the complex composition of raw material as well as the multistep analytical process.
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spelling Kinetic modeling of hemicellulose-derived biomass hydrolysis under high pressure CO2–H2O mixture technologyHydrolysisLignocellulosic biomassXylanHemicelluloseKineticsOligosaccharidesCarbon dioxideThis work is focused on the development of kinetic models of hydrolysis of hemicellulose-derived wheat straw under high-pressure CO2.H2O technology. The experiments were performed at fixed temperature (180.C), varying pressure from 0 (water-only reaction), 20, 35 to 50 bar of initial CO2 pressure and reaction times varied from 0 to 45 min. The three accurate kinetic models allowed to describe the effect of reaction conditions mainly hitherto not studied CO2 pressure and reaction time on the concentration of intermediate compounds such as xylose and arabinose in both oligomer and monomer form as well as final compounds e.g. acetic acid, furfural and other degradation products. Modeling demonstrated that addition of CO2 plays an important role in kinetics study of hemicellulose fraction hydrolysis being the fastest step the polysaccharides f hydrolysis into sugars in oligomer form. Even negligible amount of CO2 (20 bar of initial pressure) improves the initial kinetic constant of aforementioned reaction by almost 40% in comparison to water-only process. Depletion of oligosaccharides ' concentration and counterbalanced production of monomer sugars were found for longer reaction times, achieving maximum faster for CO2 assisted than CO2 free processes. Moreover, the increase of initial CO2 pressure demonstrated to be highly efficient in enhancement of the kinetic constants of all reactions occurring in the liquors. The developed models demonstrated a good fitting to the experimental data albeit the complex composition of raw material as well as the multistep analytical process.ElsevierRepositório do LNEGRelvas, F.Morais, Ana Rita C.Lukasik, Rafal M.2016-03-11T17:15:38Z2015-01-01T00:00:00Z2015-01-01T00:00:00Zinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleapplication/pdfhttp://hdl.handle.net/10400.9/2878engRelvas, F.; Morais, A.R.; Bogel-Lukasik, R. - Kinetic modeling of hemicellulose-derived biomass hydrolysis under high pressure CO2–H2O mixture technology. In: Journal of Supercritical Fluids, 2015, Vol. 99, p. 95-1020896-844610.1016/j.supflu.2015.01.022info:eu-repo/semantics/openAccessreponame:Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)instname:Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informaçãoinstacron:RCAAP2022-09-06T12:28:07Zoai:repositorio.lneg.pt:10400.9/2878Portal AgregadorONGhttps://www.rcaap.pt/oai/openaireopendoar:71602024-03-19T15:35:55.231967Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) - Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informaçãofalse
dc.title.none.fl_str_mv Kinetic modeling of hemicellulose-derived biomass hydrolysis under high pressure CO2–H2O mixture technology
title Kinetic modeling of hemicellulose-derived biomass hydrolysis under high pressure CO2–H2O mixture technology
spellingShingle Kinetic modeling of hemicellulose-derived biomass hydrolysis under high pressure CO2–H2O mixture technology
Relvas, F.
Hydrolysis
Lignocellulosic biomass
Xylan
Hemicellulose
Kinetics
Oligosaccharides
Carbon dioxide
title_short Kinetic modeling of hemicellulose-derived biomass hydrolysis under high pressure CO2–H2O mixture technology
title_full Kinetic modeling of hemicellulose-derived biomass hydrolysis under high pressure CO2–H2O mixture technology
title_fullStr Kinetic modeling of hemicellulose-derived biomass hydrolysis under high pressure CO2–H2O mixture technology
title_full_unstemmed Kinetic modeling of hemicellulose-derived biomass hydrolysis under high pressure CO2–H2O mixture technology
title_sort Kinetic modeling of hemicellulose-derived biomass hydrolysis under high pressure CO2–H2O mixture technology
author Relvas, F.
author_facet Relvas, F.
Morais, Ana Rita C.
Lukasik, Rafal M.
author_role author
author2 Morais, Ana Rita C.
Lukasik, Rafal M.
author2_role author
author
dc.contributor.none.fl_str_mv Repositório do LNEG
dc.contributor.author.fl_str_mv Relvas, F.
Morais, Ana Rita C.
Lukasik, Rafal M.
dc.subject.por.fl_str_mv Hydrolysis
Lignocellulosic biomass
Xylan
Hemicellulose
Kinetics
Oligosaccharides
Carbon dioxide
topic Hydrolysis
Lignocellulosic biomass
Xylan
Hemicellulose
Kinetics
Oligosaccharides
Carbon dioxide
description This work is focused on the development of kinetic models of hydrolysis of hemicellulose-derived wheat straw under high-pressure CO2.H2O technology. The experiments were performed at fixed temperature (180.C), varying pressure from 0 (water-only reaction), 20, 35 to 50 bar of initial CO2 pressure and reaction times varied from 0 to 45 min. The three accurate kinetic models allowed to describe the effect of reaction conditions mainly hitherto not studied CO2 pressure and reaction time on the concentration of intermediate compounds such as xylose and arabinose in both oligomer and monomer form as well as final compounds e.g. acetic acid, furfural and other degradation products. Modeling demonstrated that addition of CO2 plays an important role in kinetics study of hemicellulose fraction hydrolysis being the fastest step the polysaccharides f hydrolysis into sugars in oligomer form. Even negligible amount of CO2 (20 bar of initial pressure) improves the initial kinetic constant of aforementioned reaction by almost 40% in comparison to water-only process. Depletion of oligosaccharides ' concentration and counterbalanced production of monomer sugars were found for longer reaction times, achieving maximum faster for CO2 assisted than CO2 free processes. Moreover, the increase of initial CO2 pressure demonstrated to be highly efficient in enhancement of the kinetic constants of all reactions occurring in the liquors. The developed models demonstrated a good fitting to the experimental data albeit the complex composition of raw material as well as the multistep analytical process.
publishDate 2015
dc.date.none.fl_str_mv 2015-01-01T00:00:00Z
2015-01-01T00:00:00Z
2016-03-11T17:15:38Z
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://hdl.handle.net/10400.9/2878
url http://hdl.handle.net/10400.9/2878
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv Relvas, F.; Morais, A.R.; Bogel-Lukasik, R. - Kinetic modeling of hemicellulose-derived biomass hydrolysis under high pressure CO2–H2O mixture technology. In: Journal of Supercritical Fluids, 2015, Vol. 99, p. 95-102
0896-8446
10.1016/j.supflu.2015.01.022
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv application/pdf
dc.publisher.none.fl_str_mv Elsevier
publisher.none.fl_str_mv Elsevier
dc.source.none.fl_str_mv reponame:Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
instname:Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação
instacron:RCAAP
instname_str Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação
instacron_str RCAAP
institution RCAAP
reponame_str Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
collection Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
repository.name.fl_str_mv Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) - Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação
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