Carbon dioxide capture by [emim][Ac] ionic liquid in a polysulfone hollow fiber membrane contactor
CO2 emissions have to be controlled and reduced in order to avoid greenhouse effect. This work reports an analysis of the efficiency of CO2 separation using a hollow fiber membrane contactor and an ionic liquid. This process configuration contributes to the process intensification approach in the fi...
| Autores: | , , |
|---|---|
| Tipo de documento: | artigo |
| Data de publicação: | 2016 |
| País: | España |
| Recursos: | Universidad de Cantabria (UC) |
| Repositório: | UCrea Repositorio Abierto de la Universidad de Cantabria |
| Idioma: | inglês |
| OAI Identifier: | oai:repositorio.unican.es:10902/11166 |
| Acesso em linha: | http://hdl.handle.net/10902/11166 |
| Access Level: | Acceso aberto |
| Palavra-chave: | Carbon dioxide capture Hollow fiber membrane contactor Polysulfone [emim][Ac] ionic liquid |
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oai:repositorio.unican.es:10902/11166 |
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Carbon dioxide capture by [emim][Ac] ionic liquid in a polysulfone hollow fiber membrane contactorGómez Coma, Lucía|||0000-0001-7586-6552Garea Vázquez, Aurora|||0000-0002-6356-4298Irabien Gulías, Ángel|||0000-0002-2411-4163Carbon dioxide captureHollow fiber membrane contactorPolysulfone[emim][Ac] ionic liquidCO2 emissions have to be controlled and reduced in order to avoid greenhouse effect. This work reports an analysis of the efficiency of CO2 separation using a hollow fiber membrane contactor and an ionic liquid. This process configuration contributes to the process intensification approach in the field of CO2 capture and storage. In this study, the ionic liquid 1-ethyl-3-methylimidazolium acetate, [emim][Ac], was used as absorbent due to its high CO2 solubility. The module selected was polysulfone (Ps) because it is a well characterized polymer that allows to operate at moderate temperatures. Results were compared to previous studies with a polypropylene module. The gas stream flowed through the inside of the hollow fibers. The CO2 removal efficiency was obtained from experimental data, showing a temperature dependence: from 30 to 45.0%, corresponding to 291 K and 348 K respectively, when the Ps contactor was used. The overall mass transfer coefficient Koverall has also been evaluated. In addition, a numerical analysis was carried out to study the performance of the membrane contactor for the CO2 capture in order to estimate the process conditions to accomplish 90% CO2 capture as a target to be competitive with the conventional absorption process.This research has been funded by the Spanish Ministry Economy and Competitiveness (Project CTQ2013-48280-C3-1-R).ElsevierUniversidad de Cantabria20162016-09-01journal articlehttp://purl.org/coar/resource_type/c_6501NAhttp://purl.org/coar/version/c_be7fb7dd8ff6fe43info:eu-repo/semantics/articlehttp://hdl.handle.net/10902/11166International Journal of Greenhouse Gas Control, 2016, 52, 401–409reponame:UCrea Repositorio Abierto de la Universidad de Cantabriainstname:Universidad de Cantabria (UC)Inglésengopen accesshttp://purl.org/coar/access_right/c_abf2Atribución-NoComercial-SinDerivadas 3.0 Españahttp://creativecommons.org/licenses/by-nc-nd/3.0/es/info:eu-repo/semantics/openAccessoai:repositorio.unican.es:10902/111662026-06-02T12:39:31Z |
| dc.title.none.fl_str_mv |
Carbon dioxide capture by [emim][Ac] ionic liquid in a polysulfone hollow fiber membrane contactor |
| title |
Carbon dioxide capture by [emim][Ac] ionic liquid in a polysulfone hollow fiber membrane contactor |
| spellingShingle |
Carbon dioxide capture by [emim][Ac] ionic liquid in a polysulfone hollow fiber membrane contactor Gómez Coma, Lucía|||0000-0001-7586-6552 Carbon dioxide capture Hollow fiber membrane contactor Polysulfone [emim][Ac] ionic liquid |
| title_short |
Carbon dioxide capture by [emim][Ac] ionic liquid in a polysulfone hollow fiber membrane contactor |
| title_full |
Carbon dioxide capture by [emim][Ac] ionic liquid in a polysulfone hollow fiber membrane contactor |
| title_fullStr |
Carbon dioxide capture by [emim][Ac] ionic liquid in a polysulfone hollow fiber membrane contactor |
| title_full_unstemmed |
Carbon dioxide capture by [emim][Ac] ionic liquid in a polysulfone hollow fiber membrane contactor |
| title_sort |
Carbon dioxide capture by [emim][Ac] ionic liquid in a polysulfone hollow fiber membrane contactor |
| dc.creator.none.fl_str_mv |
Gómez Coma, Lucía|||0000-0001-7586-6552 Garea Vázquez, Aurora|||0000-0002-6356-4298 Irabien Gulías, Ángel|||0000-0002-2411-4163 |
| author |
Gómez Coma, Lucía|||0000-0001-7586-6552 |
| author_facet |
Gómez Coma, Lucía|||0000-0001-7586-6552 Garea Vázquez, Aurora|||0000-0002-6356-4298 Irabien Gulías, Ángel|||0000-0002-2411-4163 |
| author_role |
author |
| author2 |
Garea Vázquez, Aurora|||0000-0002-6356-4298 Irabien Gulías, Ángel|||0000-0002-2411-4163 |
| author2_role |
author author |
| dc.contributor.none.fl_str_mv |
Universidad de Cantabria |
| dc.subject.none.fl_str_mv |
Carbon dioxide capture Hollow fiber membrane contactor Polysulfone [emim][Ac] ionic liquid |
| topic |
Carbon dioxide capture Hollow fiber membrane contactor Polysulfone [emim][Ac] ionic liquid |
| description |
CO2 emissions have to be controlled and reduced in order to avoid greenhouse effect. This work reports an analysis of the efficiency of CO2 separation using a hollow fiber membrane contactor and an ionic liquid. This process configuration contributes to the process intensification approach in the field of CO2 capture and storage. In this study, the ionic liquid 1-ethyl-3-methylimidazolium acetate, [emim][Ac], was used as absorbent due to its high CO2 solubility. The module selected was polysulfone (Ps) because it is a well characterized polymer that allows to operate at moderate temperatures. Results were compared to previous studies with a polypropylene module. The gas stream flowed through the inside of the hollow fibers. The CO2 removal efficiency was obtained from experimental data, showing a temperature dependence: from 30 to 45.0%, corresponding to 291 K and 348 K respectively, when the Ps contactor was used. The overall mass transfer coefficient Koverall has also been evaluated. In addition, a numerical analysis was carried out to study the performance of the membrane contactor for the CO2 capture in order to estimate the process conditions to accomplish 90% CO2 capture as a target to be competitive with the conventional absorption process. |
| publishDate |
2016 |
| dc.date.none.fl_str_mv |
2016 2016-09-01 |
| dc.type.none.fl_str_mv |
journal article http://purl.org/coar/resource_type/c_6501 NA http://purl.org/coar/version/c_be7fb7dd8ff6fe43 |
| dc.type.openaire.fl_str_mv |
info:eu-repo/semantics/article |
| format |
article |
| dc.identifier.none.fl_str_mv |
http://hdl.handle.net/10902/11166 |
| url |
http://hdl.handle.net/10902/11166 |
| dc.language.none.fl_str_mv |
Inglés eng |
| language_invalid_str_mv |
Inglés |
| language |
eng |
| dc.rights.none.fl_str_mv |
open access http://purl.org/coar/access_right/c_abf2 Atribución-NoComercial-SinDerivadas 3.0 España http://creativecommons.org/licenses/by-nc-nd/3.0/es/ |
| dc.rights.openaire.fl_str_mv |
info:eu-repo/semantics/openAccess |
| rights_invalid_str_mv |
open access http://purl.org/coar/access_right/c_abf2 Atribución-NoComercial-SinDerivadas 3.0 España http://creativecommons.org/licenses/by-nc-nd/3.0/es/ |
| eu_rights_str_mv |
openAccess |
| dc.publisher.none.fl_str_mv |
Elsevier |
| publisher.none.fl_str_mv |
Elsevier |
| dc.source.none.fl_str_mv |
International Journal of Greenhouse Gas Control, 2016, 52, 401–409 reponame:UCrea Repositorio Abierto de la Universidad de Cantabria instname:Universidad de Cantabria (UC) |
| instname_str |
Universidad de Cantabria (UC) |
| reponame_str |
UCrea Repositorio Abierto de la Universidad de Cantabria |
| collection |
UCrea Repositorio Abierto de la Universidad de Cantabria |
| repository.name.fl_str_mv |
|
| repository.mail.fl_str_mv |
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1869416847180300288 |
| score |
15.301629 |