Design of an absorption tower for a laboratory scale CO2 capture plant
Carbon 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 n...
- Autores:
-
Herrera Meneses, Michel Alejandra
Román Restrepo, Valeria
- Tipo de recurso:
- Fecha de publicación:
- 2021
- Institución:
- Universidad EAFIT
- Repositorio:
- Repositorio EAFIT
- Idioma:
- spa
- OAI Identifier:
- oai:repository.eafit.edu.co:10784/30073
- Acceso en línea:
- http://hdl.handle.net/10784/30073
- Palabra clave:
- Torre de absorción
Captura de CO2 con MEA
Ingeniería de procesos
Monoetanolamina
INGENIERÍA DE LA PRODUCCIÓN
DIÓXIDO DE CARBONO - PRUEBAS
EFECTO INVERNADERO
Absorption tower
CO2 capture with MEA
- Rights
- License
- Todos los derechos reservados
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Builes Toro, SantiagoHerrera Meneses, Michel AlejandraRomán Restrepo, ValeriaIngeniero de Procesosmherre32@eafit.edu.covromanr@eafit.edu.coMedellín de: Lat: 06 15 00 N degrees minutes Lat: 6.2500 decimal degrees Long: 075 36 00 W degrees minutes Long: -75.6000 decimal degrees2021-08-03T21:11:56Z20212021-08-03T21:11:56Zhttp://hdl.handle.net/10784/30073660.28 H565Carbon 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.spaUniversidad EAFITIngeniería de ProcesosEscuela de Ingeniería. Departamento de Ingeniería ProcesosMedellínTodos los derechos reservadosAcceso abiertohttp://purl.org/coar/access_right/c_abf2Torre de absorciónCaptura de CO2 con MEAIngeniería de procesosMonoetanolaminaINGENIERÍA DE LA PRODUCCIÓNDIÓXIDO DE CARBONO - PRUEBASEFECTO INVERNADEROAbsorption towerCO2 capture with MEADesign of an absorption tower for a laboratory scale CO2 capture plantbachelorThesisinfo:eu-repo/semantics/bachelorThesisTrabajo de gradoacceptedVersionArtículohttp://purl.org/coar/resource_type/c_7a1fORIGINALValeria_RomanRestrepo_MichelAlejandra_HerreraMeneses_2021.pdfValeria_RomanRestrepo_MichelAlejandra_HerreraMeneses_2021.pdfTrabajo de gradoapplication/pdf1434878https://repository.eafit.edu.co/bitstreams/26f4f8d2-7141-4f8e-82b8-4cee11ae4e92/download8d2e6ac35061d201927cc3c23290c867MD52carta_aprobacion_trabajo_grado_eafit.pdf.pdfcarta_aprobacion_trabajo_grado_eafit.pdf.pdfCarta de aprobación de tesis de gradoapplication/pdf109788https://repository.eafit.edu.co/bitstreams/25c9f735-acfc-4e55-851c-5023c0aca01f/downloadb2e94939016b4b2b852df7fc5bba95f5MD53formulario_autorizacion_publicacion_obras.pdf.pdfformulario_autorizacion_publicacion_obras.pdf.pdfFormulario de autorización de publicación de obrasapplication/pdf630827https://repository.eafit.edu.co/bitstreams/3ba20315-c0cf-4d88-b2f3-af4673c2f232/download7b8aa30cf4625e36f7e38686f068922aMD54LICENSElicense.txtlicense.txttext/plain; charset=utf-82556https://repository.eafit.edu.co/bitstreams/9e2f7bf1-0c64-4202-bbe8-a4878f5362d7/download76025f86b095439b7ac65b367055d40cMD51LICENSElicense.txtlicense.txttext/plain; charset=utf-82556https://repository.eafit.edu.co/bitstreams/0c3b8092-f785-47ec-9fc0-d9bad3e000d5/download76025f86b095439b7ac65b367055d40cMD5110784/30073oai:repository.eafit.edu.co:10784/300732021-08-03 16:11:56.129open.accesshttps://repository.eafit.edu.coRepositorio Institucional Universidad EAFITrepositorio@eafit.edu.co |
dc.title.spa.fl_str_mv |
Design of an absorption tower for a laboratory scale CO2 capture plant |
title |
Design of an absorption tower for a laboratory scale CO2 capture plant |
spellingShingle |
Design of an absorption tower for a laboratory scale CO2 capture plant Torre de absorción Captura de CO2 con MEA Ingeniería de procesos Monoetanolamina INGENIERÍA DE LA PRODUCCIÓN DIÓXIDO DE CARBONO - PRUEBAS EFECTO INVERNADERO Absorption tower CO2 capture with MEA |
title_short |
Design of an absorption tower for a laboratory scale CO2 capture plant |
title_full |
Design of an absorption tower for a laboratory scale CO2 capture plant |
title_fullStr |
Design of an absorption tower for a laboratory scale CO2 capture plant |
title_full_unstemmed |
Design of an absorption tower for a laboratory scale CO2 capture plant |
title_sort |
Design of an absorption tower for a laboratory scale CO2 capture plant |
dc.creator.fl_str_mv |
Herrera Meneses, Michel Alejandra Román Restrepo, Valeria |
dc.contributor.advisor.spa.fl_str_mv |
Builes Toro, Santiago |
dc.contributor.author.none.fl_str_mv |
Herrera Meneses, Michel Alejandra Román Restrepo, Valeria |
dc.subject.spa.fl_str_mv |
Torre de absorción Captura de CO2 con MEA Ingeniería de procesos Monoetanolamina |
topic |
Torre de absorción Captura de CO2 con MEA Ingeniería de procesos Monoetanolamina INGENIERÍA DE LA PRODUCCIÓN DIÓXIDO DE CARBONO - PRUEBAS EFECTO INVERNADERO Absorption tower CO2 capture with MEA |
dc.subject.lemb.spa.fl_str_mv |
INGENIERÍA DE LA PRODUCCIÓN DIÓXIDO DE CARBONO - PRUEBAS EFECTO INVERNADERO |
dc.subject.keyword.spa.fl_str_mv |
Absorption tower CO2 capture with MEA |
description |
Carbon 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. |
publishDate |
2021 |
dc.date.available.none.fl_str_mv |
2021-08-03T21:11:56Z |
dc.date.issued.none.fl_str_mv |
2021 |
dc.date.accessioned.none.fl_str_mv |
2021-08-03T21:11:56Z |
dc.type.eng.fl_str_mv |
bachelorThesis |
dc.type.none.fl_str_mv |
info:eu-repo/semantics/bachelorThesis |
dc.type.coar.fl_str_mv |
http://purl.org/coar/resource_type/c_7a1f |
dc.type.local.spa.fl_str_mv |
Trabajo de grado |
dc.type.hasVersion.eng.fl_str_mv |
acceptedVersion |
dc.type.spa.spa.fl_str_mv |
Artículo |
dc.identifier.uri.none.fl_str_mv |
http://hdl.handle.net/10784/30073 |
dc.identifier.ddc.none.fl_str_mv |
660.28 H565 |
url |
http://hdl.handle.net/10784/30073 |
identifier_str_mv |
660.28 H565 |
dc.language.iso.spa.fl_str_mv |
spa |
language |
spa |
dc.rights.spa.fl_str_mv |
Todos los derechos reservados |
dc.rights.coar.fl_str_mv |
http://purl.org/coar/access_right/c_abf2 |
dc.rights.local.spa.fl_str_mv |
Acceso abierto |
rights_invalid_str_mv |
Todos los derechos reservados Acceso abierto http://purl.org/coar/access_right/c_abf2 |
dc.coverage.spatial.eng.fl_str_mv |
Medellín de: Lat: 06 15 00 N degrees minutes Lat: 6.2500 decimal degrees Long: 075 36 00 W degrees minutes Long: -75.6000 decimal degrees |
dc.publisher.spa.fl_str_mv |
Universidad EAFIT |
dc.publisher.program.spa.fl_str_mv |
Ingeniería de Procesos |
dc.publisher.department.spa.fl_str_mv |
Escuela de Ingeniería. Departamento de Ingeniería Procesos |
dc.publisher.place.spa.fl_str_mv |
Medellín |
institution |
Universidad EAFIT |
bitstream.url.fl_str_mv |
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1814110274849865728 |