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KETTELER, RANKE, AND SCHLOGL
110
this temperature which finally leads to the single-crystalline
Kx Fe22O34(0001) phase. Slightly before the constant Auger
ratio of this phase is reached, most of the film is still cov-
ered with polycrystalline KFeO2. Only small sections of
Kx Fe22O34(0001) can be seen in large-scale STM images
(Fig. 8). Nevertheless, as the Auger ratio is already very
close to the value of the pure Kx Fe22O34(0001) phase, we
can conclude that a thin KFeO2 film has formed on top
of Kx Fe22O34(0001) instead of thick KFeO2 domains. This
confirms the proposition deduced from XPS, that the deple-
tion of the film goes along with a decrease in the potassium
content in the bulk while the surface remains potassium
rich (12). Both phases are exposed side by side at the sur-
face. These films therefore appear to model the catalytically
active phase quite well, which according to investigations
of the technical catalyst consists of a KFeO2 shell forming
around a core of K2Fe22O34.
The technical dehydrogenation of ethylbenzene is per-
formed in an excess of steam. Water may have two different
functions. It may have an oxidizing impact due to the lib-
eration of oxygen by thermal decomposition into hydrogen
and oxygen at high temperatures. According to the disso-
ciation equilibrium, the partial pressures of O2 and H2 for
1 bar H2O at 870 K are 6.4 × 10−6 and 1.3 × 10−5 mbar,
respectively (5). The oxidizing or reducing impact of water
would thus be close to UHV conditions. On the other hand,
water may react with the potassium iron oxides under for-
mation of KOH, which at this temperature has a consid-
erable vapor pressure and may desorb. Previous XPS ex-
periments showed that the phase transition to KFeO2 and
KFe22O34(0001) occurred at the same temperatures in a
vacuum and in a 10−8-mbar H2O water atmosphere (12);
therefore the mixed KFeO2/KFe22O34(0001) surface struc-
ture shown here may also form at 870 K in water atmo-
sphere. However, formation of the K-rich KFeO2 surface
phase then competes with K removal by KOH formation
and desorption, and its existence therefore depends on its
rate of formation. As the technical catalyst was identified
to consist of KFeO2 and KFe22O34 (21, 23), the removal of
potassium by KOH desorption has to be compensated for
in a dynamic process in which potassium segregates from
the underlying KFe22O34 phase to the surface. In this way,
the KFe22O34 phase serves as a potassium reservoir for the
recovery of the KFeO2 surface phase. The required potas-
5. CONCLUSIONS
Using STM and AES, we investigated the stability ranges
of potassium-promoted iron oxide model catalyst films in
dependence on the annealing temperature and oxygen par-
tial pressure. In agreement with the stability ranges of
potassium-promoted iron oxide model catalyst films pre-
pared on a Pt(111) substrate, we found that the same KFeO2
phase forms at 700 K, while at higher temperatures single-
crystalline Kx Fe22O34(0001) becomes more stable. We see
no effect of the substrate on the stoichiometry or crys-
talline quality of the model catalyst film. The Ru(0001)
substrate enables the growth of thinner closed films than
on Pt(111), leading to sufficient conductivity of the insulat-
ing KFeO2 film to image this surface with STM. At condi-
tions which simulate the technical dehydrogenation reac-
tion, Kx Fe22O34(0001) is partially covered by KFeO2. Both
phases are exposed at the surface. As the same KFeO2
shell around a K2Fe22O34 core was identified for the ac-
tive state in technical catalyst samples (23), our results hint
that the pressure and material gap might be bridged for the
experiments shown here, and for the first time, details of
the surface of the potentially catalytically active phase are
presented.
ACKNOWLEDGMENT
The authors thank Thomas Bunke for experimental assistance.
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