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dc.contributor.authorQuintero Coronel, Daniel Andrés
dc.contributor.authorEspinel Blanco, Edwin
dc.contributor.authorFlorez Solano, Eder
dc.coverage.spatialColombiaen_US
dc.date.accessioned2025-10-30T14:33:18Z
dc.date.available2025-10-30T14:33:18Z
dc.date.issued2020-02-24
dc.identifier.issn0123-2126en_US
dc.identifier.urihttps://repositorioinstitucional.ufpso.edu.co/xmlui/handle/20.500.14167/5997
dc.description.abstractSe llevó a cabo un modelo en equilibrio químico para temperatura de salida de productos conocida en un gasificador de lecho fijo de corriente descendente. Se utiliza biomasa de cuesco de palma de aceite con análisis elemental y próximo conocido. La reacción general de gasificación tiene en cuenta la humedad de la biomasa, los productos de la reacción están formados por CH4, H2O, N2, CO, CO2 y H2. Se describe detalladamente cómo se realiza el modelo, las ecuaciones son resueltas mediante el software EES. El modelo muestra los resultados obtenidos para rangos de temperatura de 500 K a 1500 K y 1.0 atm de presión. El modelo se validó mediante comparación directa de la composición de los gases con los resultados reportados en la literatura para condiciones similares, y así se obtuvieron resultados favorables.en_US
dc.language.isoengen_US
dc.relationhttps://revistas.javeriana.edu.co/index.php/iyu/article/view/25566en_US
dc.titleDesarrollo de un modelo de equilibrio químico del proceso de gasificación en un lecho fijo de corrientes descendentes con temperatura conocida del producto, utilizando el aire como agente oxidanteen_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 Agent*en_US
dc.contributor.cvlacDaniel Andrés Quintero Coronel [0001638401]en_US
dc.contributor.cvlacEdwin Espinel Blanco [0001200917]en_US
dc.contributor.cvlacEder Florez Solano [0000668125]en_US
dc.contributor.googlescholarDaniel Andrés Quintero Coronel [4GlB1YIAAAAJ]en_US
dc.contributor.googlescholarEdwin Espinel Blanco [3ODKG4cAAAAJ]en_US
dc.contributor.googlescholarEder Florez Solano [kjgjoYkAAAAJ]en_US
dc.contributor.orcidEdwin Espinel Blanco [0000-0003-4479-2874]en_US
dc.contributor.orcidEder Florez Solano [0000-0003-2527-0413]en_US
dc.contributor.researchgateEder Florez Solano [Norberto-Florez-Solano]en_US
dc.contributor.scopusEdwin Espinel Blanco [57209774810]en_US
dc.contributor.scopusEder Norberto Florez Solano [57200310518]en_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.proposalequilibrio químicoen_US
dc.subject.proposalenergía de Gibbsen_US
dc.subject.proposalbiomasaen_US
dc.subject.proposalgasificador de corriente descendenteen_US
dc.subject.keywordschemical equilibriumen_US
dc.subject.keywordsGibbs energyen_US
dc.subject.keywordsbiomassen_US
dc.subject.keywordsdowndraft gasifieren_US
dc.publisher.facultyFacultad ingenieríasen_US
dc.type.redcolhttp://purl.org/redcol/resource_type/ARTen_US
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dc.identifier.DOIhttps://doi.org/10.11144/Javeriana.iyu24.dcemen_US


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