dc.creator | Rodríguez Gómez, Alberto | es |
dc.creator | Pereñíguez Rodríguez, Rosa María | es |
dc.creator | Caballero Martínez, Alfonso | es |
dc.date.accessioned | 2022-10-20T10:14:35Z | |
dc.date.available | 2022-10-20T10:14:35Z | |
dc.date.issued | 2017 | |
dc.identifier.citation | Rodríguez Gómez, A., Pereñíguez Rodríguez, R.M. y Caballero Martínez, A. (2017). Understanding the differences in catalytic performance for hydrogen production of Ni and Co supported on mesoporous SBA-15. Catalysis Today, 307, 224-230. https://doi.org/10.1016/j.cattod.2017.02.020. | |
dc.identifier.issn | 0920-5861 | es |
dc.identifier.issn | 1873-4308 | es |
dc.identifier.uri | https://hdl.handle.net/11441/138166 | |
dc.description.abstract | Three mono and bimetallic Nix Co1−x /SBA-15 catalysts (x = 1, 0.5 and 0) with a total metallic content of
10 wt% have been prepared by a deposition–precipitation (DP) method. The catalytic performances on the
dry reforming of methane reaction (DRM) have been determined and correlated with their physical and
chemical state before and after the catalytic reaction. So, while the nickel monometallic system presents
a high activity and stability in the DRM reaction, the Co/SBA-15 catalytic system turns out completely
inactive. For its part, the Ni0.5Co0.5/SBA-15 has initially a catalytic performance similar to the Ni/SBA-
15 monometallic system, but rapidly evolving to an inactive system, therefore resembling the behavior
of the cobalt-based catalyst. The characterization by TEM and in situ XPS techniques has allowed us
to ascribe these differences to the initial state of metallic particles after reduction and their different
evolution under reaction conditions. So, while after reduction both nickel containing Nix Co1−x /SBA-15
catalysts (x = 1 and 0.5) present a well dispersed metallic phase, the cobalt monometallic catalyst yields
big metallic particles with a heterogeneous distribution of sizes. Additionally, unlike the Ni/SBA-15, the
NiCo/SBA-15 system increases during reaction the metallic particle sizes.
Besides indicating that the particle size is a major reason determining the catalytic performances, these
results suggest that in the Ni–Co system both metals form after reduction a bimetallic phase mainly
located inside the mesoporous channels of SBA-15 support. Under DRM reaction conditions, the cobalt
is segregated to the surface of the bimetallic particles, which seems to determine the interaction with
the support surface SBA-15. This feature gives rise to a much less stable metallic phase which suffers an
important sintering process under DRM catalytic conditions.
© 2017 Elsevier B.V. All rights reserved.
1. Introduction
Supported nickel catalytic systems are currently one of the
most important industrial heterogeneous catalysts because its
remarkable performance in a number of economically strategic
processes [1–5]. Among them, the steam reforming of methane
(SRM, CH4 + H2O ↔ 3H2 + CO) can be outlined as the main industrial
process for obtaining hydrogen and synthesis gas, used to syn-
thesize various important chemicals and fuels [6–9]. Although it
is not yet commercially exploited, the dry reforming of methane
(DRM, CH4 + CO2 ↔ 2H2 + 2CO) is an especially interesting reac-
tion that transforms two of the most harmful greenhouse gases,
methane and carbon dioxide, into a mixture of hydrogen and car-
bon monoxide [10–12]. Once again, Ni-based catalysts are the most
∗ Corresponding author.
E-mail address: caballero@us.es (A. Caballero).
widely tested in the literature for this reforming reaction, even
though noble metal based catalysts such as Pt, Ru and Rh are much
more performance toward methane conversion. The principal issue
comes from the fact that Ni typically undergoes severe deactivation
processes, mainly due to coke formation, but also due to sinter-
ing of the metallic phase, generating big metallic particles which
at the same time, favors the coke formation processes [13–17]. As
an alternative to overcome these issues, a number of publications
have shown as the use of bimetallic systems, as the combination of
nickel and cobalt modified the catalytic performance in steam and
dry reforming of methane [18–23]. But, depending on the support
or the preparation methods both effects, improvements and wors-
ening of the efficiency, have been reported. Main reasons explaining
these contradictory findings are probably related with differences
in the interaction of metals with support surface, which has been
recognized as an essential factor affecting the stability of metal
[24–26]. So, a strategy to avoid the growth of metallic particles is
the use of special supports, and in particular mesoporous supports. | es |
dc.description.sponsorship | Ministerio Economía y Competitividad de España (MINECO) y fondos FEDER de la Unión Europea-ENE2011-24412 y CTQ2014-60524-R | es |
dc.format | application/pdf | es |
dc.format.extent | 7 p. | es |
dc.language.iso | eng | es |
dc.publisher | Elsevier | es |
dc.relation.ispartof | Catalysis Today, 307, 224-230. | |
dc.rights | Attribution-NonCommercial-NoDerivatives 4.0 Internacional | * |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-nd/4.0/ | * |
dc.subject | Nickel cobalt catalysts | es |
dc.subject | In situ XPS | es |
dc.subject | Hydrogen production | es |
dc.subject | DRM methane reforming | es |
dc.title | Understanding the differences in catalytic performance for hydrogen production of Ni and Co supported on mesoporous SBA-15 | es |
dc.type | info:eu-repo/semantics/article | es |
dcterms.identifier | https://ror.org/03yxnpp24 | |
dc.type.version | info:eu-repo/semantics/submittedVersion | es |
dc.rights.accessRights | info:eu-repo/semantics/openAccess | es |
dc.contributor.affiliation | Universidad de Sevilla. Departamento de Química Inorgánica | es |
dc.relation.projectID | ENE2011-24412 | es |
dc.relation.projectID | CTQ2014-60524-R | es |
dc.relation.publisherversion | https://doi.org/10.1016/j.cattod.2017.02.020 | es |
dc.identifier.doi | 10.1016/j.cattod.2017.02.020 | es |
dc.journaltitle | Catalysis Today | es |
dc.publication.volumen | 307 | es |
dc.publication.initialPage | 224 | es |
dc.publication.endPage | 230 | es |
dc.contributor.funder | Ministerio de Economía y Competitividad (MINECO). España | es |
dc.contributor.funder | European Commission (EC). Fondo Europeo de Desarrollo Regional (FEDER) | es |