PoplarV1, Main, Exploration, bibRecord, 000759

Pretreatment and enzymatic hydrolysis for the efficient production of glucose and furfural from wheat straw, pine and poplar chips.

Identifieur interne : 000759 ( Main/Exploration ); précédent : 000758; suivant : 000760

Pretreatment and enzymatic hydrolysis for the efficient production of glucose and furfural from wheat straw, pine and poplar chips.

Auteurs : Alfonso Cornejo [Espagne] ; Irantzu Alegria-Dallo [Espagne] ; Í Igo García-Yoldi [Espagne] ; Í Igo Sarobe [Espagne] ; David Sánchez [Espagne] ; Eduardo Otazu [Espagne] ; Ibai Funcia [Espagne] ; María J. Gil [Espagne] ; Víctor Martínez-Merino [Espagne]

Source :

Bioresource technology [ 1873-2976 ] ; 2019.

RBID : pubmed:31176941

Descripteurs français

KwdFr :
- Biomasse (MeSH), Furfural (MeSH), Glucose (MeSH), Hydrolyse (MeSH), Triticum (MeSH).
MESH :
- Biomasse, Furfural, Glucose, Hydrolyse, Triticum.

English descriptors

KwdEn :
- Biomass (MeSH), Furaldehyde (MeSH), Glucose (MeSH), Hydrolysis (MeSH), Triticum (MeSH).
MESH :
- chemical : Furaldehyde, Glucose.
- Biomass, Hydrolysis, Triticum.

Abstract

A flexible approach to a two-step Biorefinery for the production of glucose and furfural from three different feedstocks is presented. Pretreatment conditions were selected to drive the production towards the generation of glucose or furfural. Harsh pretreatment conditions produced solids with highly accessible glycan contents for the enzymatic hydrolysis with 100% glucose yields when wheat straw or poplar chips were used as feedstock. Mild conditions afforded xylan-rich hydrolysates that could be efficiently transformed to furfural, either under conventional or microwave heating in biphasic media. Yields for the transformation of xylan from feedstocks ranged between 45% and 90% depending on the feedstock, the thermal pretreatment and the cyclodehydration conditions. Up to 12.6 kg of glucose and materials and 2.5 kg of furfural can be produced starting from 50 kg of biomass. A new analytical methodology based on ¹³C NMR that provided good quality analytical results is also presented.

DOI: 10.1016/j.biortech.2019.121583
PubMed: 31176941

Affiliations:

Links toward previous steps (curation, corpus...)

to stream Main, to step Corpus: 000852
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Le document en format XML

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<series><title level="j">Bioresource technology</title>
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<imprint><date when="2019" type="published">2019</date>
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<profileDesc><textClass><keywords scheme="KwdEn" xml:lang="en"><term>Biomass (MeSH)</term>
<term>Furaldehyde (MeSH)</term>
<term>Glucose (MeSH)</term>
<term>Hydrolysis (MeSH)</term>
<term>Triticum (MeSH)</term>
</keywords>
<keywords scheme="KwdFr" xml:lang="fr"><term>Biomasse (MeSH)</term>
<term>Furfural (MeSH)</term>
<term>Glucose (MeSH)</term>
<term>Hydrolyse (MeSH)</term>
<term>Triticum (MeSH)</term>
</keywords>
<keywords scheme="MESH" type="chemical" xml:lang="en"><term>Furaldehyde</term>
<term>Glucose</term>
</keywords>
<keywords scheme="MESH" xml:lang="en"><term>Biomass</term>
<term>Hydrolysis</term>
<term>Triticum</term>
</keywords>
<keywords scheme="MESH" xml:lang="fr"><term>Biomasse</term>
<term>Furfural</term>
<term>Glucose</term>
<term>Hydrolyse</term>
<term>Triticum</term>
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<front><div type="abstract" xml:lang="en">A flexible approach to a two-step Biorefinery for the production of glucose and furfural from three different feedstocks is presented. Pretreatment conditions were selected to drive the production towards the generation of glucose or furfural. Harsh pretreatment conditions produced solids with highly accessible glycan contents for the enzymatic hydrolysis with 100% glucose yields when wheat straw or poplar chips were used as feedstock. Mild conditions afforded xylan-rich hydrolysates that could be efficiently transformed to furfural, either under conventional or microwave heating in biphasic media. Yields for the transformation of xylan from feedstocks ranged between 45% and 90% depending on the feedstock, the thermal pretreatment and the cyclodehydration conditions. Up to 12.6 kg of glucose and materials and 2.5 kg of furfural can be produced starting from 50 kg of biomass. A new analytical methodology based on <sup>13</sup>
C NMR that provided good quality analytical results is also presented.</div>
</front>
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<Title>Bioresource technology</Title>
<ISOAbbreviation>Bioresour Technol</ISOAbbreviation>
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<ArticleTitle>Pretreatment and enzymatic hydrolysis for the efficient production of glucose and furfural from wheat straw, pine and poplar chips.</ArticleTitle>
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<Abstract><AbstractText>A flexible approach to a two-step Biorefinery for the production of glucose and furfural from three different feedstocks is presented. Pretreatment conditions were selected to drive the production towards the generation of glucose or furfural. Harsh pretreatment conditions produced solids with highly accessible glycan contents for the enzymatic hydrolysis with 100% glucose yields when wheat straw or poplar chips were used as feedstock. Mild conditions afforded xylan-rich hydrolysates that could be efficiently transformed to furfural, either under conventional or microwave heating in biphasic media. Yields for the transformation of xylan from feedstocks ranged between 45% and 90% depending on the feedstock, the thermal pretreatment and the cyclodehydration conditions. Up to 12.6 kg of glucose and materials and 2.5 kg of furfural can be produced starting from 50 kg of biomass. A new analytical methodology based on <sup>13</sup>
C NMR that provided good quality analytical results is also presented.</AbstractText>
<CopyrightInformation>Copyright © 2019 Elsevier Ltd. All rights reserved.</CopyrightInformation>
</Abstract>
<AuthorList CompleteYN="Y"><Author ValidYN="Y"><LastName>Cornejo</LastName>
<ForeName>Alfonso</ForeName>
<Initials>A</Initials>
<AffiliationInfo><Affiliation>Institute for Advanced Materials (INAMAT)-Dpt. of Sciences, Campus de Arrosadia, Universidad Pública de Navarra, E31006 Pamplona, Spain. Electronic address: alfonso.cornejo@unavarra.es.</Affiliation>
</AffiliationInfo>
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<Author ValidYN="Y"><LastName>Alegria-Dallo</LastName>
<ForeName>Irantzu</ForeName>
<Initials>I</Initials>
<AffiliationInfo><Affiliation>National Renewable Energy Centre (CENER), Av. Ciudad de la Innovación 7, E31621 Sarriguren, Spain.</Affiliation>
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<Author ValidYN="Y"><LastName>García-Yoldi</LastName>
<ForeName>Íñigo</ForeName>
<Initials>Í</Initials>
<AffiliationInfo><Affiliation>Institute for Advanced Materials (INAMAT)-Dpt. of Sciences, Campus de Arrosadia, Universidad Pública de Navarra, E31006 Pamplona, Spain.</Affiliation>
</AffiliationInfo>
</Author>
<Author ValidYN="Y"><LastName>Sarobe</LastName>
<ForeName>Íñigo</ForeName>
<Initials>Í</Initials>
<AffiliationInfo><Affiliation>Institute for Advanced Materials (INAMAT)-Dpt. of Sciences, Campus de Arrosadia, Universidad Pública de Navarra, E31006 Pamplona, Spain.</Affiliation>
</AffiliationInfo>
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<Author ValidYN="Y"><LastName>Sánchez</LastName>
<ForeName>David</ForeName>
<Initials>D</Initials>
<AffiliationInfo><Affiliation>National Renewable Energy Centre (CENER), Av. Ciudad de la Innovación 7, E31621 Sarriguren, Spain.</Affiliation>
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<Author ValidYN="Y"><LastName>Otazu</LastName>
<ForeName>Eduardo</ForeName>
<Initials>E</Initials>
<AffiliationInfo><Affiliation>National Renewable Energy Centre (CENER), Av. Ciudad de la Innovación 7, E31621 Sarriguren, Spain.</Affiliation>
</AffiliationInfo>
</Author>
<Author ValidYN="Y"><LastName>Funcia</LastName>
<ForeName>Ibai</ForeName>
<Initials>I</Initials>
<AffiliationInfo><Affiliation>National Renewable Energy Centre (CENER), Av. Ciudad de la Innovación 7, E31621 Sarriguren, Spain.</Affiliation>
</AffiliationInfo>
</Author>
<Author ValidYN="Y"><LastName>Gil</LastName>
<ForeName>María J</ForeName>
<Initials>MJ</Initials>
<AffiliationInfo><Affiliation>Institute for Advanced Materials (INAMAT)-Dpt. of Sciences, Campus de Arrosadia, Universidad Pública de Navarra, E31006 Pamplona, Spain.</Affiliation>
</AffiliationInfo>
</Author>
<Author ValidYN="Y"><LastName>Martínez-Merino</LastName>
<ForeName>Víctor</ForeName>
<Initials>V</Initials>
<AffiliationInfo><Affiliation>Institute for Advanced Materials (INAMAT)-Dpt. of Sciences, Campus de Arrosadia, Universidad Pública de Navarra, E31006 Pamplona, Spain.</Affiliation>
</AffiliationInfo>
</Author>
</AuthorList>
<Language>eng</Language>
<PublicationTypeList><PublicationType UI="D016428">Journal Article</PublicationType>
</PublicationTypeList>
<ArticleDate DateType="Electronic"><Year>2019</Year>
<Month>05</Month>
<Day>31</Day>
</ArticleDate>
</Article>
<MedlineJournalInfo><Country>England</Country>
<MedlineTA>Bioresour Technol</MedlineTA>
<NlmUniqueID>9889523</NlmUniqueID>
<ISSNLinking>0960-8524</ISSNLinking>
</MedlineJournalInfo>
<ChemicalList><Chemical><RegistryNumber>DJ1HGI319P</RegistryNumber>
<NameOfSubstance UI="D005662">Furaldehyde</NameOfSubstance>
</Chemical>
<Chemical><RegistryNumber>IY9XDZ35W2</RegistryNumber>
<NameOfSubstance UI="D005947">Glucose</NameOfSubstance>
</Chemical>
</ChemicalList>
<CitationSubset>IM</CitationSubset>
<MeshHeadingList><MeshHeading><DescriptorName UI="D018533" MajorTopicYN="N">Biomass</DescriptorName>
</MeshHeading>
<MeshHeading><DescriptorName UI="D005662" MajorTopicYN="Y">Furaldehyde</DescriptorName>
</MeshHeading>
<MeshHeading><DescriptorName UI="D005947" MajorTopicYN="N">Glucose</DescriptorName>
</MeshHeading>
<MeshHeading><DescriptorName UI="D006868" MajorTopicYN="N">Hydrolysis</DescriptorName>
</MeshHeading>
<MeshHeading><DescriptorName UI="D014908" MajorTopicYN="Y">Triticum</DescriptorName>
</MeshHeading>
</MeshHeadingList>
<KeywordList Owner="NOTNLM"><Keyword MajorTopicYN="N">Biorefinery</Keyword>
<Keyword MajorTopicYN="N">Biphasic medium</Keyword>
<Keyword MajorTopicYN="N">Cyclodehydration</Keyword>
<Keyword MajorTopicYN="N">Enzymatic hydrolysis</Keyword>
<Keyword MajorTopicYN="N">Glucose</Keyword>
<Keyword MajorTopicYN="N">Microwave</Keyword>
<Keyword MajorTopicYN="N">NMR quantification</Keyword>
<Keyword MajorTopicYN="N">Scale up</Keyword>
<Keyword MajorTopicYN="N">Thermochemical pretreatment</Keyword>
</KeywordList>
</MedlineCitation>
<PubmedData><History><PubMedPubDate PubStatus="received"><Year>2019</Year>
<Month>04</Month>
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Pretreatment and enzymatic hydrolysis for the efficient production of glucose and furfural from wheat straw, pine and poplar chips.

Pretreatment and enzymatic hydrolysis for the efficient production of glucose and furfural from wheat straw, pine and poplar chips.

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