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Gas Adsorption Modelling of the Oxidative Coupling of Methane (OCM) Process on Zeolite X Molecular Sieves

dc.contributor.advisorOrjuela Londoño, Alvarospa
dc.contributor.advisorRodriguez Niño, Gerardospa
dc.contributor.authorRodriguez Paez, Cristian Camilospa
dc.contributor.researchgroupGrupo de Investigación en Procesos Químicos y Bioquímicosspa
dc.date.accessioned2020-02-20T20:58:11Zspa
dc.date.available2020-02-20T20:58:11Zspa
dc.date.issued2019spa
dc.description.abstractIn this work was studied the modeling of the adsorption of effluent gases from the methane oxidative coupling process (OCM) on CaX zeolite for the separation of ethylene. To describe the adsorption process, a mathematical model was implemented within the Aspen Adsorption software based on Mass, Energy and Momentum balances, and the Linear Driving Force adsorption rate model. The transport parameters were adjusted from dynamic experimental data in order to validate the proposed mathematical model, to be used in the design of a pressure swing adsorption system (PSA) on an industrial scale. The PSA system can be an alternative to cryogenic distillation for the separation of methane because the methane is not adsorbed on CaX zeolite, and also the zeolite CaX presents selectivity for ethane and ethylene. The ethylene purification process was carried out with cryogenic distillation columns. However, the substitution of the demethanizer unit with a PSA system resulted in an energy saving of 30% and a reduction in utility costs of 18% compared to the traditional cryogenic distillation process.spa
dc.description.abstractEn este trabajo se estudió el modelamiento de la adsorción de gases efluentes del proceso de acoplamiento oxidativo de metano (OCM) sobre zeolita CaX para la separación de etileno. Para describir el proceso de adsorción un modelo matemático fue implementado dentro del software Aspen Adsorption basado en los balances de Masa, Energía y Momentum, y el modelo de velocidad de adsorción de fuerza impulsora lineal. Los parámetros de transporte fueron ajustados a partir de datos experimentales dinámicos con el fin de validar el modelo matemático propuesto, para ser utilizado en el diseño de un sistema de adsorción por oscilación de presión (PSA) a escala industrial. El sistema de PSA puede ser una alternativa a la destilación criogénica para la separación de metano debido a que la zeolita CaX no adsorbe metano, y además presenta selectividad por el etano y etileno. El proceso de purificación de etileno se llevó a cabo con columnas de destilación criogénica. Sin embargo, al sustituir la unidad demetanizadora por un sistema PSA se presentó un ahorro de energía del 30% y una reducción de costos de utilidad del 18% en comparación con el proceso de destilación criogénica tradicionalspa
dc.description.additionalMagister en Ingeniería – Ingeniería Química. Línea de investigación: Modelamiento y Simulación.spa
dc.description.degreelevelMaestríaspa
dc.format.extent141spa
dc.format.mimetypeapplication/pdfspa
dc.identifier.urihttps://repositorio.unal.edu.co/handle/unal/75669
dc.language.isoengspa
dc.publisher.branchUniversidad Nacional de Colombia - Sede Bogotáspa
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dc.rightsDerechos reservados - Universidad Nacional de Colombiaspa
dc.rights.accessrightsinfo:eu-repo/semantics/openAccessspa
dc.rights.licenseAtribución-NoComercial-SinDerivadas 4.0 Internacionalspa
dc.rights.spaAcceso abiertospa
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/spa
dc.subject.ddcIngeniería químicaspa
dc.subject.proposalAdsorción por oscilación de presiónspa
dc.subject.proposalPressure swing adsorptioneng
dc.subject.proposalOxidative Coupling of Methaneeng
dc.subject.proposalOxidación acoplada de metanospa
dc.subject.proposalDestilación criogénicaspa
dc.subject.proposalCryogenic Distillationeng
dc.subject.proposalBreakthrough Curveeng
dc.subject.proposalCurva de rupturaspa
dc.subject.proposalEthylene Separationeng
dc.subject.proposalSeparación de etilenospa
dc.titleGas Adsorption Modelling of the Oxidative Coupling of Methane (OCM) Process on Zeolite X Molecular Sievesspa
dc.title.alternativeModelamiento de la adsorción de gases del proceso de Acoplamiento Oxidativo de Metano (OCM) sobre tamices moleculares de zeolita Xspa
dc.typeTrabajo de grado - Maestríaspa
dc.type.coarhttp://purl.org/coar/resource_type/c_bdccspa
dc.type.coarversionhttp://purl.org/coar/version/c_ab4af688f83e57aaspa
dc.type.contentTextspa
dc.type.driverinfo:eu-repo/semantics/masterThesisspa
dc.type.versioninfo:eu-repo/semantics/acceptedVersionspa
oaire.accessrightshttp://purl.org/coar/access_right/c_abf2spa

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