Gasification of sawdust and wood chips in a fixed bed under autothermal and stable conditions

The high potential in Colombian agroforestry residues can be exploited through gasification; however, biomass pretreatment must be minimized to increase process efficiency. In this article, the gasification of woodchips and sawdust mixtures (0, 30, 70, and 100% of sawdust, wt%) with three air veloci...

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Autores:
Lenis, Yuhan A.
Pérez J.F.
Tipo de recurso:
Article of journal
Fecha de publicación:
2014
Institución:
Universidad Cooperativa de Colombia
Repositorio:
Repositorio UCC
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OAI Identifier:
oai:repository.ucc.edu.co:20.500.12494/41713
Acceso en línea:
https://doi.org/10.15381/rivep.v29i4.14297
https://hdl.handle.net/20.500.12494/41713
Palabra clave:
Chemical reactors
Convergence of numerical methods
Fluidization
Particle size
Particle size analysis
Sawdust
Wood products
Auto-thermal
Biomass pre treatments
Devolatilization
Fixed bed
Fixed bed reactor
Process efficiency
Sawdust mixture
Woodchips
Gasification
Chips
Gasification
Saw Dust
Stability
Rights
closedAccess
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http://purl.org/coar/access_right/c_14cb
id COOPER2_cc439d6d193c531c9fa74df9edb1c464
oai_identifier_str oai:repository.ucc.edu.co:20.500.12494/41713
network_acronym_str COOPER2
network_name_str Repositorio UCC
repository_id_str
spelling Lenis, Yuhan A.Pérez J.F.2021-12-16T22:15:44Z2021-12-16T22:15:44Z2014https://doi.org/10.15381/rivep.v29i4.1429715567036https://hdl.handle.net/20.500.12494/41713Lenis YA,Pérez JF. Gasification of sawdust and wood chips in a fixed bed under autothermal and stable conditions. Energy Sources Recovery Util. Environ. Eff. 2014. 36. (23):p. 2555-2565. .The high potential in Colombian agroforestry residues can be exploited through gasification; however, biomass pretreatment must be minimized to increase process efficiency. In this article, the gasification of woodchips and sawdust mixtures (0, 30, 70, and 100% of sawdust, wt%) with three air velocities below the fluidization one is studied. Experiments were carried out on a lab scale fixed-bed reactor. For sawdust percentages greater than 30%, the particle size distribution causes the fluidized smaller particles to leave from the reactor. Biomass losses are due to the weight and size reduction of the particles during drying and devolatilization subprocesses; this instability can lead to formation of bridging and extinction of the reaction front. © Copyright Taylor & Francis.2565-2555Taylor & FrancisChemical reactorsConvergence of numerical methodsFluidizationParticle sizeParticle size analysisSawdustWood productsAuto-thermalBiomass pre treatmentsDevolatilizationFixed bedFixed bed reactorProcess efficiencySawdust mixtureWoodchipsGasificationChipsGasificationSaw DustStabilityGasification of sawdust and wood chips in a fixed bed under autothermal and stable conditionsArtículohttp://purl.org/coar/resource_type/c_6501http://purl.org/coar/resource_type/c_2df8fbb1http://purl.org/coar/version/c_970fb48d4fbd8a85info:eu-repo/semantics/articlehttp://purl.org/redcol/resource_type/ARTinfo:eu-repo/semantics/publishedVersionENERG SOURCE PART Ainfo:eu-repo/semantics/closedAccesshttp://purl.org/coar/access_right/c_14cbPublication20.500.12494/41713oai:repository.ucc.edu.co:20.500.12494/417132024-08-20 16:21:28.578metadata.onlyhttps://repository.ucc.edu.coRepositorio Institucional Universidad Cooperativa de Colombiabdigital@metabiblioteca.com
dc.title.spa.fl_str_mv Gasification of sawdust and wood chips in a fixed bed under autothermal and stable conditions
title Gasification of sawdust and wood chips in a fixed bed under autothermal and stable conditions
spellingShingle Gasification of sawdust and wood chips in a fixed bed under autothermal and stable conditions
Chemical reactors
Convergence of numerical methods
Fluidization
Particle size
Particle size analysis
Sawdust
Wood products
Auto-thermal
Biomass pre treatments
Devolatilization
Fixed bed
Fixed bed reactor
Process efficiency
Sawdust mixture
Woodchips
Gasification
Chips
Gasification
Saw Dust
Stability
title_short Gasification of sawdust and wood chips in a fixed bed under autothermal and stable conditions
title_full Gasification of sawdust and wood chips in a fixed bed under autothermal and stable conditions
title_fullStr Gasification of sawdust and wood chips in a fixed bed under autothermal and stable conditions
title_full_unstemmed Gasification of sawdust and wood chips in a fixed bed under autothermal and stable conditions
title_sort Gasification of sawdust and wood chips in a fixed bed under autothermal and stable conditions
dc.creator.fl_str_mv Lenis, Yuhan A.
Pérez J.F.
dc.contributor.author.none.fl_str_mv Lenis, Yuhan A.
Pérez J.F.
dc.subject.spa.fl_str_mv Chemical reactors
Convergence of numerical methods
Fluidization
Particle size
Particle size analysis
Sawdust
Wood products
Auto-thermal
Biomass pre treatments
Devolatilization
Fixed bed
Fixed bed reactor
Process efficiency
Sawdust mixture
Woodchips
Gasification
Chips
Gasification
Saw Dust
Stability
topic Chemical reactors
Convergence of numerical methods
Fluidization
Particle size
Particle size analysis
Sawdust
Wood products
Auto-thermal
Biomass pre treatments
Devolatilization
Fixed bed
Fixed bed reactor
Process efficiency
Sawdust mixture
Woodchips
Gasification
Chips
Gasification
Saw Dust
Stability
description The high potential in Colombian agroforestry residues can be exploited through gasification; however, biomass pretreatment must be minimized to increase process efficiency. In this article, the gasification of woodchips and sawdust mixtures (0, 30, 70, and 100% of sawdust, wt%) with three air velocities below the fluidization one is studied. Experiments were carried out on a lab scale fixed-bed reactor. For sawdust percentages greater than 30%, the particle size distribution causes the fluidized smaller particles to leave from the reactor. Biomass losses are due to the weight and size reduction of the particles during drying and devolatilization subprocesses; this instability can lead to formation of bridging and extinction of the reaction front. © Copyright Taylor & Francis.
publishDate 2014
dc.date.issued.none.fl_str_mv 2014
dc.date.accessioned.none.fl_str_mv 2021-12-16T22:15:44Z
dc.date.available.none.fl_str_mv 2021-12-16T22:15:44Z
dc.type.none.fl_str_mv Artículo
dc.type.coar.fl_str_mv http://purl.org/coar/resource_type/c_2df8fbb1
dc.type.coar.none.fl_str_mv http://purl.org/coar/resource_type/c_6501
dc.type.coarversion.none.fl_str_mv http://purl.org/coar/version/c_970fb48d4fbd8a85
dc.type.driver.none.fl_str_mv info:eu-repo/semantics/article
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dc.type.version.none.fl_str_mv info:eu-repo/semantics/publishedVersion
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status_str publishedVersion
dc.identifier.none.fl_str_mv https://doi.org/10.15381/rivep.v29i4.14297
dc.identifier.issn.spa.fl_str_mv 15567036
dc.identifier.uri.none.fl_str_mv https://hdl.handle.net/20.500.12494/41713
dc.identifier.bibliographicCitation.spa.fl_str_mv Lenis YA,Pérez JF. Gasification of sawdust and wood chips in a fixed bed under autothermal and stable conditions. Energy Sources Recovery Util. Environ. Eff. 2014. 36. (23):p. 2555-2565. .
url https://doi.org/10.15381/rivep.v29i4.14297
https://hdl.handle.net/20.500.12494/41713
identifier_str_mv 15567036
Lenis YA,Pérez JF. Gasification of sawdust and wood chips in a fixed bed under autothermal and stable conditions. Energy Sources Recovery Util. Environ. Eff. 2014. 36. (23):p. 2555-2565. .
dc.relation.ispartofjournal.spa.fl_str_mv ENERG SOURCE PART A
dc.rights.accessrights.none.fl_str_mv info:eu-repo/semantics/closedAccess
dc.rights.coar.none.fl_str_mv http://purl.org/coar/access_right/c_14cb
eu_rights_str_mv closedAccess
rights_invalid_str_mv http://purl.org/coar/access_right/c_14cb
dc.format.extent.spa.fl_str_mv 2565-2555
dc.publisher.spa.fl_str_mv Taylor & Francis
institution Universidad Cooperativa de Colombia
repository.name.fl_str_mv Repositorio Institucional Universidad Cooperativa de Colombia
repository.mail.fl_str_mv bdigital@metabiblioteca.com
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