M. Santhosh Kumar et al. / Journal of Catalysis 239 (2006) 173–186
185
the oxide clusters. In contrast to NH3-SCR, where they are se-
lective up to temperatures of about 700 K, FexOy agglomerates
play a detrimental role in isobutane-SCR because they oxidize
the isobutane reductant to COx at temperatures as low as 623 K.
This is evident from carbonyl-containing species detected by
in situ FTIR preferentially on Fe-Z(1.2) but not on Fe-Z(0.3)
content ꢁ0.3 wt%) represents isolated reduction-resistant and
3
+
thus probably active Fe sites. Permanent reduction of isolated
3+
Fe was more pronounced during SCR with i-butane than with
NH , which may be why the catalysts were markedly less active
3
in the former case.
In contrast to certain isolated Fe3 sites, oxidic clusters of
+
(
Fig. 9). Recently we showed that the commercial H-ZSM-5
different sizes, reflected by UV–vis signals above 300 nm and
ꢀ
matrix used for the preparation of the Fe-Z samples contains
about 500 ppm of Fe impurities in the form of clusters rather
than as isolated sites [17], demonstrating why a carbonyl band
an EPR line at g ≈ 2 (in samples with Fe content ꢁ0.6 wt%),
remained essentially trivalent during SCR of NO with both NH
and i-butane, due to their slow reduction and very rapid re-
oxidation. Consequently, these species have a higher oxidizing
3
−1
at 1690 cm is also observed on this sample (Fig. 9).
power than isolated Fe3 sites. This leads to undesired total ox-
idation of the reducing agent at higher temperatures, an effect
that is most detrimental for i-butane but not as crucial for NH3.
As a rule for knowledge-based catalyst design, the results
+
Carbonyl-containing adsorbates are considered as intermedi-
ates in the total oxidation of isobutane. As a result of this unse-
lective oxidation behavior of the FexOy agglomerates, NO con-
version decreases dramatically above 600 K, and this undesired
effect becomes more and more pronounced as the content of
oxide clusters increases with increasing Fe content [10]. In con-
trast, the formation of C/N-containing species, such as nitriles,
cyanates, and isocyanates, seems to proceed preferentially on
isolated Fe sites, the amount of which increases from sample
Fe-Z(0.3) to sample Fe-Z(1.2) (Fig. 9). Some have claimed that
these species are active intermediates in NOx reduction [35,38–
of this study indicate that for both NH - and i-butane-SCR,
3
the concentration of accessible Fe3 that can participate in a
reversible redox cycle should be maximized, whereas the for-
mation of Fe O clusters must be completely (i-butane-SCR)
+
x
y
or largely (NH -SCR) avoided.
3
Acknowledgments
4
0], which can be considered another reason for the superior
catalytic performance of isolated Fe sites in isobutane-SCR.
We thank the Deutsche Forschungsgemeinschaft for finan-
cial support (grants BR 1380/7-2 and Gr 1447/7-2).
4
. Conclusion
References
A series of Fe-ZSM-5 catalysts with a tailored dispersion
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[
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ꢀ
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[
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