K. Stawicka
CatalysisTodayxxx(xxxx)xxx–xxx
transfer between O2− and Ce3+ or Ce4+, respectively. The intensity of
the first band decreased, while the second one increased in comparison
to those in the spectrum of Ce/MCF-14. As a consequence, the surface
ratio of Ce3+/Ce3++Ce4+ decreased by 47% for Mel/Ce/MCF-14
(from 0.41 to 0.22). Consequently, the ratio of oxygen vacancies on the
surface of Mel/Ce/MCF-14 also decreased from 0.80 to 0.50. Further-
more, the position of the bands typical of oxygen in oxygen vacancies
(534.2 eV) and lattice oxygen in metal oxides (530.2 eV) was shifted to
higher BE (from 534.0 eV and 529.7 eV for Ce/MCF-14, respectively)
after melamine loading into Ce/MCF-14. A similar phenomenon was
observed for Mel/Nb/MCF-14. The differences which appeared for Mel/
Ce/MCF-14 indicated that melamine played a role of an electron-
withdrawing modifier, which caused the change in oxidation state of
surface cerium species from +3 to +4 (XPS analyses only the surface of
the materials). It is well known that cerium cations in defected cerium
oxide can exist in two forms, in a more stable tetravalent state and
trivalent state having the deficiency of positive charge compensated by
oxygen vacancies [30]. Experimental studies have shown that the
highly mobile lattice oxygen available at the surface of ceria together
with the oxygen vacancies are responsible for the transfer of electrons
in the fluorite structure of ceria [31]. Ce3+ has one electron in the 4f
orbital and this electron is mobile [32]. The close neighborhood of
melamine with resonate structure of heterocyclic ring bonded with
three amine species to cerium oxide in Mel/Ce/MCF-14 caused the
migration of mobile electrons from the surface of ceria to melamine. As
a result the very unstable Ce3+ cations in Mel/Ce/MCF-14 were im-
mediately transformed into Ce4+ state. At the same time the number of
oxygen vacancies and lattice oxygen on the surface of Mel/Ce/MCF-14
was changed.
however it undergoes sublimation at temperatures below its melting
point [33]. The DTG curves presented the maxima of the first mass loss
at 324 °C for Mel/MCF, 329 °C for Mel/Ce/MCF-14 and 335 °C for Mel/
Nb/MCF-14. These temperatures are close to the melting point of
melamine, thus they could be correlated with the sublimation of un-
reacted form of this modifier. The second less intense mass loss ob-
served in the DTG curves has its maximum at 476 °C for Mel/Ce/MCF-
14 and at 556 °C for Mel/Nb/MCF-14, while for Mel/MCF a broad
maximum corresponding to mass loss was detected. This mass loss
might be linked to the decomposition of melamine anchored via a
propyl chain of ClPTMS to the supports (Scheme 1). The formed che-
mical bonding between these two compounds could increase the mel-
amine stability and thus could be responsible for the shift of the tem-
perature of its decomposition to the higher value.
The temperature of the maximum that corresponds to the decom-
position of melamine is an indicator of the modifier stability. It is visible
that melamine was more stable on the sample containing niobium than
on that with cerium species. The temperature of melamine decom-
position was higher by 6 °C for the first mass loss (329 °C in comparison
to 335 °C) and by 80 °C for the second mass loss (476 °C compared to
556 °C). The visible difference between Mel/Ce/MCF-14 and Mel/Nb/
MCF-14 might be caused by the change in the oxidation state of cerium
species in Mel/Ce/MCF-14 after melamine anchoring. A similar phe-
nomenon of decreasing stability of anchored basic modifier in cerium
modified silicas in comparison to niobiosilicates was observed for the
samples modified with imidazole species [3].
3.2. Results of the Knoevenagel condensation
It has been already reported that the Knoevenagel condensation
between aldehydes and active methylenes proceeds efficiently in the
presence of catalysts which exhibit base or acid-base properties [9].
Thus, the synthesis of catalysts containingmelamine, as a basic modi-
fier, and different supports to which it was anchored, such as MCF, Nb/
MCF-14 and Ce/MCF-14, seems to be the appropriate. Melamine con-
tains a high number of basic nitrogen species, which could play a role of
active sites in the Knoevenagel condensation, while the used supports
exhibit different properties (acid or basic one) and thus they can affect
the efficiency of melamine loading and its basicity strength. The per-
formed reactions between benzaldehyde and malononitrile, illustrated
in Scheme 2, allowed to support some conclusions drawn from the
structural/textural characterization and chemical composition of the
synthesized samples. Moreover, the above reactions provided the in-
formation that helped explain the differences in the strength of basicity
of melamine anchored to the silica and metalosilicates.
The results of the Knoevenagel condensation between benzaldehyde
and malononitrile in the presence of the synthesized samples are given
in Fig. 8. It is important to note that the selectivity of the reaction was
100% to the main product, benzylidenemalononitrile. It evidenced that
anchoring of melamine to MCF, Nb/MCF-14 and Ce/MCF-14 caused a
significant increase in the activity of benzaldehyde conversion in
comparison to the activity of silica and metalosilicate supports. It is
worth noting that melamine was not detected in the reaction mixtures
of Mel/MCF, Mel/Nb/MCF-14 and Mel/Ce/MCF-14 by GC–MS. It im-
plies that melamine did not leach from these catalysts during the
Knoevenagel condensation. In order to check if the reaction was not
limited by external or internal diffusion, the additional reactions were
performed in which a mixture of benzaldehyde and malononitrile with
Mel/Ce/MCF-14 was stirred at 100 rpm, 200 rpm and 400 rpm. The
obtained results clearly demonstrated that the reactions performed over
the modified metalosilicate were not controlled by external or internal
diffusion because for each reaction a similar benzaldehyde conversion
was obtained, ca 87%. Interestingly, the reaction performed over free
melamine (2 mg) was not so efficient as for samples modified with this
substance. Thus, the role of the support in increasing the basicity
strength of melamine was evidenced. This occurrence might be
3.1.3. The efficiency of melamine loading and its stability
The efficiency of melamine loading can be estimated from the ni-
trogen content. The weight percentage of nitrogen and moles of an-
chored melamine calculated from the elemental analysis data are given
in Table 3. It is evidenced that the effectiveness of melamine anchoring
depends on the composition of the support used. The presence of nio-
bium or cerium in MCF enhanced (more than twice) the modifier
loading. It can be caused by the strong interaction between metal
species and melamine inferred from the UV–vis and XP spectra
(Figs. 3–6). The increase in modifier loading is higher for Nb/MCF-14
than Ce/MCF-14 support. Similar results were obtained in our earlier
paper in which the chemical interaction between niobium species and
imidazole, triazole or aminopropyl species was proved [3]. A similar
interaction can occur with melamine species and thus the visible in-
crease in efficiency of melamine loading in Nb/MCF-14 support was
obtained.
The metal species in MCF also have an important effect on the
stability of anchored melamine, which is particularly significant for
processes performed in liquid phase, such as the Knoevenagel con-
densation. The stability of anchored melamine was estimated by ther-
mogravimetric analysis whose results are shown in Fig. 7. The TG
curves revealed two mass loss events between 270–390 °C and
400–600 °C. The first greater mass loss could be assigned to the de-
composition of melamine that did not react with anchored ClPTMS. The
chlorine precursor decomposed from MCF and NbMCF-14 at tempera-
ture below 300 °C [14]. Melamine melts and decomposes at 347 °C,
Table 3
The melamine loading on silica and metalosilicate supports (based on elemental
analysis).
Catalyst
N, wt.%
Melamine, mmol/g
Mel/MCF
Mel/Ce/MCF-14
Mel/Nb/MCF -14
13.1
41.2
44.2
2.2
4.9
5.3
8