Pd-Ni Core-Shell Nanoparticles
J. Phys. Chem. B, Vol. 109, No. 1, 2005 347
In the case of Pd/Ni nanoparticles, the coexistence of Ni and
NiO in the core allows a perfect lattice accommodation with
MgO (001) in the “cube-on-cube orientation”. The NiO forma-
tion at the interface of Ni/MgO can be explained by the ability
of Pd to dissociate O2, then by the diffusion of atomic oxygen
through the shell.
The outer shape of pure Ni particles observed on MgO(001)
is typical from better wetting than for Pd/MgO, which is
unexpected for pure Ni. The corresponding increase of the
adhesion energy is also explained by the existence of interfacial
NiO that decreases the misfit with MgO.
The adhesion energy calculated21 for various transition metals
on Mg and on O indicates a weak interaction which normally
leads to a more isotropic shape, with reentrance angles at the
interface. So, it seems reasonable to believe that NiO exists at
the interface, which increases the adhesion energy of the cluster.
For the average size (5-7 nm) of our core-shell clusters,
the catalytic activities toward CO oxidation are similar to the
case of pure Pd clusters. As Pd is on the external faces, it
represents an interesting savings of expensive metal. However,
we do not observe an enhancement of reactivity for the core-
shell clusters for the oxidation of CO, in contradiction with the
experiments on four monolayers (ML) of Pd on Ni(110) in the
case of butadiene hydrogenation.7,8 It is interesting to note that
for this reaction, no increase of reactivity was observed on PdNi
alloy particles,22 although the bulk alloys show an increase of
reactivity. It has been recently shown that the enhancement of
catalytic activity was due to a local strain in the Pd top layer in
the case of four ML of Pd on Ni(110).10 A possible explanation
for the absence of enhanced activity of small particles could be
the presence of edges. By HRTEM, it is impossible to quantity
the deformations on the first external layer.
Figure 10. Rate of CO2 production in the reactor, as a function of the
time, during heating from room temperature to 100 °C.
TABLE 1: Reaction Rate at 50% Conversion and
Maximum Reaction Temperature for Each Sample, for Two
Cycles of Reaction
Ni/MgO Ni/MgO Pd/Ni/MgO Pd/Ni/MgO
1
2
1
2
Pd/MgO
0.31
reaction rate
at 50%
0.07
88
0.24
70
conversion
(Torr/min)
maximum
reaction rate
temperature
(°C)
63
References and Notes
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the catalyst. Sample a contains 100% of Pd atoms, b 15% of
Pd and 85% of Ni, and c 100% of Ni.
The respective quantities used for the elaboration of each
sample are given. Sample a was elaborated with 150 mg of
MgO and 39.28 mg of Pd(acac)2. Sample b was elaborated with
150 mg of MgO, 5.55 mg of Pd(acac)2, and 28.3 mg of
Ni(acac)2. Sample c was elaborated with 150 mg of MgO and
32.9 mg of Ni(acac)2.
It is clearly seen that a and b catalysts present similar
behaviors for the oxidation of CO, while c is poorly active and
only at higher temperature. Table 1 clearly shows that deactiva-
tion does not occur in the Pd-Ni catalyst. So, it is clear that
the core-shell structure is stable during the catalytic reaction
and does not alloy in the particles.
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As the reactivities of pure Pd and Pd-Ni particles are very
close, it is evident that the use of core-shell clusters with Pd
outside allows us to save important amounts of Pd.
5. Discussion
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The chemical structure and geometrical deformations in Ni-
Pd core-shell particles supported on MgO have been ex situ
studied by XPS and various techniques of TEM.
XPS indicates the partial oxidation of the Ni in the particles.
This oxidized Ni is at least due to the air transfer, but the partial
oxidation of Ni atoms at the Ni/MgO interface is another
possible explanation.
After air transfer, bimetallic Ni50Pt50 catalysts and pure Ni
supported on SiO220 show the existence of NiO as observed by
HRTEM.
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