16626 Phys. Chem. Chem. Phys., 2012, 14, 16626–16632 This journal is c the Owner Societies 2012 Cite this: Phys. Chem. Chem. Phys., 2012, 14, 16626–16632 Density functional study of water-gas shift reaction on M 3 O 3x /Cu(111)w Alba B. Vidal ab and Ping Liu* a Received 21st June 2012, Accepted 10th August 2012 DOI: 10.1039/c2cp42091k Density functional theory (DFT) was employed to study the water dissociation and water-gas shift (WGS) reaction on a series of inverse model catalysts, M 3 O 3x /Cu(111) (M = Mg, Ti, Zr, Mo, W; x = 1, 2, 3). It has been found that the WGS reaction on Cu can be facilitated by introducing various oxides to lower the barrier of water dissociation. Accordingly, the calculated reaction energy for water dissociation was used as a scaling descriptor to screen the WGS activity of oxide–Cu model catalysts. Our calculations show that the activity towards water dissociation decreases in a sequence: Mg 3 O 3 /Cu(111) > Zr 3 O 6 /Cu(111) > Ti 3 O 6 /Cu(111) > W 3 O 9 /Cu(111), Mo 3 O 9 /Cu(111). It seems that Mg 3 O 3 /Cu(111) is the best WGS catalyst among the systems studied here, being able to dissociate water with no barrier. During the process, both Cu and oxides participate in the reaction directly. The strong M 3 O 3x –Cu interaction is able to tune the electronic structure of M 3 O 3x and therefore the activity towards water dissociation. Further studies of the overall WGS reaction on Mg 3 O 3 /Cu(111) show that water dissociation may not be the key step to control the WGS reaction on Mg 3 O 3 /Cu(111) and the removal of H from Mg 3 O 3 can be problematic. The strong interaction between H and O from Mg 3 O 3 blocks the O sites for further water dissociation and therefore the WGS reaction. Our study observes a very different behavior of oxide clusters in such small size from the bigger ones supported on Cu(111) and provides new insight into the rational design of the WGS catalysts. I. Introduction The water-gas-shift (WGS) reaction (CO + H 2 O - CO 2 +H 2 ) has attracted considerable interest, due to its potential applications in fuel cells, Fischer–Tropsch processes and hydrogen produc- tion. 1–4 Common industrial catalysts for the WGS (mixtures of Fe–Cr or Zn–Al–Cu oxides) are pyrophoric and normally require lengthy and complex activation steps before usage. 5 Recently, inverse model catalysts of CeO x nanoparticles supported over Au(111) or Cu(111) surfaces have been found to display a superior catalytic activity in the WGS reaction. In particular, the recent study showed that CeO x /Cu(111) is more active than the traditional catalysts, Cu/CeO 2 (111) and Cu/ZnO(0001), towards the WGS reaction, 6 though the corner and edge atoms present in the Cu nanoparticles facilitate the dissociation of water. 7,8 On one hand, the oxide 2 metal interactions can alter the electronic states of the supported oxide and lead to new chemical properties. 6,9 On the other hand, an inverse oxide/metal catalyst allows the reactants to interact with not only metal sites and the metal–oxide interface as in the case of a traditional metal/oxide catalyst, 10 but also defect sites of oxide nanoparticles, which can be very important for the overall conversion. 6,11 By adopting the inverse model, the catalyst can gain activity due to the active participation of oxide in the catalytic reaction. 6,11–13 In our previous study, 14 the oxide chain (b-MO x , M = Zn, Zr, Ti, Mo) deposited on the Cu(111) surface was used as a simplified model to simulate the interface between Cu and relatively big oxide particles observed experimentally under the WGS conditions, which display bulk-like structures. 6 It was found that the calculated reaction energy for water dissociation, the rate-limiting step for the WGS reaction on pure Cu surfaces and nanoparticles, 7,15,16 correlates well with the experimentally measured activity. The high WGS activity of oxide/Cu(111) relies heavily on the direct participation of both oxide and metal sites, where the oxide–Cu interaction plays an important role. The reducible oxides (e.g. ZrO 2 , TiO 2 and MoO 3 ) that are fully oxidized can be reduced due to the interaction with Cu, which help in releasing the bottleneck water dissociation and therefore facilitating the WGS reaction on Cu. In the present study, we move from the previous MO x / Cu(111) system to M 3 O 3x /Cu(111) (M = Mg, Ti, Zr, Mo, W; x = 1, 2, 3), where the oxide trimer is used to model the relatively small oxide particles. Our goal is to gain more insight into the WGS reaction and screening good catalysts using density functional theory (DFT). Extensive studies have shown that for conventional metal/oxide model catalysts, the a Chemistry Department, Brookhaven National Laboratory, Upton, New York 11973, USA. E-mail: [email protected]b Centro de Quı´mica, Instituto Venezolano de Investigaciones Cientı´ficas (IVIC), Apartado 21827, Caracas 1020-A, Venezuela w This article was submitted as part of a collection on Computational Catalysis and Materials for Energy Production, Storage and Utilization. PCCP Dynamic Article Links www.rsc.org/pccp PAPER Downloaded by BNL Research Library on 03 December 2012 Published on 13 August 2012 on http://pubs.rsc.org | doi:10.1039/C2CP42091K View Article Online / Journal Homepage / Table of Contents for this issue
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Density functional study of water-gas shift reaction on M3O(3x)/Cu(111)
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16626 Phys. Chem. Chem. Phys., 2012, 14, 16626–16632 This journal is c the Owner Societies 2012
Mg3O3/Cu(111) seems to be the best WGS catalyst among the
systems studied here, being able to break water with no barrier.
The oxide trimers behave differently from the big oxide clusters
studied previously.14 For the big oxide clusters, the reduction of
oxide has been found as the key to promote the water dissocia-
tion and therefore the WGS reaction on oxide/Cu(111) model
catalysts. In contrast, for the oxide trimers, it is more complex.
In the case of Mo3O9/Cu(111), Mo3O9 is heavily reduced, yet
water dissociation is endothermic. For Mg3O3/Cu(111), the
stable MgO in such small size and unique conformation can
be further oxidized, which facilitate the O–H bond cleavage.
The DOS of metal ions and O 2p near the Fermi level are
essential in this case. In addition, further studies show that
water dissociation is not the key step to control the WGS
reaction on Mg3O3/Cu(111). With the O 2p dominated
conduction band, a strong interaction between O of Mg3O3
and H from water is observed, which leads to a barrierless
water dissociation at the interface ofMg3O3/Cu(111). However, as
a consequence, the removal of H fromMg3O3 can be problematic,
which blocks the O sites for further water dissociation and
therefore the WGS reaction. Our results imply that to achieve
the high WGS activity, the oxides of Cu–oxide nanocatalysts
have to compromise, being able to dissociate water easily, but
still allowing the facile H removal. The particle size of oxide can
be very important for the overall activity. Our study provides
new insight into the design of the WGS catalysts.
Acknowledgements
This research was carried out at Brookhaven National
Laboratory under contract DE-AC02-98CH10886 with the
US Department of Energy, Division of Chemical Sciences.
The DFT calculations were carried out using the computing
facilities at the Center for Functional Nanomaterials at Brookhaven
National Laboratory and National Energy Research Scientific
Computing (NERSC) Center.
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