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after 24 h at 408C (83%, entry 3). Catalyst 4 showed the high-
est activity. Under standard conditions, complete reduction
along with deoxygenation was observed, and 4-ethyl-toluene
(17) was quantitatively formed (entry 4). Even after 6 h reaction
time, a substantial amount of fully reduced and deoxygenated
17 was formed when 4 was used as a catalyst (entry 5). A
slightly lower activity was noted for hybrid system 5. Hence,
running hydrogenation with 5 at 408C for 24 h provided the
deoxygenated compound 17 as a minor product along with
15 and small amounts of 16 (entry 9). Stopping the reaction
after 6 h did not lead to any deoxygenation product 17
(entry 10). As a control experiment, hydrogenation was repeat-
ed using commercially available Pd/C, and 4-ethylbenzalde-
hyde (15) was formed as the major product along with the
semihydrogenation product 14 (entry 11). With Pd/SiO2, in
which the PdNPs are present as agglomerates and are not
bound to SiO2, 4-ethylbenzaldehyde (15) was quantitatively
formed (entry 12).
22 h in the absence of 4. It was observed that the semihydro-
genation product was formed in 55% yield after 2 h at an
overall conversion of 55% (Table 2, entry 6). However, even
after the removal of the catalyst the reaction proceeded to de-
liver product 15 in a quantitative yield after 24 h, clearly reveal-
ing that Pd leached out of 4 into the solution during the initial
2 h reaction period and that the leached Pd species is active
(entry 7). Leaching was also noted for hybrid 3 where total re-
flection X-ray fluorescence analysis (TXRF)[27] revealed that a sig-
nificant amount of palladium leached out from the surface
into the solution within 2 h (462.4 mgLÀ1, see the Supporting
Information for detailed analysis). A further control experiment
was conducted by using the precursor salt (neat PdCl2) as the
catalyst. In the course of the reaction, the yellow solution
turned black, indicating a reduction of the palladium salt to
Pd0 under the applied reaction conditions. Not surprisingly, it
was observed that the fully reduced and deoxygenated prod-
uct 17 was formed after 24 under these conditions (entry 8).
This result showed that Pd nanoparticles are formed from Pd
salts under the applied reducing conditions. However, the reac-
tivity of these PdNPs is different than the reactivity of the NPs
derived from hybrid 4.
Because one of the main advantages of heterogeneous cat-
alysis is the recyclability of the catalyst system, recycling ex-
periments were conducted. We tried several methods, includ-
ing filtration and centrifugation, to recover the silica particles
after successful hydrogenation in DCM. The method of choice
for catalyst separation and recovery turned out to be centrifug-
ing of the reaction mixture using Teflonꢃ vials. By using this
technique, we were able to recycle catalyst 2 four times (see
the experimental section below).
From these studies we can conclude that the highest activity
and hence the lowest selectivity for semihydrogenation is ach-
ieved for catalyst systems 4 and 5 (bearing methyl sulfoxide li-
gands), leading to aldehyde reduction and also deoxygenation.
Notably, in these two hybrid materials the mean diameter of
the PdNPs lies at around 30 nm. The least active catalyst 2 is
composed of PdNPs with the largest mean diameter (around
40 nm). To our surprise, hybrid 3 with PdNPs showing the
smallest mean diameter of around 25 nm turned out to be less
active than systems 4 and 5.
Next we investigated solvent effects on the hydrogenation
of 4-vinylbenzaldehyde. To this end, reductions were repeated
in MeOH as a solvent. We found that activity of all catalyst sys-
tems was higher in this polar protic solvent, and therefore hy-
drogenations were conducted under atmospheric pressure of
H2 at room temperature. After 6 h reaction time with catalyst
2, 65% of the semihydrogenation product 14, along with 15
(7%) and unreacted starting material was observed (Table 2,
entry 13). However, extending reaction time to 24 h provided
17 quantitatively (entry 14). Note that catalyst 2 in DCM did
not provide any aldehyde reduction and deoxygenation (com-
pare with entry 1).
Hydrogenation of external and internal alkynes
To investigate substrate scope, various alkynes were hydrogen-
ated. Experiments were conducted in MeOH and in DCM. One
major point of interest was the capability of our particles to
semihydrogenate internal alkynes with ideally high Z/E-selectiv-
ity. Results obtained for the reduction of alkynes, which show
different steric and electronic properties, are depicted in
Table 3.
Again 3 showed lower activity than 2 (Table 2, entry 15), and
the highest activity was noted for system 4 (entry 16). As in
DCM, activity of 5 was lower than that of 4 in MeOH (entry 17).
Interestingly, hydrogenation with Pd/C as the catalyst provided
benzyl alcohol 16 quantitatively (entries 18 and 19). We then
switched to polar aprotic solvents such as EtOAc and THF. The
hydrogenation proceeded faster in EtOAc than in THF (en-
tries 20–22). With Pd/C as a catalyst no significant activity dif-
ference was observed in DCM and THF (entries 11 and 23).
Hence, the order of activity of our hybrid systems with respect
to the tested solvents is as follows: MeOH>EtOAc>THF>
DCM.
Hydrogenation of 1-phenyl-1-propyne in DCM provided fully
reduced propylbenzene quantitatively even with the least reac-
tive catalyst 2 (Table 3, entry 1), and with Pd/C the same result
was obtained (entry 2). Therefore, we tested the sterically more
hindered diphenylacetylene as a substrate. In order to obtain
better conversion, MeOH was chosen as solvent and reactions
were conducted with the more reactive catalysts 3–5, which
showed similar results. Semihydrogenation with high Z selec-
tivity was achieved in these transformations (entries 3–5). Pd/C
was significantly less reactive than the hybrid catalysts 3–5
(entry 6). Ethyl 3-phenyl-propiolate is a reactive substrate, and
hence reductions were performed in DCM with the least reac-
tive catalyst 2. We were pleased to find that only the corre-
sponding semihydrogenation product was identified with com-
plete Z selectivity and good conversion (entry 7). In contrast,
Pd/C as a catalyst in the control experiment under the same
In order to estimate leaching effects, the most active catalyst
4 was employed for 2 h at an atmospheric pressure of hydro-
gen, and the reaction was analyzed. Hybrid catalyst 4 was then
removed by simple filtration, the filtrate was analyzed, and the
hydrogenation of the filtrate was continued for an additional
Chem. Eur. J. 2016, 22, 1 – 11
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