dc.creator | Megías Sayago, Cristina | es |
dc.creator | Santos Muñoz, José Luis | es |
dc.creator | Ammari, Fatima | es |
dc.creator | Chenouf, Meriem | es |
dc.creator | Ivanova, Svetlana | es |
dc.creator | Centeno Gallego, Miguel Ángel | es |
dc.creator | Odriozola Gordón, José Antonio | es |
dc.date.accessioned | 2022-10-20T12:00:17Z | |
dc.date.available | 2022-10-20T12:00:17Z | |
dc.date.issued | 2017 | |
dc.identifier.citation | Megías Sayago, C., Santos Muñoz, J.L., Ammari, F., Chenouf, M., Ivanova, S., Centeno Gallego, M.Á. y Odriozola Gordón, J.A. (2017). Influence of gold particle size in Au/C catalysts for base-free oxidation of glucose. Catalysis Today, 306, 183-190. https://doi.org/10.1016/j.cattod.2017.01.007. | |
dc.identifier.issn | 0920-5861 | es |
dc.identifier.issn | 1873-4308 | es |
dc.identifier.uri | https://hdl.handle.net/11441/138192 | |
dc.description.abstract | A series of gold colloids were prepared and immobilized on commercial activated carbon. The influence of
the colloid preparation and stability were studied and related to the gold particle size in the final catalyst.
The catalysts show an important activity in the glucose to gluconic acid oxidation reaction, leading to
gluconic acid yield close to 90% in base free mild conditions (0.1 MPa O2 and 40 ◦C). The size-activity
correlation and probable mechanism were also discussed. Finally, the viability of the catalyst was tested
by recycling it up to four times.
© 2017 Elsevier B.V. All rights reserved.
1. Introduction
Biorefinery, defined as the efficient transformation of renew-
able materials to fuels and intermediate chemicals, and associated
to environmental and economic benefits, has driven the research
in this area to notable increase in the last decades [1–4]. Within
the renewable materials the vegetal biomass, mostly constituted
by carbohydrates, represents around 75% of the total renewable
biomass [5]. Among the carbohydrates represented in this biomass
the cellulose remains the most attractive fuel precursor, mainly due
to its low price, chemical purity and because it is formed only by one
monomer – glucose [6]. After cellulose depolimerazion the subse-
quent transformation of glucose to valuable compounds involves a
variety of processes such as hydrogenation [7], isomerization [8],
dehydration [9] and oxidation [10]. Every single mentioned pro-
cess or a combination of them lead to the formation of different
‘platform chemicals’. As an example, the D-Gluconic acid, derived
from the oxidation of glucose at anomeric position, results to be an
useful food additive and raw material for drugs and biodegradable
polymers manufacturing [11,12]. Industrially D-Gluconic acid is
∗ Corresponding author.
E-mail address: cristina.megias@icmse.csic.es (C. Megías-Sayago).
produced by enzymatic fermentation process [13,14] for which the
principal inconvenient for sustainable large-scale production is the
necessity of a neutralization step in order to avoid enzymes deac-
tivation by the produced acid [15]. This problem could be solved
either by using a base or by the substitution of the enzymes with a
heterogeneous catalyst able to oxidize glucose under mild base-free
conditions by using either O2 or H2O2 as oxidants [16–19].
Although the use of base (NaOH and a relatively high pH of
around 9-9.5) results in increase of heterogeneous catalyst’s activ-
ity due to particle size stabilization and metal leaching suppression
[20–22], a decrease in the selectivity to gluconic acid is often
observed caused by the glucose to fructose isomerization process
[23]. In addition, the formation of gluconate salt instead of pure glu-
conic acid occurs and entails the need of cost effective post-reaction
treatment to obtain the target acid. Therefore, a simple base-free
heterogeneously catalyzed process able to produce selectively glu-
conic acid and avoiding the problems of particle size sintering and
metal leaching is highly desirable.
Within the catalyst’s candidates for such a process, the most
promising alternative is nanometric gold. Glucose oxidation has
been carried out over both unsupported [24,25] and supported
[20,26] gold catalysts with good results in activity and selectiv-
ity; however, some issues must be addressed in order to improve
the catalytic system. Various studies reported the base-free aero-
https://doi.org/10.1016/j.cattod.2017.01.007
0920-5861/© 2017 Elsevier B.V. All rights reserved. | es |
dc.description.sponsorship | Ministerio de Economía y Competitividad de España (MINECO) y fondos FEDER de la Unión Europea-ENE2013-47880-C3-2-R | es |
dc.format | application/pdf | es |
dc.format.extent | 8 p. | es |
dc.language.iso | eng | es |
dc.publisher | Elsevier | es |
dc.relation.ispartof | Catalysis Today, 306, 183-190. | |
dc.rights | Attribution-NonCommercial-NoDerivatives 4.0 Internacional | |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-nd/4.0/ | |
dc.subject | Gold catalysts | es |
dc.subject | Carbon-supported catalysts | es |
dc.subject | Glucose oxidation | es |
dc.subject | Liquid-phase oxidation | es |
dc.subject | Biomass conversion | es |
dc.title | Influence of gold particle size in Au/C catalysts for base-free oxidation of glucose | es |
dc.type | info:eu-repo/semantics/article | es |
dcterms.identifier | https://ror.org/03yxnpp24 | |
dc.type.version | info:eu-repo/semantics/acceptedVersion | es |
dc.rights.accessRights | info:eu-repo/semantics/openAccess | es |
dc.contributor.affiliation | Universidad de Sevilla. Departamento de Química Inorgánica | es |
dc.relation.projectID | ENE2013-47880-C3-2-R | es |
dc.relation.publisherversion | https://doi.org/10.1016/j.cattod.2017.01.007 | es |
dc.identifier.doi | 10.1016/j.cattod.2017.01.007 | es |
dc.journaltitle | Catalysis Today | es |
dc.publication.volumen | 306 | es |
dc.publication.initialPage | 183 | es |
dc.publication.endPage | 190 | 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 |