Please use this identifier to cite or link to this item: http://repositorio.ufpso.edu.co/jspui/handle/123456789/3489
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dc.contributor.authorQuintero Coronel, Daniel Andres-
dc.contributor.authorEspinel Blanco, Edwin Edgardo-
dc.contributor.authorFlórez Solano, Eder Norberto-
dc.date.accessioned2021-09-28T19:34:39Z-
dc.date.available2021-09-28T19:34:39Z-
dc.date.issued2020-
dc.identifier.citationQuintero-Coronel, DA, Espinel-Blanco, EE y Flórez-Solano, EN (2020). Desarrollo de un modelo de equilibrio químico del proceso de gasificación de lecho fijo de corriente descendente con temperatura de producto conocida, utilizando aire como agente oxidante. Ingenieria Y Universidad , 24 .en_US
dc.identifier.issn211-2769en_US
dc.identifier.urihttp://repositorio.ufpso.edu.co/jspui/handle/123456789/3489-
dc.description.abstractA chemical equilibrium model for known outlet temperature of the products was carried out on a downdraft fixed bed gasifier. Biomass from oil palm kernel is used with proximate and ultimate analysis; the general gasification reaction takes into account the biomass moisture, the reaction products are formed by CH4, H2O, N2, CO, CO2 and H2. The model is described in detail and the equations are solved using the EES software. The model shows the results obtained for temperature ranges from 500 K to 1500 K and 1.0 atm. The model is validated by direct comparison of the gas composition with the results reported in the literature for similar conditions, obtaining favorable results.en_US
dc.description.sponsorshipUniversidad Francisco de Paula Santander Ocaña, Colombia.en_US
dc.description.tableofcontentsspa
dc.format.mimetypespa
dc.language.isoengen_US
dc.publisherCarlos Barrenecheen_US
dc.relationhttps://revistas.javeriana.edu.co/index.php/en_US
dc.relation.ispartofseriesINGAP;ART37-
dc.relation.uri
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/2.5/co/*
dc.subjectequilibrio químico, energía de Gibbs, biomasa, gasificador de corriente descendente.en_US
dc.titleDevelopment of a Chemical Equilibrium Model of the Downdraft Fixed Bed Gasification Process with known Product Temperature, Using air as an Oxidizing Agenten_US
dc.typeArtículoen_US
dc.title.translatedDevelopment of a Chemical Equilibrium Model of the Downdraft Fixed Bed Gasification Process with known Product Temperature, Using air as an Oxidizing Agenten_US
dc.description.abstractenglishA chemical equilibrium model for known outlet temperature of the products was carried out on a downdraft fixed bed gasifier. Biomass from oil palm kernel is used with proximate and ultimate analysis; the general gasification reaction takes into account the biomass moisture, the reaction products are formed by CH4, H2O, N2, CO, CO2 and H2. The model is described in detail and the equations are solved using the EES software. The model shows the results obtained for temperature ranges from 500 K to 1500 K and 1.0 atm. The model is validated by direct comparison of the gas composition with the results reported in the literature for similar conditions, obtaining favorable results.en_US
dc.subject.proposaleng
dc.subject.keywordschemical equilibrium, Gibbs energy, biomass, downdraft gasifier Resumen.en_US
dc.subject.lembspa
dc.identifier.instnameinstname:Universidad Francisco de Paula Santander Ocañaspa
dc.identifier.reponamereponame:Repositorio Institucional UFPSOspa
dc.identifier.repourlrepourl:https://repositorio.ufpso.edu.cospa
dc.publisher.facultyFacultad ingenieríasen_US
dc.publisher.grantorUniversidad Francisco de Paula Santander Ocañaspa
dc.rights.accessrightsinfo:eu-repo/semantics/openAccessspa
dc.rights.accessrightshttp://purl.org/coar/access_right/c_abf2
dc.rights.creativecommonsAtribución-NoComercial-SinDerivadas 2.5 Colombia*
dc.rights.localspa
dc.type.coarhttp://purl.org/coar/resource_type/c_6501
dc.type.driverinfo:eu-repo/semantics/article
dc.type.localArtículoen_US
dc.type.redcolArtículo de investigación http://purl.org/redcol/resource_type/ART Artículo de divulgación http://purl.org/redcol/resource_type/ARTDIV*
dc.relation.referencesM. Bassyouni et al., “Date palm waste gasification in downdraft gasifier and simulation using ASPEN HYSYS,” vol. 88, pp. 693–699, 2014.en_US
dc.relation.referencesG. García, “Estudio experimental de la cogasificación de fangos de EDAR y carbón con aire en lecho fluidizado,” tesis, Universidad de Zaragoza, España, 2013.en_US
dc.relation.referencesS. Jarungthammachote and A. Dutta, “Thermodynamic equilibrium model and second law analysis of a downdraft waste gasifier,” Energy, vol. 32, no. 9, pp. 1660–1669, 2007.en_US
dc.relation.referencesA. Melgar, J.F. Pérez, H. Laget, and A. Horillo, “Thermochemical equilibrium modelling of a gasifying process,” Energ. Convers. Manage., vol. 48, no. 1, pp. 59–67, 2007.en_US
dc.relation.referencesT.H. Jayah, L. Aye, R.J. Fuller, and D.F. Stewart, “Computer simulation of a downdraft wood gasifier for tea drying,” Biomass Bioenergy, vol. 25, no. 4, pp. 459–469, 2003.en_US
dc.relation.referencesA. Khadse, P. Parulekar, P. Aghalayam, and A. Ganesh, “Equilibrium model for biomass gasification.” Proceedings of the 1st National Conference on Advances in Energy Research (AER-2006), December 4-5, 2006-ISBN 9780230630062.en_US
dc.relation.referencesA.Z. Mendiburu, J.A. Carvalho, R. Zanzi, C.R. Coronado, and J.L. Silveira, “Thermochemical equilibrium modeling of a biomass downdraft gasifier: Constrained and unconstrained non-stoichiometric models,” Energy, vol. 71, pp. 624–637, 2014.en_US
dc.type.hasversioninfo:eu-repo/semantics/acceptedVersion
dc.identifier.DOI10.11144/Javeriana.iyu24.dcemen_US
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