Design of an absorption tower for a laboratory scale CO2 capture plant

dc.contributor.advisorBuiles Toro, Santiagospa
dc.contributor.authorHerrera Meneses, Michel Alejandra
dc.contributor.authorRomán Restrepo, Valeria
dc.coverage.spatialMedellín de: Lat: 06 15 00 N degrees minutes Lat: 6.2500 decimal degrees Long: 075 36 00 W degrees minutes Long: -75.6000 decimal degreeseng
dc.creator.degreeIngeniero de Procesosspa
dc.creator.emailmherre32@eafit.edu.cospa
dc.creator.emailvromanr@eafit.edu.cospa
dc.date.accessioned2021-08-03T21:11:56Z
dc.date.available2021-08-03T21:11:56Z
dc.date.issued2021
dc.description.abstractCarbon dioxide (CO2) is the main greenhouse gas in the earth’s atmosphere. The current concentration levels of CO2 in the atmosphere contribute to generate irreversible changes in the climate, sea level and the environment. Due to the highly industrialized economy, for today's society it will not be possible, in the mid-term, to stop these CO2 emissions without serious economic and social consequences. Therefore, it is necessary to implement several strategies to reduce CO2 emissions, for instance integrated CO2 capture systems that are efficient and economically viable. Strategies such as carbon capture and storage can used to reduce the impact of CO2 emissions on the global climate to an acceptable level. Reactive absorption with aqueous solutions of amines in an absorber/stripper loop is the most mature technology for CO2 capture from existing plants. Therefore, it is proposed to design an absorption tower at laboratory scale in stainless-steel due to its stability and resistance to corrosion for the capture of CO2 using monoethanolamine. This requires the assessment of the best model for describing an absorption tower at laboratory scale by comparing different models and simulations programs to determine the most appropriate one for design at laboratory scale. The model implemented in Python absorption tower design was chosen over the commercial simulators, resulting in a 10 mm Raschig ceramic ring packing, a CO2 removal rate of 80%, an internal diameter of 21.7 mm and a packing height of 400 mm.spa
dc.identifier.ddc660.28 H565
dc.identifier.urihttp://hdl.handle.net/10784/30073
dc.language.isospaspa
dc.publisherUniversidad EAFITspa
dc.publisher.departmentEscuela de Ingeniería. Departamento de Ingeniería Procesosspa
dc.publisher.placeMedellínspa
dc.publisher.programIngeniería de Procesosspa
dc.rightsTodos los derechos reservadosspa
dc.rights.accessrightsinfo:eu-repo/semantics/openAccessspa
dc.rights.localAcceso abiertospa
dc.subjectTorre de absorciónspa
dc.subjectCaptura de CO2 con MEAspa
dc.subjectIngeniería de procesosspa
dc.subjectMonoetanolaminaspa
dc.subject.keywordAbsorption towerspa
dc.subject.keywordCO2 capture with MEAspa
dc.subject.lembINGENIERÍA DE LA PRODUCCIÓNspa
dc.subject.lembDIÓXIDO DE CARBONO - PRUEBASspa
dc.subject.lembEFECTO INVERNADEROspa
dc.titleDesign of an absorption tower for a laboratory scale CO2 capture plantspa
dc.typebachelorThesiseng
dc.typeinfo:eu-repo/semantics/bachelorThesis
dc.type.hasVersionacceptedVersioneng
dc.type.localTrabajo de gradospa
dc.type.spaArtículospa

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