Blends of bio-oil/biogas model compounds for high-purity H2 production by sorption enhanced steam reforming (SESR): Experimental study and energy analysis

H2 production by sorption enhanced steam reforming (SESR) of bio-oil/biogas blends was demonstrated in a fluidized bed reactor. It combines steam reforming (SR) with simultaneous CO2 capture by a solid sorbent. SESR was performed on a Pd/Ni-Co catalyst derived from a hydrotalcite-like material (HT)...

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Published in:Chemical Engineering Journal
Main Authors: Rodríguez, S., Capa, Alma, García Fernández, Roberto, Chen, D., Rubiera González, Fernando, Pevida García, Covadonga, Gil Matellanes, María Victoria
Other Authors: Ministerio de Ciencia e Innovación (España), Principado de Asturias
Format: Article in Journal/Newspaper
Language:English
Published: Elsevier 2022
Subjects:
Online Access:http://hdl.handle.net/10261/296479
https://doi.org/10.1016/j.cej.2021.134396
https://doi.org/10.13039/501100004837
https://doi.org/10.13039/100011941
https://api.elsevier.com/content/abstract/scopus_id/85122260699
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spelling ftcsic:oai:digital.csic.es:10261/296479 2024-06-23T07:50:55+00:00 Blends of bio-oil/biogas model compounds for high-purity H2 production by sorption enhanced steam reforming (SESR): Experimental study and energy analysis Rodríguez, S. Capa, Alma García Fernández, Roberto Chen, D. Rubiera González, Fernando Pevida García, Covadonga Gil Matellanes, María Victoria Ministerio de Ciencia e Innovación (España) Principado de Asturias García Fernández, Roberto Rubiera González, Fernando Pevida García, Covadonga Gil Matellanes, María Victoria 2022-03-15 http://hdl.handle.net/10261/296479 https://doi.org/10.1016/j.cej.2021.134396 https://doi.org/10.13039/501100004837 https://doi.org/10.13039/100011941 https://api.elsevier.com/content/abstract/scopus_id/85122260699 en eng Elsevier #PLACEHOLDER_PARENT_METADATA_VALUE# info:eu-repo/grantAgreement/AEI/Plan Estatal de Investigación Científica y Técnica y de Innovación 2013-2016/ENE2017-83530-R/ES/CONVERSION DE BIOGAS EN BIO-HIDROGENO EN UNA SOLA ETAPA: REFORMADO CATALITICO CON CAPTURA INTEGRADA DE CO2/ Chemical Engineering Journal Publisher's version https://doi.org/10.1016/j.cej.2021.134396 Sí Chemical Engineering Journal 432: 134396 (2022) 1385-8947 http://hdl.handle.net/10261/296479 doi:10.1016/j.cej.2021.134396 http://dx.doi.org/10.13039/501100004837 http://dx.doi.org/10.13039/100011941 2-s2.0-85122260699 https://api.elsevier.com/content/abstract/scopus_id/85122260699 open Bio-oil Biogas/Bio-oil blend CO2 capture Energy efficiency Hydrogen Sorption enhanced steam reforming artículo http://purl.org/coar/resource_type/c_6501 2022 ftcsic https://doi.org/10.1016/j.cej.2021.13439610.13039/50110000483710.13039/100011941 2024-05-29T00:01:24Z H2 production by sorption enhanced steam reforming (SESR) of bio-oil/biogas blends was demonstrated in a fluidized bed reactor. It combines steam reforming (SR) with simultaneous CO2 capture by a solid sorbent. SESR was performed on a Pd/Ni-Co catalyst derived from a hydrotalcite-like material (HT) using dolomite as CO2 sorbent. Bio-oil from fast pyrolysis of biomass is a carbon–neutral and renewable energy source with great potential for clean H2 production by steam reforming processes. Biogas is also a promising renewable bio-based resource for hydrogen generation that can be used to increase the H2 production of a biomass-based plant. In turn, it could improve the energy efficiency of the process due to the exothermic reaction of the CO2 contained in biogas with the sorbent. Bio-oil composed of acetic acid and acetone (1/1 mol/mol) and biogas composed of CH4 and CO2 (60/40 vol%) were used as fuels. They were blended (50 wt% bio-oil + 50 wt% CH4) to study the SESR process. Effects of temperature, steam/C molar ratio, and pressure on the process performance were evaluated. SESR results showed an effective reforming of bio-oil/biogas blends and an enhancement in the H2 production and fuel conversion compared to conventional SR. Higher temperature and steam/C ratio, but lower pressure, favored H2 yield and purity. High H2 yield (87.1%) and H2 purity (98.6 vol%) were obtained at 625 °C and 2.5 bar (steam/C molar ratio three times higher than the stoichiometric value). The thermodynamic energy analysis of the SESR of bio-oil/biogas blends rendered 1.34% higher cold gas efficiency (CGE) than bio-oil SESR. The authors thank Franefoss Miljøkalk AS (Norway) for supplying Arctic dolomite. This work was carried out with financial support from the Spanish MICINN (Project ENE2017-83530-R), co-financed by the European Regional Development Fund (ERDF), and from the Gobierno del Principado de Asturias (PCTI, Ref. IDI/2021/000060). S. Rodríguez acknowledges an Introduction to research JAE Intro scholarship, financed by CSIC ... Article in Journal/Newspaper Arctic Digital.CSIC (Spanish National Research Council) Arctic Norway Chemical Engineering Journal 432 134396
institution Open Polar
collection Digital.CSIC (Spanish National Research Council)
op_collection_id ftcsic
language English
topic Bio-oil
Biogas/Bio-oil blend
CO2 capture
Energy efficiency
Hydrogen
Sorption enhanced steam reforming
spellingShingle Bio-oil
Biogas/Bio-oil blend
CO2 capture
Energy efficiency
Hydrogen
Sorption enhanced steam reforming
Rodríguez, S.
Capa, Alma
García Fernández, Roberto
Chen, D.
Rubiera González, Fernando
Pevida García, Covadonga
Gil Matellanes, María Victoria
Blends of bio-oil/biogas model compounds for high-purity H2 production by sorption enhanced steam reforming (SESR): Experimental study and energy analysis
topic_facet Bio-oil
Biogas/Bio-oil blend
CO2 capture
Energy efficiency
Hydrogen
Sorption enhanced steam reforming
description H2 production by sorption enhanced steam reforming (SESR) of bio-oil/biogas blends was demonstrated in a fluidized bed reactor. It combines steam reforming (SR) with simultaneous CO2 capture by a solid sorbent. SESR was performed on a Pd/Ni-Co catalyst derived from a hydrotalcite-like material (HT) using dolomite as CO2 sorbent. Bio-oil from fast pyrolysis of biomass is a carbon–neutral and renewable energy source with great potential for clean H2 production by steam reforming processes. Biogas is also a promising renewable bio-based resource for hydrogen generation that can be used to increase the H2 production of a biomass-based plant. In turn, it could improve the energy efficiency of the process due to the exothermic reaction of the CO2 contained in biogas with the sorbent. Bio-oil composed of acetic acid and acetone (1/1 mol/mol) and biogas composed of CH4 and CO2 (60/40 vol%) were used as fuels. They were blended (50 wt% bio-oil + 50 wt% CH4) to study the SESR process. Effects of temperature, steam/C molar ratio, and pressure on the process performance were evaluated. SESR results showed an effective reforming of bio-oil/biogas blends and an enhancement in the H2 production and fuel conversion compared to conventional SR. Higher temperature and steam/C ratio, but lower pressure, favored H2 yield and purity. High H2 yield (87.1%) and H2 purity (98.6 vol%) were obtained at 625 °C and 2.5 bar (steam/C molar ratio three times higher than the stoichiometric value). The thermodynamic energy analysis of the SESR of bio-oil/biogas blends rendered 1.34% higher cold gas efficiency (CGE) than bio-oil SESR. The authors thank Franefoss Miljøkalk AS (Norway) for supplying Arctic dolomite. This work was carried out with financial support from the Spanish MICINN (Project ENE2017-83530-R), co-financed by the European Regional Development Fund (ERDF), and from the Gobierno del Principado de Asturias (PCTI, Ref. IDI/2021/000060). S. Rodríguez acknowledges an Introduction to research JAE Intro scholarship, financed by CSIC ...
author2 Ministerio de Ciencia e Innovación (España)
Principado de Asturias
García Fernández, Roberto
Rubiera González, Fernando
Pevida García, Covadonga
Gil Matellanes, María Victoria
format Article in Journal/Newspaper
author Rodríguez, S.
Capa, Alma
García Fernández, Roberto
Chen, D.
Rubiera González, Fernando
Pevida García, Covadonga
Gil Matellanes, María Victoria
author_facet Rodríguez, S.
Capa, Alma
García Fernández, Roberto
Chen, D.
Rubiera González, Fernando
Pevida García, Covadonga
Gil Matellanes, María Victoria
author_sort Rodríguez, S.
title Blends of bio-oil/biogas model compounds for high-purity H2 production by sorption enhanced steam reforming (SESR): Experimental study and energy analysis
title_short Blends of bio-oil/biogas model compounds for high-purity H2 production by sorption enhanced steam reforming (SESR): Experimental study and energy analysis
title_full Blends of bio-oil/biogas model compounds for high-purity H2 production by sorption enhanced steam reforming (SESR): Experimental study and energy analysis
title_fullStr Blends of bio-oil/biogas model compounds for high-purity H2 production by sorption enhanced steam reforming (SESR): Experimental study and energy analysis
title_full_unstemmed Blends of bio-oil/biogas model compounds for high-purity H2 production by sorption enhanced steam reforming (SESR): Experimental study and energy analysis
title_sort blends of bio-oil/biogas model compounds for high-purity h2 production by sorption enhanced steam reforming (sesr): experimental study and energy analysis
publisher Elsevier
publishDate 2022
url http://hdl.handle.net/10261/296479
https://doi.org/10.1016/j.cej.2021.134396
https://doi.org/10.13039/501100004837
https://doi.org/10.13039/100011941
https://api.elsevier.com/content/abstract/scopus_id/85122260699
geographic Arctic
Norway
geographic_facet Arctic
Norway
genre Arctic
genre_facet Arctic
op_relation #PLACEHOLDER_PARENT_METADATA_VALUE#
info:eu-repo/grantAgreement/AEI/Plan Estatal de Investigación Científica y Técnica y de Innovación 2013-2016/ENE2017-83530-R/ES/CONVERSION DE BIOGAS EN BIO-HIDROGENO EN UNA SOLA ETAPA: REFORMADO CATALITICO CON CAPTURA INTEGRADA DE CO2/
Chemical Engineering Journal
Publisher's version
https://doi.org/10.1016/j.cej.2021.134396

Chemical Engineering Journal 432: 134396 (2022)
1385-8947
http://hdl.handle.net/10261/296479
doi:10.1016/j.cej.2021.134396
http://dx.doi.org/10.13039/501100004837
http://dx.doi.org/10.13039/100011941
2-s2.0-85122260699
https://api.elsevier.com/content/abstract/scopus_id/85122260699
op_rights open
op_doi https://doi.org/10.1016/j.cej.2021.13439610.13039/50110000483710.13039/100011941
container_title Chemical Engineering Journal
container_volume 432
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