Acetic acid removal from bio-oil on alumina-supported CaO and/or Ag catalysts
- Autores
- Montaña, Maia; Navas, Marisa Belén; Bideberripe, Hernán Pablo; Siri, Guillermo Jorge; Casella, Mónica Laura; Lick, Ileana Daniela
- Año de publicación
- 2017
- Idioma
- inglés
- Tipo de recurso
- documento de conferencia
- Estado
- versión publicada
- Descripción
- Acetic acid removal from bio-oil by catalytic processes was investigated over alumina-supported calcium oxide and silver catalysts. A 20 wt.% CaO supported on γ-Al2O3 system (CaO-Al) was prepared by precipitation of CaCO3 followed by calcination to obtain the supported oxide. A 10 wt.% Ag catalyst was prepared by impregnation on CaO-Al as support (Ag/CaO-Al). The conversion of acetic acid was tested in batch micro-reactors, with the purpose of screening the reaction conditions. Both CaO-Al and Ag/CaO-Al were active for the reaction, with the contribution of the metal phase increasing the conversion with respect to CaO-Al (75.7% vs. 58% at 200 °C). The Ag/CaO-Al catalyst was also tested in a batch reactor at two pressures, achieving a conversion of acetic acid of 97.5% at the lowest pressure (280 kPa). Based on the results, it is postulated that multiple pathways (catalytic decarboxylation, neutralization and ketonization) are responsible for acetic acid conversion.
Centro de Investigación y Desarrollo en Ciencias Aplicadas - Materia
-
Química
Acetic acid
Bio-oil
Catalytic processes - Nivel de accesibilidad
- acceso abierto
- Condiciones de uso
- http://creativecommons.org/licenses/by-nc-sa/4.0/
- Repositorio
.jpg)
- Institución
- Universidad Nacional de La Plata
- OAI Identificador
- oai:sedici.unlp.edu.ar:10915/146849
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Acetic acid removal from bio-oil on alumina-supported CaO and/or Ag catalystsMontaña, MaiaNavas, Marisa BelénBideberripe, Hernán PabloSiri, Guillermo JorgeCasella, Mónica LauraLick, Ileana DanielaQuímicaAcetic acidBio-oilCatalytic processesAcetic acid removal from bio-oil by catalytic processes was investigated over alumina-supported calcium oxide and silver catalysts. A 20 wt.% CaO supported on γ-Al2O3 system (CaO-Al) was prepared by precipitation of CaCO3 followed by calcination to obtain the supported oxide. A 10 wt.% Ag catalyst was prepared by impregnation on CaO-Al as support (Ag/CaO-Al). The conversion of acetic acid was tested in batch micro-reactors, with the purpose of screening the reaction conditions. Both CaO-Al and Ag/CaO-Al were active for the reaction, with the contribution of the metal phase increasing the conversion with respect to CaO-Al (75.7% vs. 58% at 200 °C). The Ag/CaO-Al catalyst was also tested in a batch reactor at two pressures, achieving a conversion of acetic acid of 97.5% at the lowest pressure (280 kPa). Based on the results, it is postulated that multiple pathways (catalytic decarboxylation, neutralization and ketonization) are responsible for acetic acid conversion.Centro de Investigación y Desarrollo en Ciencias Aplicadas2017-08info:eu-repo/semantics/conferenceObjectinfo:eu-repo/semantics/publishedVersionObjeto de conferenciahttp://purl.org/coar/resource_type/c_5794info:ar-repo/semantics/documentoDeConferenciaapplication/pdfhttp://sedici.unlp.edu.ar/handle/10915/146849enginfo:eu-repo/semantics/openAccesshttp://creativecommons.org/licenses/by-nc-sa/4.0/Creative Commons Attribution-NonCommercial-ShareAlike 4.0 International (CC BY-NC-SA 4.0)reponame:SEDICI (UNLP)instname:Universidad Nacional de La Platainstacron:UNLP2025-10-22T17:18:25Zoai:sedici.unlp.edu.ar:10915/146849Institucionalhttp://sedici.unlp.edu.ar/Universidad públicaNo correspondehttp://sedici.unlp.edu.ar/oai/snrdalira@sedici.unlp.edu.arArgentinaNo correspondeNo correspondeNo correspondeopendoar:13292025-10-22 17:18:26.03SEDICI (UNLP) - Universidad Nacional de La Platafalse |
| dc.title.none.fl_str_mv |
Acetic acid removal from bio-oil on alumina-supported CaO and/or Ag catalysts |
| title |
Acetic acid removal from bio-oil on alumina-supported CaO and/or Ag catalysts |
| spellingShingle |
Acetic acid removal from bio-oil on alumina-supported CaO and/or Ag catalysts Montaña, Maia Química Acetic acid Bio-oil Catalytic processes |
| title_short |
Acetic acid removal from bio-oil on alumina-supported CaO and/or Ag catalysts |
| title_full |
Acetic acid removal from bio-oil on alumina-supported CaO and/or Ag catalysts |
| title_fullStr |
Acetic acid removal from bio-oil on alumina-supported CaO and/or Ag catalysts |
| title_full_unstemmed |
Acetic acid removal from bio-oil on alumina-supported CaO and/or Ag catalysts |
| title_sort |
Acetic acid removal from bio-oil on alumina-supported CaO and/or Ag catalysts |
| dc.creator.none.fl_str_mv |
Montaña, Maia Navas, Marisa Belén Bideberripe, Hernán Pablo Siri, Guillermo Jorge Casella, Mónica Laura Lick, Ileana Daniela |
| author |
Montaña, Maia |
| author_facet |
Montaña, Maia Navas, Marisa Belén Bideberripe, Hernán Pablo Siri, Guillermo Jorge Casella, Mónica Laura Lick, Ileana Daniela |
| author_role |
author |
| author2 |
Navas, Marisa Belén Bideberripe, Hernán Pablo Siri, Guillermo Jorge Casella, Mónica Laura Lick, Ileana Daniela |
| author2_role |
author author author author author |
| dc.subject.none.fl_str_mv |
Química Acetic acid Bio-oil Catalytic processes |
| topic |
Química Acetic acid Bio-oil Catalytic processes |
| dc.description.none.fl_txt_mv |
Acetic acid removal from bio-oil by catalytic processes was investigated over alumina-supported calcium oxide and silver catalysts. A 20 wt.% CaO supported on γ-Al2O3 system (CaO-Al) was prepared by precipitation of CaCO3 followed by calcination to obtain the supported oxide. A 10 wt.% Ag catalyst was prepared by impregnation on CaO-Al as support (Ag/CaO-Al). The conversion of acetic acid was tested in batch micro-reactors, with the purpose of screening the reaction conditions. Both CaO-Al and Ag/CaO-Al were active for the reaction, with the contribution of the metal phase increasing the conversion with respect to CaO-Al (75.7% vs. 58% at 200 °C). The Ag/CaO-Al catalyst was also tested in a batch reactor at two pressures, achieving a conversion of acetic acid of 97.5% at the lowest pressure (280 kPa). Based on the results, it is postulated that multiple pathways (catalytic decarboxylation, neutralization and ketonization) are responsible for acetic acid conversion. Centro de Investigación y Desarrollo en Ciencias Aplicadas |
| description |
Acetic acid removal from bio-oil by catalytic processes was investigated over alumina-supported calcium oxide and silver catalysts. A 20 wt.% CaO supported on γ-Al2O3 system (CaO-Al) was prepared by precipitation of CaCO3 followed by calcination to obtain the supported oxide. A 10 wt.% Ag catalyst was prepared by impregnation on CaO-Al as support (Ag/CaO-Al). The conversion of acetic acid was tested in batch micro-reactors, with the purpose of screening the reaction conditions. Both CaO-Al and Ag/CaO-Al were active for the reaction, with the contribution of the metal phase increasing the conversion with respect to CaO-Al (75.7% vs. 58% at 200 °C). The Ag/CaO-Al catalyst was also tested in a batch reactor at two pressures, achieving a conversion of acetic acid of 97.5% at the lowest pressure (280 kPa). Based on the results, it is postulated that multiple pathways (catalytic decarboxylation, neutralization and ketonization) are responsible for acetic acid conversion. |
| publishDate |
2017 |
| dc.date.none.fl_str_mv |
2017-08 |
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info:eu-repo/semantics/conferenceObject info:eu-repo/semantics/publishedVersion Objeto de conferencia http://purl.org/coar/resource_type/c_5794 info:ar-repo/semantics/documentoDeConferencia |
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http://sedici.unlp.edu.ar/handle/10915/146849 |
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eng |
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eng |
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