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plains the first N2 desorption peak. NOad decomposition started
at above 400 K [12], and the Nad formed in this process de-
sorbed as N2 at around 450 K, the second N2 desorption peak.
A similar reaction scheme was proposed by Bradley et al. [11]
for Pt(100).
This specific experiment was difficult to reproduce during
the TP-XPS measurements (due to reaction of Oad with back-
ground gases); thus, a different approach was adopted. An O2
uptake experiment (not shown) on a NH3ad-saturated surface (at
175 K) revealed that O2 could access the surface and dissoci-
ate, even in the presence of a saturated NH3ad layer. We drew on
this finding in an attempt to make NOad. In this particular ex-
periment, a mixed Oad/NH3ad layer was heated in the presence
of 5 × 10−8 mbar O2. Here O2 could replenish the Oad con-
sumed during NHxad dehydrogenation, and as a result Oad was
present throughout the experiment. Fig. 6c shows the results of
this experiment, as observed with XPS.
Comparing these results with those of a similar experiment
in the absence of O2(g) but in the presence of Oad (see Fig. 5)
reveals several differences. The NHad concentration decreased
at a lower temperature in the presence of O2(g), due to the fact
that in this experiment more Oad was available and NHad could
be completely dehydrogenated via reaction with Oad. The for-
mation of NOad was observed only in the presence of O2(g).
This finding is in line with the model presented in the previ-
ous paragraphs; that is, NOad could form only when Oad was
available after all NHxad was dehydrogenated.
3.5. Steady-state NH3 oxidation on Pt(410)
Fig. 7 shows the results obtained during steady-state NH3
oxidation (ratio 1:1). Panels (a) and (b) show the gas-phase
products, and panels (c) and (d) and (e) and (f) show the N 1s
and O 1s components, respectively. Both the results obtained
during heating [(a), (c), and (e)] and during subsequent cooling
[(b), (d), and (f)] are shown. The surface was saturated with Oad
(10 L O2, 200 K) before being exposed to the reaction mixture.
At 250 K, the surface was covered with a mixture of NH3ad
(+NH2ad), NHad, Nad, and NOad. The concentrations of NH3ad
(+NH2ad), NHad, and Nad decreased with increasing temper-
ature. The adsorption of O2 from the gas phase seemed to be
hindered by the NHxad species present on the surface, and all
O
ad that formed on the surface immediately reacted with NHxad
species. This explains why the Oad concentration remained low.
NOad formation was already observed around 250 K. In
the N 1s spectrum, the peak due to NOad was not very well
resolved, due to the presence of several other N-containing
species (especially NH3ad), but it was clearly observed in the
O 1s spectra, being the only peak present at this temperature.
The amount of NOad did not change between 200 and 400 K,
but above 400 K, NO decomposition started (because no Oad
was present, which would otherwise inhibit NOad decomposi-
tion). As a result, the NOad concentration dropped. It is impor-
tant to note that only a part of the Nad formed NOad, whereas
an equal part did not react and was present as Nad.
In the gas phase, both H2O and N2 formation were ob-
served between 400 and 600 K. The N-selectivity of the reac-
tion changed above 600 K from N2(g) to NO(g). The surface
was almost empty at this temperature; that is, the NHxad, NOad,
and Oad concentrations were almost zero. Due to experimental
limitations, we were not able to observe the surface coverage
above this temperature.
The change in N-selectivity was accompanied by a decrease
in H2O(g) formation. According to the overall reaction equa-
tions (1) and (2), more oxygen is needed for the formation of
NO and H2O than for formation of N2 and H2O. The ratio of
1:1 used in this experiment means that only a relatively small
amount of oxygen was available, too little to oxidize all of the
NH3 to NO. As a result, the NH3 conversion dropped above
600 K. In other words, the reaction rate during NO + H2O for-
mation decreased due to a lack of oxygen:
The differentiated total N 1s signal (θNH + θN + θNO, not
x
shown) corresponds rather well to the TPD results obtained
using a low NH3 postexposure; the decreased N 1s intensity
between 300 and 350 K corresponds to the first N2 desorp-
tion peak. A part of the Nad formed NOad, which desorbed/
decomposed between 400 and 500 K. NOad can be clearly ob-
served in both the N 1s and O 1s region above 400 K, where
it was the only species (next to Oad) present. Below 400 K,
determining the exact intensity of the NOad peak is more diffi-
cult, due to the fact that other species (especially NH3ad) over-
lapped with the NOad peak. Therefore, the exact temperature
at which NOad formation started cannot be determined. From
spectra obtained during steady-state NH3 oxidation (see Sec-
tion 3.5), we tentatively conclude that NOad formation started
already at around 200 K. Reflection absorption infrared spec-
troscopy (RAIRS) experiments done by Kim et al. [38] showed
that NOad formation on Pt(100) started at around 275 K.
4NH3 + 3O2 → 2N2 + 6H2O,
4NH3 + 5O2 → 4NO + 6H2O.
(1)
(2)
From the XPS data, we cannot distinguish NOad decomposi-
tion from NOad desorption, because Nad formed during dissoci-
ation immediately desorbed as N2 and was not observed on the
surface. The fact that the NOad concentration dropped at around
450 K and not at around 400 K, the temperature at which NOad
decomposition started (see Ref. [12]), indicates that NOad de-
sorbed rather than decomposed. Experiments done by Bradley
et al. on Pt(100) indicated that a high Oad concentration in-
hibited NOad dissociation [11]. In our experiment, we found
a rather high Oad concentration at around 450 K, so it is very
well possible that it blocked NOad dissociation and that the de-
creased NOad was due to desorption rather than to dissociation.
The cooling branch provides a better source of information
about the steady-state reaction, because non-steady-state ef-
fects, caused by desorption of adsorbates present at low tem-
perature, are absent. Above 400 K, the reaction, as observed
by the gas-phase products, proceeded in the same manner, and
all essential features, including reaction rate, selectivity change
(around 600 K), and starting/stopping of the reaction (around
400 K), were similar for the heating and cooling branches.
The surface composition as a function of temperature was
slightly different in the cooling branch, specifically below