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...
- 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
- Idioma:
- 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
- License
- http://purl.org/coar/access_right/c_14cb
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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 |
dc.type.redcol.none.fl_str_mv |
http://purl.org/redcol/resource_type/ART |
dc.type.version.none.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
format |
http://purl.org/coar/resource_type/c_6501 |
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 |
_version_ |
1814247153410768896 |