Gas phase synthesis of dimethyl carbonate from CO2 and CH3OH over Cu-Ni/AC. A kinetic study
ABSTRACT : The catalytic activity for dimethyl carbonate formation from carbon dioxide and methanol over mono and bimetallic Cu:Ni supported on activated carbon is presented. Bimetallic catalysts exhibit higher catalytic activity than the monometallic samples, being Cu:Ni-2:1 (molar ratio) the best...
- Autores:
-
Arbeláez Pérez, Oscar Felipe
Domínguez Cardozo, Sara
Orrego Romero, Andrés Felipe
Villa Holguín, Aida Luz
Bustamante Londoño, Felipe
- Tipo de recurso:
- Article of investigation
- Fecha de publicación:
- 2020
- Institución:
- Universidad de Antioquia
- Repositorio:
- Repositorio UdeA
- Idioma:
- eng
- OAI Identifier:
- oai:bibliotecadigital.udea.edu.co:10495/24959
- Acceso en línea:
- http://hdl.handle.net/10495/24959
https://revistas.udea.edu.co/index.php/ingenieria/article/view/338344
- Palabra clave:
- Metanol
Methanol
Catalizador
Catalysts
Dióxido de carbono
Carbon dioxide
Mecanismo de reacción
Velocidad de reacción
http://aims.fao.org/aos/agrovoc/c_12521
http://aims.fao.org/aos/agrovoc/c_27480
http://aims.fao.org/aos/agrovoc/c_1302
- Rights
- openAccess
- License
- http://creativecommons.org/licenses/by-nc-sa/2.5/co/
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dc.title.spa.fl_str_mv |
Gas phase synthesis of dimethyl carbonate from CO2 and CH3OH over Cu-Ni/AC. A kinetic study |
dc.title.alternative.spa.fl_str_mv |
Síntesis en fase gaseosa de dimetil carbonato con CO2 y CH3OH sobre Cu-Ni/AC. Estudio cinético |
title |
Gas phase synthesis of dimethyl carbonate from CO2 and CH3OH over Cu-Ni/AC. A kinetic study |
spellingShingle |
Gas phase synthesis of dimethyl carbonate from CO2 and CH3OH over Cu-Ni/AC. A kinetic study Metanol Methanol Catalizador Catalysts Dióxido de carbono Carbon dioxide Mecanismo de reacción Velocidad de reacción http://aims.fao.org/aos/agrovoc/c_12521 http://aims.fao.org/aos/agrovoc/c_27480 http://aims.fao.org/aos/agrovoc/c_1302 |
title_short |
Gas phase synthesis of dimethyl carbonate from CO2 and CH3OH over Cu-Ni/AC. A kinetic study |
title_full |
Gas phase synthesis of dimethyl carbonate from CO2 and CH3OH over Cu-Ni/AC. A kinetic study |
title_fullStr |
Gas phase synthesis of dimethyl carbonate from CO2 and CH3OH over Cu-Ni/AC. A kinetic study |
title_full_unstemmed |
Gas phase synthesis of dimethyl carbonate from CO2 and CH3OH over Cu-Ni/AC. A kinetic study |
title_sort |
Gas phase synthesis of dimethyl carbonate from CO2 and CH3OH over Cu-Ni/AC. A kinetic study |
dc.creator.fl_str_mv |
Arbeláez Pérez, Oscar Felipe Domínguez Cardozo, Sara Orrego Romero, Andrés Felipe Villa Holguín, Aida Luz Bustamante Londoño, Felipe |
dc.contributor.author.none.fl_str_mv |
Arbeláez Pérez, Oscar Felipe Domínguez Cardozo, Sara Orrego Romero, Andrés Felipe Villa Holguín, Aida Luz Bustamante Londoño, Felipe |
dc.subject.agrovoc.none.fl_str_mv |
Metanol Methanol Catalizador Catalysts Dióxido de carbono Carbon dioxide |
topic |
Metanol Methanol Catalizador Catalysts Dióxido de carbono Carbon dioxide Mecanismo de reacción Velocidad de reacción http://aims.fao.org/aos/agrovoc/c_12521 http://aims.fao.org/aos/agrovoc/c_27480 http://aims.fao.org/aos/agrovoc/c_1302 |
dc.subject.proposal.spa.fl_str_mv |
Mecanismo de reacción Velocidad de reacción |
dc.subject.agrovocuri.none.fl_str_mv |
http://aims.fao.org/aos/agrovoc/c_12521 http://aims.fao.org/aos/agrovoc/c_27480 http://aims.fao.org/aos/agrovoc/c_1302 |
description |
ABSTRACT : The catalytic activity for dimethyl carbonate formation from carbon dioxide and methanol over mono and bimetallic Cu:Ni supported on activated carbon is presented. Bimetallic catalysts exhibit higher catalytic activity than the monometallic samples, being Cu:Ni-2:1 (molar ratio) the best catalyst; X-Ray diffraction, transmission electron microscopy, and metal dispersion analysis provided insight into the improved activity. In situ FT-IR experiments were conducted to investigate the mechanism of formation of dimethyl carbonate from methanol and carbon dioxide over Cu-Ni:2-1. The kinetics of the direct synthesis of dimethyl carbonate in gas phase over Cu:Ni-2:1 supported on activated carbon catalyst was experimentally investigated at 12 bar and temperatures between 90 oC and 130 oC, varying the partial pressures of CO2 and methanol. Experimental kinetic data were consistent with a Langmuir–Hinshelwood model that included carbon dioxide and methanol adsorption on catalyst actives sites (Cu, Ni and Cu-Ni), and the reaction of adsorbed CO2 with methoxi species as the rate determining step. The estimated apparent activation energy was 94.2 kJ mol-1. |
publishDate |
2020 |
dc.date.issued.none.fl_str_mv |
2020 |
dc.date.accessioned.none.fl_str_mv |
2021-12-10T21:18:23Z |
dc.date.available.none.fl_str_mv |
2021-12-10T21:18:23Z |
dc.type.spa.fl_str_mv |
info:eu-repo/semantics/article |
dc.type.coarversion.fl_str_mv |
http://purl.org/coar/version/c_970fb48d4fbd8a85 |
dc.type.hasversion.spa.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
dc.type.coar.spa.fl_str_mv |
http://purl.org/coar/resource_type/c_2df8fbb1 |
dc.type.redcol.spa.fl_str_mv |
https://purl.org/redcol/resource_type/ART |
dc.type.local.spa.fl_str_mv |
Artículo de investigación |
format |
http://purl.org/coar/resource_type/c_2df8fbb1 |
status_str |
publishedVersion |
dc.identifier.citation.spa.fl_str_mv |
Arbeláez-Pérez O. F., Domínguez-Cardozo S., Orrego-Romero A. F., Villa-Holguín A. L., and Bustamante-Londoño F., “Gas phase synthesis of dimethyl carbonate from CO2 and CH3OH over Cu-Ni/AC. A kinetic study”, Rev.Fac.Ing.Univ.Antioquia, no. 95, pp. 88-99, Dec. 2020. |
dc.identifier.issn.none.fl_str_mv |
0120-6230 |
dc.identifier.uri.none.fl_str_mv |
http://hdl.handle.net/10495/24959 |
dc.identifier.doi.none.fl_str_mv |
10.17533/udea.redin.20190941 |
dc.identifier.eissn.none.fl_str_mv |
2422-2844 |
dc.identifier.url.spa.fl_str_mv |
https://revistas.udea.edu.co/index.php/ingenieria/article/view/338344 |
identifier_str_mv |
Arbeláez-Pérez O. F., Domínguez-Cardozo S., Orrego-Romero A. F., Villa-Holguín A. L., and Bustamante-Londoño F., “Gas phase synthesis of dimethyl carbonate from CO2 and CH3OH over Cu-Ni/AC. A kinetic study”, Rev.Fac.Ing.Univ.Antioquia, no. 95, pp. 88-99, Dec. 2020. 0120-6230 10.17533/udea.redin.20190941 2422-2844 |
url |
http://hdl.handle.net/10495/24959 https://revistas.udea.edu.co/index.php/ingenieria/article/view/338344 |
dc.language.iso.spa.fl_str_mv |
eng |
language |
eng |
dc.relation.ispartofjournalabbrev.spa.fl_str_mv |
Rev. Fac. Ing. Univ. Antioquia |
dc.rights.spa.fl_str_mv |
info:eu-repo/semantics/openAccess |
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http://creativecommons.org/licenses/by-nc-sa/2.5/co/ |
dc.rights.accessrights.spa.fl_str_mv |
http://purl.org/coar/access_right/c_abf2 |
dc.rights.creativecommons.spa.fl_str_mv |
https://creativecommons.org/licenses/by-nc-sa/4.0/ |
eu_rights_str_mv |
openAccess |
rights_invalid_str_mv |
http://creativecommons.org/licenses/by-nc-sa/2.5/co/ http://purl.org/coar/access_right/c_abf2 https://creativecommons.org/licenses/by-nc-sa/4.0/ |
dc.format.extent.spa.fl_str_mv |
12 |
dc.format.mimetype.spa.fl_str_mv |
application/pdf |
dc.publisher.spa.fl_str_mv |
Universidad de Antioquia, Facultad de Ingeniería |
dc.publisher.group.spa.fl_str_mv |
Catálisis Ambiental |
dc.publisher.place.spa.fl_str_mv |
Medellín, Colombia |
institution |
Universidad de Antioquia |
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Repositorio Institucional Universidad de Antioquia |
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spelling |
Arbeláez Pérez, Oscar FelipeDomínguez Cardozo, SaraOrrego Romero, Andrés FelipeVilla Holguín, Aida LuzBustamante Londoño, Felipe2021-12-10T21:18:23Z2021-12-10T21:18:23Z2020Arbeláez-Pérez O. F., Domínguez-Cardozo S., Orrego-Romero A. F., Villa-Holguín A. L., and Bustamante-Londoño F., “Gas phase synthesis of dimethyl carbonate from CO2 and CH3OH over Cu-Ni/AC. A kinetic study”, Rev.Fac.Ing.Univ.Antioquia, no. 95, pp. 88-99, Dec. 2020.0120-6230http://hdl.handle.net/10495/2495910.17533/udea.redin.201909412422-2844https://revistas.udea.edu.co/index.php/ingenieria/article/view/338344ABSTRACT : The catalytic activity for dimethyl carbonate formation from carbon dioxide and methanol over mono and bimetallic Cu:Ni supported on activated carbon is presented. Bimetallic catalysts exhibit higher catalytic activity than the monometallic samples, being Cu:Ni-2:1 (molar ratio) the best catalyst; X-Ray diffraction, transmission electron microscopy, and metal dispersion analysis provided insight into the improved activity. In situ FT-IR experiments were conducted to investigate the mechanism of formation of dimethyl carbonate from methanol and carbon dioxide over Cu-Ni:2-1. The kinetics of the direct synthesis of dimethyl carbonate in gas phase over Cu:Ni-2:1 supported on activated carbon catalyst was experimentally investigated at 12 bar and temperatures between 90 oC and 130 oC, varying the partial pressures of CO2 and methanol. Experimental kinetic data were consistent with a Langmuir–Hinshelwood model that included carbon dioxide and methanol adsorption on catalyst actives sites (Cu, Ni and Cu-Ni), and the reaction of adsorbed CO2 with methoxi species as the rate determining step. The estimated apparent activation energy was 94.2 kJ mol-1.RESUMEN : Se reporta la actividad catalítica en la formación de dimetil carbonato a partir de dióxido de carbono y metanol sobre catalizadores mono y bimetálicos de Cu-Ni soportado en carbón activado. Los catalizadores bimetálicos presentaron una mayor actividad catalítica que los monometálicos, siendo la muestra Cu:Ni-2:1 el mejor catalizador. La caracterización de los materiales mediante análisis de difracción de rayos X, microscopía electrónica de transmisión y dispersión metálica permitieron sugerir una explicación al porqué de su mejor desempeño. Se realizaron experimentos de FT-IR in situ para investigar el mecanismo de formación de carbonato de dimetilo a partir de metanol y dióxido de carbono sobre Cu-Ni:2-1. Se estudió la cinética de la síntesis directa de dimetil carbonato en fase gaseosa sobre Cu:Ni-2:1 soportado en carbón activado, a 12 bar y temperaturas entre 90 oC y 130 oC, como función de la presión parcial del dióxido de carbono y del metanol. Los datos experimentales fueron consistentes con un mecanismo Langmuir-Hinshelwood, el cual incluyó la adsorción de dióxido de carbono y metanol sobre los sitios activos del catalizador (Cu, Ni, y Cu-Ni), siendo la reacción del dióxido de carbono adsorbido con las especies metoxi como etapa limitante. La energía de activación aparente estimada de la reacción fue 94,2 kJ mol-1.COL000194112application/pdfengUniversidad de Antioquia, Facultad de IngenieríaCatálisis AmbientalMedellín, Colombiainfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articlehttp://purl.org/coar/resource_type/c_2df8fbb1https://purl.org/redcol/resource_type/ARTArtículo de investigaciónhttp://purl.org/coar/version/c_970fb48d4fbd8a85info:eu-repo/semantics/openAccesshttp://creativecommons.org/licenses/by-nc-sa/2.5/co/http://purl.org/coar/access_right/c_abf2https://creativecommons.org/licenses/by-nc-sa/4.0/Gas phase synthesis of dimethyl carbonate from CO2 and CH3OH over Cu-Ni/AC. A kinetic studySíntesis en fase gaseosa de dimetil carbonato con CO2 y CH3OH sobre Cu-Ni/AC. Estudio cinéticoMetanolMethanolCatalizadorCatalystsDióxido de carbonoCarbon dioxideMecanismo de reacciónVelocidad de reacciónhttp://aims.fao.org/aos/agrovoc/c_12521http://aims.fao.org/aos/agrovoc/c_27480http://aims.fao.org/aos/agrovoc/c_1302Rev. Fac. Ing. Univ. AntioquiaRevista Facultad de Ingeniería Universidad de Antioquia889995CC-LICENSElicense_rdflicense_rdfapplication/rdf+xml; charset=utf-81051http://bibliotecadigital.udea.edu.co/bitstream/10495/24959/2/license_rdfe2060682c9c70d4d30c83c51448f4eedMD52ORIGINALArbelaezOscar_2020_GasPhaseSynthesis.pdfArbelaezOscar_2020_GasPhaseSynthesis.pdfArtículo de investigaciónapplication/pdf380266http://bibliotecadigital.udea.edu.co/bitstream/10495/24959/1/ArbelaezOscar_2020_GasPhaseSynthesis.pdf688474876b4233d73d012be267e0c41cMD51LICENSElicense.txtlicense.txttext/plain; charset=utf-81748http://bibliotecadigital.udea.edu.co/bitstream/10495/24959/3/license.txt8a4605be74aa9ea9d79846c1fba20a33MD5310495/24959oai:bibliotecadigital.udea.edu.co:10495/249592021-12-10 16:18:23.98Repositorio Institucional Universidad de Antioquiaandres.perez@udea.edu.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 |