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Tar reduction in downdraft biomass gasifier using a primary method

dc.contributor.authorMachin, Einara Blanco [UNESP]
dc.contributor.authorPedroso, Daniel Travieso [UNESP]
dc.contributor.authorProenza, Nestor
dc.contributor.authorSilveira, Jose Luz [UNESP]
dc.contributor.authorConti, Leonetto
dc.contributor.authorBraga, Lucia Bollini [UNESP]
dc.contributor.authorMachin, Adrian Blanco [UNESP]
dc.contributor.institutionUniversidade Estadual Paulista (Unesp)
dc.contributor.institutionUniv Camaguey
dc.contributor.institutionUniv Sassari
dc.date.accessioned2015-10-21T21:09:22Z
dc.date.available2015-10-21T21:09:22Z
dc.date.issued2015-06-01
dc.description.abstractThis work present a novel primary method, for tar reduction in downdraft gasification. The principle of this new technology is to change the fluid dynamic behaviour of the mixture, formed by pyrolysis product and gasification agent in combustion zone; allowing a homogeneous temperature distribution in radial direction in this reaction zone. To achieve the change in the fluid dynamic behaviour of the mixture; the entry of gasification agent to combustion zone is oriented by means of wall nozzles in order to form a swirl flow. This modification in combination with the extension of the reduction zone, will allow, to increases the efficiency of the tar thermal cracking inside the gasifier and the extension of the Boudouard reactions. Consequently, the quantity of tar passing through the combustion zone without cracking and the concentration of tar in the final gas, decrease significantly in relation with the common value obtained for this type of reactor, without affecting significantly the heating value of the producer gas. In this work is presented a new design for 15 kW downdraft gasification reactor, with this technology implemented, the tar content obtained in the experiments never overcome 10 mg/Nm(3), with a lower heating value of 3.97 MJ/Nm(3). (C) 2015 Elsevier Ltd. All rights reserved.en
dc.description.affiliationSao Paulo State Univ UNESP, Dept Energy, Guaratingueta, SP, Brazil
dc.description.affiliationUniv Camaguey, Dept Mech Engn, Camaguey, Cuba
dc.description.affiliationUniv Sassari, Dept Chem, I-07100 Sassari, Italy
dc.description.affiliationUnespEnergy Department, São Paulo State University (UNESP), Guaratinguetá, SP, Brazil
dc.description.sponsorshipCoordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)
dc.description.sponsorshipConselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)
dc.description.sponsorshipIdCAPES: 5993105
dc.description.sponsorshipIdCNPq: 162633/2013-0
dc.format.extent478-483
dc.identifierhttp://www.sciencedirect.com/science/article/pii/S0960148115000038
dc.identifier.citationRenewable Energy. Oxford: Pergamon-elsevier Science Ltd, v. 78, p. 478-483, 2015.
dc.identifier.doi10.1016/j.renene.2014.12.069
dc.identifier.issn0960-1481
dc.identifier.lattes1750154267305530
dc.identifier.urihttp://hdl.handle.net/11449/129464
dc.identifier.wosWOS:000351646400052
dc.language.isoeng
dc.publisherElsevier B.V.
dc.relation.ispartofRenewable Energy
dc.relation.ispartofjcr4.900
dc.relation.ispartofsjr1,847
dc.rights.accessRightsAcesso restrito
dc.sourceWeb of Science
dc.subjectBiomassen
dc.subjectDowndraft gasifieren
dc.subjectGasificationen
dc.subjectTaren
dc.subjectSwirl flowen
dc.titleTar reduction in downdraft biomass gasifier using a primary methoden
dc.typeArtigo
dcterms.licensehttp://www.elsevier.com/about/open-access/open-access-policies/article-posting-policy
dcterms.rightsHolderElsevier B.V.
dspace.entity.typePublication
unesp.author.lattes1750154267305530
unesp.author.orcid0000-0002-8885-5614[7]
unesp.author.orcid0000-0002-5270-9041[2]
unesp.campusUniversidade Estadual Paulista (UNESP), Faculdade de Engenharia, Guaratinguetápt
unesp.departmentEnergia - FEGpt

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